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ADVANCED AND CONTEMPORARY STUDIES IN ENGINEERING

CENGİZ, Mehmet Sait

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ADV ANCED AND CONTEMPORAR Y STUDIES IN ENGINEERING Editor: Assoc. Prof. Mehmet Sait CENGİZ Advanced and Contemporary Studies in Engineering Editor: Assoc. Prof. Mehmet Sait CENGİZ Editor in chief: Berkan Balpetek Cover and Page Design: Duvar Design Printing : December -2023 Publisher Certificate No: 49837 ISBN: 978-625-6585-69-0 © Duvar Y ayınları 853 Sokak No:13 P .10 Kemeraltı-Konak/İzmir T el: 0 232 484 88 68 www .duvaryayinlari.com [email protected] TABLE OF CONTEN TS Chapter 1.................... 7 The Effects of Using Superplasticizer and Pozzolans at Different Ratios on the Rheological Properties of Self-Compact ing Cement Paste Fethi İŞSEVER , M. Hulusi ÖZKUL , Sadık VAROLGÜ NEŞ Chapter 2................. .... 33 Formation Mechanisms an d Deposition Processes of Pyroclastic Rocks Abdullah SAR , Mehmet Al i ERTÜRK Chapter 3................. .... 50 Effects of Operating Param eters on NOX Emıssıons in Diesel En gines Adem TÜYLÜ , Kub ilay HAN , Yasin AKIN Chapter 5.....................64 In -Situ Hydrogen Peroxide and Hydrogen Production in Wastewater Treatment with Fenton-Fenton Like Oxidation Ay şe Elif ATEŞ , Sinan ATEŞ Chapter 4................. .... 77 Modeling the COD removal of DMS O-Con taining Wastewater from the Pharmaceutical Industry Using Photo -Fenton Oxidation with the Response Surface Method Ay ş e Elif ATE Ş Chapter 6.....................88 Energy Management Strategies and Techniques in Hybrid and Electric Vehicles Bayram KILIÇ , Emr e ARABACI Chapter 7.....................97 ENVIRONMENTAL BIOTECHNOLOGY PROCESSES IN THE TREATMENT OF LIVESTOCK WASTES B üş ra YAYLI 1 İlker KILIÇ 2 Chapter 8.....................112 Environmental Impact Assessment Of Laying Hen Production Systems Through Life Cycle Assessment B üş ra YAYLI , İlker KILIÇ Chapter 9.....................132 Material Strength Tests With Electrical Approach Emrah KAPLAN , Dursun EKMEKCI Chapter 10 152 Effects of the Use of Nanofluids in Solar Collectors on Thermal- Hydraulic Performance Fatma OFLAZ Chapter 11.....................162 The Effect of Using Wire Coil Inserts on Heat Transfer Enhancement in Tube Flow Fatma OFLAZ Chapter 12.....................173 Urban Climate Change Resilience Gökhan KARA , Esma Gül EMECEN KARA Chapter 13.....................186 Investigation Of Chaotic Behavior In A 3D Nonlinear System With Exponential Function Haris CALGAN , Metin DEMİ RTAS Chapter 14.....................196 Investigation of the Phase Development of NBT, KB T and BT Lead-Free Piezoelectric Ceramics Hatice Şule ÇOBAN TET İK Chapter 15.....................210 SMALL HORIZONTAL AXIS WIND TURBINE: A CASE STUDY Kemal ERM İŞ , Mehmet ÇALIŞKAN , Mur at KARABEKTA Ş 3 Chapter 16.....................230 The Role of Sensors and Encoders in Exoskeleton Technologies Melih CANLIDİNÇ , Musta fa GÜ LE Ş EN Chapter 17.....................242 Effects of Climate Change on Water Resources, Soil Resources and Weather Events Sümeyye ADALI , Melike YALIL I KILIÇ Chapter 18.....................254 The Rehabilitation Of Open Solid Waste Dumping Areas Fatma ALFARRA , Mirac Nur CİNER , H. Kurtulus Ozca n Chapter 19 .....................284 Criteria for Determining Parameters in Metal Powder Production by Gas Atomization Mustafa GÜ LE Ş EN , Osman S elim Kİ BAR Chapter 20 .....................296 The Response Of Soil Properties To Global Climate Change Fatma Olcay TOPAÇ Chapter 21.....................311 Modeling and Simulation of Fuzzy Logic MPPT Method for Photovoltaic DC/DC Boost Converter Yasemin ÖNAL Chapter 22.....................328 Results and Suggestions Regarding Cutting Forces, Surface Roughness And Tool Wear In Turning Inconel 718 With Different Cutting Tools Abdullah ALTIN Chapter 23.....................337 Contact Mechanics of Functionally Graded Orthotropic Materials: Semi-Analytical Solution for Rigid Punch Loading Erdal ÖNER , Ahmed Wasfi Hasa n AL-QADO Chapter 25.....................348 Blockchain Technology and Consensus Algorithms İrfan SARIYILDIZ , Mehta p KÖSE ULUKÖK Chapter 25.....................357 A Review on the Design, Modeling and Optimization of Fused Deposition Process Printing Parameters Melih SAVRAN Chapter 27 .....................385 Analyzing and Fixing the Grasshopper Optimization Algorithm Okkes Tolga ALTINOZ Chapter 27.....................396 Health Problem Pre-Application System Recommendation for International Transportation Personnel and Passengers and Evaluation of The Proposed System Orhan GÖNEL , Beng isu OLGUN BEKMAN Chapter 28.....................414 Detect�on a nd Recogn� t �on of Allerg�c Fru�t w� th Deep Learn�ng Model s Sev� nç AY Chapter 29.....................424 A Compa r at�ve Study on S i gnal Pro cess�ng for Ha r mon�cs S ı tk ı AKKAYA Chapter 30.....................439 Numer�cal Analys�s of the Effects of D�fferent F�n Geometr�es on the Performance of Thermoelectr�c Modules �n Channel Conf�gurat�ons Al � T A Ş KI RAN , İhs a n D A ĞT EK İ N , Cel al KIST AK , Nev � n ÇE Lİ K Chapter 31.....................459 Energy Sav�ng Potent�als �n Compressed A�r Systems Er gün KORKMAZ Chapter 32.....................491 Invest�gat�on of the Effect of Hole D�ameter and Aspect Rat�o on Elast�c Buckl�ng Strength and Determ�nat�on Buckl�ng Coeff�c�ents for Th�n Plate Structural Parts �n Aerospace Industry w�th F�n�te Elements Method Mert SUBRAN, Fat�h KARPAT1 Chapter 33.....................507 Energy Consumpt�on of Headl�ghts �n Electr�c Veh�cles Wh�le Dr�v�ng Ç�ğdem CENGİZ, Met�n KAYNAKLI Chapter 34.....................527 R-SHINY App As An Interface For Top�c Model�ng: Rtoptech Ahmet ALBAYRAK, Muammer ALBAYRAK Chapter 1 The Effects of Using Su perplasticizer a nd Pozzolans at Different Ratios on the Rh eological Properties of Self -Compacting Ce ment Paste Fethi İŞSEVER 1 M. Hulusi ÖZKUL 2 Sadık VAROLGÜNEŞ 3 I N T R O D UCT IO N Se lf - c om p a c ti ng c o n c r et e (S C C) h a s a u ni q u e pr o p e r ty t ha t e n a bl e s it t o s p r e ad t o s m a l l - f or m e d an d t ig h t ly r ei n fo r c ed e le me n t s w hi ls t re ta i ni n g i ts ho mo g e ne i t y, w i t h o ut t h e r e qu i r e m en t o f c o m pre ss io n. T h i s m a k e s SC C w e l l-s ui t e d f o r h i g h - pe rf or m a nc e c onc re te st ru ct u r e s, w h i c h t yp i c a l ly u s e c o n v e nt i o na l v i b ro- c om p a c te d c o n c r e te . T h e co n c e pt of SC C wa s i n t r od u c ed fo r u n d e r wa t e r c o n c r et e a p p l ic a t io n s i n t h e ea r l y 19 8 0s (O ka m ura , 19 97 ) . Se lf -c o m pa c ti n g c o n c r e te ( SC C) f i nd s a p p l i c a ti o n i n p r e c a st c o nc r e te , o n-s it e p o ur e d c on c re t e , o r f i br e - re i n f or c ed c on c r e t e ( S ka re nd a hl & P e t e r s so n , 20 00 ) . M o r e o ve r , S C C t a ke s t h e f o r m o f c em e n t p a s te s or m o r t a r s i n a va ri e ty o f st ru ct u r a l a n d s o i l i m p r ov e m en t a p p l i ca t io n s , s u c h a s s o i l gr ou ti n g or f i l l in g co n c re t e c r a c k s ( La c e rd a, da Si lv a , Al va , & de Li ma , 20 1 8 ; T u l li n i & M in gh i n i , 20 16 ; Va su mi t h r an , An an d, & Sa th ya n , 2 0 2 1 ) . As SC C ha s a le ss po ro us st ru c tu r e wi th a mo re u n i f or m i n t e r fa ci a l t r a ns i t i on z o n e ( I T Z ) t ha n t r a d i t io n a l c o n c r e te , i t ha s f e we r po r e s . Mo re ov e r , c e m e nt pa s te pr ov id e s se ve ra l be ne fi t s pe rt ai ni n g t o la bo u r a n d wo r ke r s a f e t y , wo rk a b i l it y, se gr e ga t i o n, ea se a n d du ra t i on o f pr od u c ti o n, en e rg y ef fi c ie n c y, s o u n d i n s u l at i o n a n d d u r a bi l i ty ( R a m an a t h a n, B a s ka r , M u t hu p r i ya , & V e n k a t as u b r a ma ni , 2 0 1 3 ) . I t i s a l s o e m pl o y e d in th e re s t o r a t i on of hi st o r i c al c o n s t r uc t i on s , p r e c as t e n g i n e er i n g, a nd f i ll i ng t il e jo i nts ( Va su m i t hr a n et a l ., 2 02 1 ) . 1 Asst. Prof.; Bingöl University Facult y of Engineering a nd Architecture, Department of Civil Engineering. [email protected] .tr ORCID No: 0000 -0002-8394 -7026 2 2Prof. Dr.; Beykent University Faculty of Engineering and Architecture, Department of Civ il Engineering. [email protected] .tr ORCID No: 0000 -0002-6453-8 956. 3 3Asst. Prof.; Bingöl University Faculty of Engineering and Architecture, Department of Civ il Engineering. [email protected] .tr ORCID No: 0000 -0001-9580 -9889 7 C h e m i c a l a d mi x t u r e s u t i li z ed i n t h e p r od u c t io n o f s e lf- c om p a c t in g c o n c re t e c o m p r i se a bl en d of va ri ou s ad m i xt u r e s , ma in l y su p e rp l a s ti c iz e rs an d vi s c os i t y- r e g u l a t in g a d m i x t ur e s . S u p er p l a s ti c i z er a d m i x t ur e s ar e e m p l o ye d t o de li ve r hi g h f l u i d i ty an d lo we r th e wa te r /b i nd e r ra ti o. Vi sc o s i ty re gu l a ti n g ad m ix t ur e s ar e us ed to pr ev en t s e gr e ga t i on s uc h a s s w ea t i ng a n d p r e c ip it a t io n , to e n s ur e un i fo r m i ty o f t he c o n c r e te , a n d t o r e duc e t h e s h e a r y i e ld s t r e ss ( B ü r g e , 1 9 9 9 ). Mo s t c on c re t e s t r u c tu r e s c u r r e nt l y i n us e ha ve s ta nd a rd st r e ng t h. Ho we v e r , du e t o th e p r a c t ic a l co ns t r a in t s , t he re is li mi te d sc op e fo r t h e a p p l i c a ti on of c o n v e n t io n al co nc r e te . He nc e , t h e r e is a ne ed t o i nn o v at e l ow- bo nd i n g , n o r m a l- s tr e ng t h a nd h i gh - f l o w a bi li t y co n c re t e , w hi c h c a n be i m p l e me n t e d n o t o n l y in re gu la r co ns t ru c ti o n s b u t al s o in s pe c i a li z e d bu il di n gs . Th is de ve lo p m e nt ha s th e p o t e nt i a l t o s ig n i fi c an t l y re du c e c o n s t r uc t io n t i m e l i ne a n d la bo r c o s t s . T h i s h a s a l s o pa ve d t h e w a y fo r t h e d i s c ove ry a n d a p p l i c a ti o n o f P o l y c ar bo x y l a te - b a s e d s u pe r pl a s t ic i z e rs ( K on g & L e e , 2 0 2 1 ). U p o n e x a m i na ti o n o f t h e wo r k i ng p r i n ci p l e s o f s u p e rp l a s ti c i z er s , i t b e c o m e s e v i d e n t th a t th e la t e s t ge n e ra t io n of su p e rp l a s ti c i z er s, co nt a i ni n g l e ng t h y po l y m e r c h a i n s , am a ss o n t he s ur f a c e of f in e p a r t ic l e s. Co ns e qu e nt l y , th e e l e ct r i ca l i m p ul s e a n d s te ri c ef fe c t a re ut il i ze d , e n s u r i ng th e di s t ri bu t i o n o f ce m en t gr ai ns ( U c hi k a wa , H a n e h a r a , & Sa wa k i , 19 97 ; Yo sh i ok a , S a k a i , Da im o n, & Ki ta h a ra , 1 9 9 7). Wh il e t r a d i t io n a l su pe r p l a st i ci z e rs ar e de ri v e d fr om su lf on e na ph t h a le n e f o r ma ld e h y de or s u l f o na t e d m e la m i n e fo rm a l de h y de , ne w e r s up e rp l a st i c iz er s c on s is t of c op o l ym e r s i n w h i c h a c a rb o x yl i c g r o u p is p r e s en t in t h e ma i n c ha in an d a p o l y e th y l e ne gl yc o l gr o u p i s c on ne c t e d t o t he s id e c ha in ( H o u s t e t a l. , 1 9 99) . V is c os it y - r e gu l a t in g a d m i x t ur e s or f in e a gg r e ga t e , o r bo th , ma y of f e r in c re a se d re s i s ta n c e to se gr e g a ti o n, s e t t l in g , a nd co m p r e s s ib il i t y. T h e f in e ma t e ri a l c o n t en t ( l e s s th a n 90μ m) , wh i c h i nc lu de s ce me nt , is de l i be r at e l y in cr e a se d be yo nd a c e rt a i n th re sh o ld to im pr ov e r e s i s t a nc e to we at h e ri n g ( Ö z ku l , Do g a n, Ça vd a r , Sa gl a m, & Pa rl a k, 20 0 0 ; Öz ku l , D o ğa n, Ça v d ar , S a ğ la m , & Pa rl a k, 19 9 9 ) . M i n e r al a d m i xt u r e s , f i n e ly g r ou n d m a t e r i al s bl e n de d w i th c e m en t mo rt ar a n d co nc r e te , a r e us ed to ac hi ev e sp ec if i c e n g i n e e ri ng pr o pe r t i es ( A S T M _ C 12 5 - 1 3a , 20 13 ) . Th e se ma t e r ia l s ma y be ad d e d du ri ng m i xi n g o r t h e c li n k e r p ro d u c ti o n s t a ge . S u bs e q u e nt l y f in e gr i n di n g m a y b e e m p l o y e d f o r bo th na tu ra l a n d pr oc es s e d ma nu f ac t ur e d m a t e ri a l s us e d as mi n e ra l a d m i x t ur e s . Nu m e ro u s s t ud i e s h a ve r e s e ar c h e d m a te r i a l s th a t a c t as m i ne r a l a d m i x t ur e s , r e d u c i n g t h e c e m e n t q u a n ti t y us e d (A rd al an , Jo s ha gha n i , & Ho ot o n , 20 17 ; C h o u d h a ry , Gu pt a , A l o m a yr i , Ja in , & N a g a r, 20 2 1 ; C h o u d ha r y , G u p t a , & N a g a r , 2 0 2 0 ; Da ds e t a n & B a i , 2 0 1 7 ; Gü ne y i s i, G e s oğ l u, Al - R a w i , & M e r m e r da ş , 20 14 ; M e n de s & Du t ra , 20 04 ; Pr in c en & K i s s , 19 89 ; Ra ma n a t ha n et al ., 20 13 ; Sa dr m om t a zi , G a sh t i , & T a h m o u r e si , 2 02 0 ; S ha r b a td a r , Ab b a s i, & Fa kh ar i a n, 2 0 2 0 ) . C e m e n t p a s t e fe a tu r e s no n- N e w t o ni a n f l u i d wi th Bi ng h a m at tr i b ut e s ; it s fr e sh 8 RESULTS AND DISCUS SIONS Plastic viscos ities and yield shear stresses of CPs were measured considering that they have Bingham body properties. In the measurements made with the Viscometer (Rheomat) test device, the averages of the forward and reverse readings were measured between (6 -120) minutes and at (10-15 0) RPM speeds. Figure 3: Rheomat measu rement graph fo r the 90th mi nute of the CP8 sample For this, thresho ld shear stress  0 and viscosity  pl data, known as Bingham constants, were con sidered in all test result evaluations. Cement paste tests were evaluated in four sections. These are: I. Superplasticizer effect for varyin g proportions of Viscocrete II. Water effect III. Effect of Mineral Admixture and binders IV. Correlations between above relation s. In the evalu ations, the first readings, which are the sixth minute readings, were neglected as they contradicted Bingham behavior and distorted the linear part. Viscosity was found from the slope of the linear part, and SYS values were found from the point where the cur ve cuts the shear axis. 4,19 16,2 26,05 34,75 40,3 45,4 53,6 62,5 6,39 11,2 17,65 25,95 35,55 47,1 62,5 y = 2,5142x - 8,9365 R² = 0,9859 0 20 40 60 80 100 120 140 160 0 20 40 60 80 Rotational Speeds (RPM) Shear Yield Stress (Pa) CP8(90) 15 Effects of Fresh Concrete Properties • Effects on Shear Yield Stress (SYS) - Superplasticizer Effect In CPs without admixtures and FA add ed CPs, SYS decreases whe n the ratio of ot her materials is kept constant (W/B= 0.26, C/B=100%) and SP is in creased (Figure 4a, b). If the amount of both W and FA is to o high, the SY S values take small values (Figure 4c). This indicates that there is near to segregation. It has been foun d that the appropriate rate for FA in this combination is about 20 %. Optimum SYS values in terms of workability and consistency are obtained with 20% FA, 1.2% SP and 26% water. When the amount of SP increased in SF -doped CP, the SYS value decreased, albeit slightly. However, it was ob served that the viscosity tester could not measure when the SF ratio was high, and the SP and water ratio s were lo w. This shows that due to the very fine structure of the SF, it needs a lar ge amount of water to get wet (Figure 4d). Figure 4: SYS change s in CP caused b y SP effect - Water Effect In CP without mineral admixtures, when the value of SP was kept constant and the W/B ratio increased, the SYS value decreased. Thi s rate of decrease was approximately 10 times. However, when the SP ratio increases from 1% to 1.5%, there is no point in incr easing the water. Fig ure 5 (a, b) While the SP ratio was lo w in FA added mixtures, there w as an insignificant decrease in SYS when the amount of water was increased. In other word s, the 1. CP1-CP2-CP3 ( SP effect) (b) CP4-CP6-CP8 (FA%2 0, W/B%26) 1. CP17- CP 19 (FA%35, W/B%30) (d) CP 21 - CP 23 (SF%35, W/B%30) 5,17 16,40 24,05 41,85 0 4,56 6,3 12 ,36 19,34 5,68 3,67 1 ,80 2,42 2 ,36 -10 0 10 20 30 40 50 6 30 60 90 120 SYS (Pa) time (m in) 1% 1,2% 1,5% 10,77 7,76 9,22 11,09 11 ,74 0,50 1,71 2 ,28 2,33 2 ,80 2,96 3,67 3 ,96 3,55 4 ,15 0 5 10 15 6 30 60 90 120 SYS (Pa) time (m in) 1% 1,20% 1,50% 1,06 1,34 1,39 1 ,54 1,71 0,0 0,5 1,0 1,5 2,0 1,06 1,34 1,3 9 1,54 1,71 SYS (Pa) time (m in) 1% 1,50% 53,13 67,16 68, 20 75,31 7 6,22 16,40 20 ,06 22,1 1 23,72 23 ,17 0 20 40 60 80 6 30 60 90 120 SYS (Pa) time (m in) 1% 1,50% 16 desired yield could not be obtained by increasing the water. In addition, if both the FA ratio and the SP ratio are high, as in the CP16 experiment, segregation occurred in the CP and water vomiting was observed. Figure 5 (c) It was observed that in th e experiments with high SF ratio, lo w water and SP admixtures, a consistency that was too dense to be measured in SF-added CP and viscosity and spread measu rements cou ld not be made. When SF is in very fine- grained structure, it was be neficial to have both water and SP ratios as high as possible. Fo r Figure 5 (d) SF, appropriate ratios of 5% SF/B, 30 -32% W/B, 1. 5- 2% SP would be appropr iate. Figure 5 : SYS changes in CP caused by water effect - Pozzolan Effect In pure CP experiments, it was observed that SYS decreased in general when the FA/B rati o was incr eased from 20 % to 35%. It was observed that SYS values decreased by an average of 5 times when the FA ratio was kept con stant at W/B=26%, and SP=1.5% in FA added mixtu res and the FA ratio was increase d from 20% to 35%. Figure 6 (a) and (b) It was observed that in th e experiments with high SF ratio, lo w water and SP admixtures, a consistency that was too dense to be measured in SF-added CP and viscosity and spread measu rements cou ld not be made. When SF is in very fin e - grained structure, it was beneficial to have both water and SP ratios as high as (a) CP1-CP14 (SP %1) (b) CP1-CP14 (SP %1.5) (c) CP14- CP16 (FA %20 ,SP%1) (d) CP12 -CP22 (SF%5, SP%1.5) 5,17 16,40 24,05 41,85 0,87 1,9 0 1,91 2,1 8 3,47 0 10 20 30 40 50 6 30 60 90 120 SYS (Pa) time (m in) 0,26 0,3 5,68 3,67 1,80 2,4 2 2,36 2,48 4,31 4,3 0 4,09 4,1 4 0 2 4 6 8 6 30 60 90 120 SYS (Pa) tim e (min) 0,26 0,3 10,77 7,76 9 ,22 11,09 11 ,74 1,91 1, 89 2,36 3 ,71 4,23 -1 3 7 11 15 6 30 60 90 120 SYS (Pa) time (m in) 0,26 0,3 13,82 19,51 19 ,84 22,1 0 22,30 11,63 14,85 14 ,18 14,2 5 15,11 0 5 10 15 20 25 6 30 60 90 120 SYS (Pa) time (min) 0,26 0,3 17 possible. Fo r Figure 5 (d) SF, appropriate ratios of 5% SF/B, 30 -32% W/B, 1. 5- 2% SP would be appropr iate Figure 6(c). Figure 6 : Change of SYS wit h the effect of mineral a dmixtures in C P • Effects on Viscosity Viscosity is the most impo rtant rh eological property in determ ining the homogeneity of CP and thus of concrete. Th erefore, it is desirable th at the viscosity be above a certain ratio. In the experiments carried out, it has been seen that SP gives a better beh avior to CP than water for viscosity. Because water, besides being effective in reducing SYS, also reduces the viscosity below the desired valu es, causing segregatio n and deterio ration of ho mogeneity. Although separations were observed when the SP was a pplied more th an the required dose, an excellent machinability was obtained when the SP/B ratio was well adju sted. In other words, the more advantageous aspect of SP than water is that it prevents segregation whil e increasing the work ability. In add ition, the processing time of CP has increased. 1. CP4- CP 5 (W/ B %2 6,SP%1 ) (b) CP14- CP16 (FA %20,SP%1) (c) CP12-CP13 (W/B%26, SP%1.5 ) 10,77 7,76 9,22 11,09 11 ,74 0,52 0,8 8 1,40 1,4 1 2,28 -2 2 6 10 14 6 30 60 90 120 SYS (Pa) tim e (min) 0,2 0,35 2,96 3,67 3,9 6 3,55 4,15 1,06 1,1 9 1,17 1,22 1 ,37 0 2 4 6 6 30 60 90 120 SYS (Pa) time (m in) 0,2 0,35 13,8 2 19,51 19 ,84 22, 10 22,3 0 36,3 3 47,24 48 ,48 51,5 0 0 10 20 30 40 50 60 6 30 60 90 120 SYS (Pa) time (m in) 5% 10% 18 - Superplasticizer Effect I n the CP experiments witho ut mineral admixtures (control samples), it was observed that the viscosity increased as th e SP ratio increased. Figure 7 (a). It was observed that increasing the SP ratio (1-1.2 -1.5%) in CP with FA did not improve the viscosity, on the contrary, when the SP ratio increased with the water ratio, undesired separation became inevitable. Naturally, when FA and other admixtures are used at optimum values, v ery good consistency and workability are provided in CP. Fig ure 7(b, c) In admixtur es with SF, when the SP ratio increased from 1% to 1.5%, the viscosity did not change much. For these experiment s, th e reason for this is that SF is already a ma terial that requires a l ot of water and SP on its own. Figure 7 (d). Figure 7: Effects of SP o n viscosity i n CP - Water Effect In CP without mineral admixtures, viscosity decreases enormou sly when water increases (26- 30%). It can be said that among all binders, the material that interacts best with water is cement. However, in general, th e viscosity increases rapidly over time, as water decrea ses the viscosity. Figure 8 (a, b, c). (a) CP1-CP2- CP3 (W/B %26) (b) CP1-CP2-CP3 (FA %20, W/B %26) (c) CP17- CP19 (FA%35, W/B %30) (d) CP21-CP23 (SF%10, W/B %30) 0,51 0,5 3 0,56 0,6 1 0,42 0,50 0,5 4 0,57 0,6 3 0,58 0,6 3 0,74 0,7 4 0,79 0,20 0,40 0,60 0,80 1,00 6 30 60 90 120 Vis. (Pa.s) time (m in) 1% 1,20% 1,50% 0,30 0,35 0,3 6 0,36 0,39 0,33 0,34 0,38 0,40 0,41 0,25 0,30 0,35 0,40 0,45 6 30 60 90 120 Vis. (Pa.s) time (m in) 1% 1,20% 1,50% 0,14 6 0,149 0,148 0,154 0,154 0,13 5 0,139 0,144 0,144 0,145 0,12 0,14 0,16 0,18 6 30 60 90 120 Vis. (Pa.s) time (m in) 1% 1,50% 0,08 0,1 0 0,09 0 ,09 0,09 0,17 0,1 6 0,16 0 ,16 0,1 7 0,05 0,10 0,15 0,20 0,25 6 30 60 90 120 Vis. (Pa.s) time (m in) 1% 1,50% 19 Water, which already has th e ability to reduce viscosity in CP mixtures with FA, also decreases when it is processed with a coarser gr ained material than cement. In SF, although the viscosity decreased when th e amount of water was increased, this did not decrease over time and preserved its value. Figur e 8(d). Figure 8 : Effect of water ef fect on viscosit y in CP - Pozzolan Effect In FA added CP, the viscosity increases with the amount of FA (20 -35%) at low water (26%) and SP ratios, that is, it sho ws the desired behavior. On the other hand, when FA increases, viscosity decreases in mixtures with high water and SP content. Figure 9 (a, b) It is observed that the viscosity decreas es very littl e when the SF increases. All evaluations were obta ined because of the comparison of the specified experiments with other experiments. Viscosity increases from 6 to 120 minutes because of the recovery of so me of the mixtures over time, and the condensation of some of the mixtures over time, since they already have a normal consistency, in almost all exp eriments, in other word s, they go towards the viscou s state. Th e amount of this increase varies from mixture to mixture. It has been observed that time alone is not as effective as S YS for v iscosity. (a) CP1-CP14 (SP %1) (b) CP3-CP15 (SP %1.5 ) (c) CP14- CP16 (FA%20, SP %1) (d) CP12-CP22 (SF%5, SP %1.5 ) 0,51 0,53 0 ,56 0,61 0,19 0,21 0 ,23 0,26 0, 31 0,00 0,20 0,40 0,60 0,80 6 30 60 90 120 Vis. (Pa.s) time (m in) 0,26 0,3 0,58 0,63 0,74 0,74 0 ,79 0,24 0,25 0 ,26 0,27 0 ,27 0,00 0,30 0,60 0,90 6 30 60 90 120 Vis. (Pa.s) time (m in) 0,26 0,3 0,19 0,21 0 ,23 0,26 0,31 0,15 0,17 0 ,18 0,19 0,1 9 0,00 0,10 0,20 0,30 0,40 6 30 60 90 120 Vis. (Pa.s) time (m in) 0,26 0,3 0,25 0,2 4 0,24 0 ,23 0,17 0,1 6 0,16 0 ,16 0,17 0,00 0,10 0,20 0,30 0,40 6 30 60 90 120 Vis. (Pa.s) time (m in) 0,26 0,3 20 Figure 9: Effect of SF on viscosity i n CP • Evaluation of Spread Test Results Slump-scattering experiments were performed for CP mixtures using slump cones. For each mixture, the spreading diameter, and the time to reach 100 mm were measured in seconds. - Superplasticizer Effect In the examinations made with mini slump spreading experiments, it was understood that the use of SP increased the spread and maintained this spread regularly for 12 0 minutes. Wh ile no measurement could be made after the 30th minute in contro l samples, this problem was overcome with the use of S P, in addition, it was observed that viscosity and homog eneity were preserved. It has been determined that the use of SP together with FA ensures that the spread is smooth and uniform in all directions. When the time to reac h a diameter of 100 mm in CP was examined, it was observed that the us e of SP shortened the time to reach. Thus, it is understo od that fres h material will settle into t he mold more quickly in concrete pouring at con struction sites Figure 10(b). Figure 10 : SP effect on CP4-CP8 s pread diamete r and time to reach 1 00 mm diameter (a) CP4- CP 5 (W/B %2 6, SP % 1) (b) CP8-CP9 (W/B%26, SP %1,5) 0,27 0,3 5 0,37 0 ,40 0,38 0,42 0,5 0 0,54 0 ,57 0,63 0,00 0,20 0,40 0,60 0,80 6 30 60 90 120 Vis. (Pa.s) tim e (min) 0,2 0,35 0,33 0,3 4 0,38 0,4 0 0,41 0,25 0,2 5 0,26 0,2 6 0,28 0,00 0,20 0,40 0,60 6 30 60 90 120 Vis. (Pa.s) tim e (min) 0,2 0,35 (a) (b) 159 156 153 155 152 179 179 168 168 164 120 140 160 180 200 6 30 60 90 120 Spread ( m m ) tim e (min) SP effect on spread diameter CP4 CP8 1,89 2 ,2 2,35 2 ,38 2,6 3 1,44 1 ,54 1,7 1 ,87 1,9 0 0,5 1 1,5 2 2,5 3 6 30 60 90 120 Spread t ime (sn) tim e (min) SP effect on sam ples reaching 100mm CP4 CP8 21 - Water Effect When the effect of water on the spreading in CP was examin ed, it was observed that the spreading increased with the increase in water . Th e diameter difference between the samples was maintained at almost th e same rate fro m the 6th minute to the 120th minut e. Figure 11 (a). When the time to reach 100 mm was examined, it was understood that the amount of water accelerated the spread, and this speed was maintained for 120 minutes. Figure 11 (b). Figure 11 : W/B effect on CP 8-CP18 spread an d time to reach 100mm - Pozzolan Effect While examining the pozzolan effect in the diffu sion experiments for CP, the effect of FA was examined first. While the use of FA was more effective in the first minutes of the mixture, the effec t of th e use of FA on the spread decreased as time progressed. The effect of using 35% FA instead of 20% FA decreased rapidly after 30 minutes. Figure 12 (a). For the time to reach 100 mm, the use of water reduced the time by approximately 40%, which was tru e for all 5 measurements over 120 minutes. Figure 12 (b). Figure 12 : FA effect on CP16-CP 17 spread and time t o reach 100 mm diameter Increasing the amount of Silica Fu me greatly reduced th e spread. Increasing the SF/B ratio from 5% to 10% prevented measurements after a certain time in (a) (b) 179 179 168 168 164 189 186 186 186 186 140 160 180 200 220 6 30 60 90 120 Spread ( mm ) tim e (min) Water effect on t he spreading of sam ples CP8 CP18 1,44 1,5 4 1,7 1,87 1 ,9 0,94 1,0 2 1,25 1, 31 1,41 0,5 0,8 1,1 1,4 1,7 2 2,3 6 30 60 90 120 Spread t ime (sn) tim e (min) Water effect on sam pl es reaching 100 m m CP8 CP18 (a) (b) 170 168 168 168 168 188 184 175 172 171 140 160 180 200 6 30 60 90 120 Spread ( m m ) tim e (min) FA effect on spreading diam eter of sam ples CP16 CP1 7 0,93 1,31 1,3 2 1,41 1,4 1 0,72 0,8 9 1 1,05 1,0 5 0 0,4 0,8 1,2 1,6 6 30 60 90 120 Spread tim e (sn) tim e (min) FA effect on samp les reaching 100 m m diameter CP16 CP1 7 22 many mixtures. Despite th e use of the h ighest amou nt of water and SP, both t he final spread and the results of reaching a diameter of 100 mm could not be measured after the 90th minute, even in the CP22 -CP23 samples. Figure 13 (a). Figure 13 (b) While th ere was a directly proportional difference in the spreadin g diameter measurements depending on the time, there was a rapid slowdown in reaching 100 mm between the 6th and 30th minu tes. Figure 13 : SF effect on CP spread and time to reach 100 mm diamete r Analysis of Correlations between F resh Cement Paste Properties • Correlation between Visco sity-Shear Yi eld Stresses In general, a directly proportional relationship is determined between viscosity and SYS. SYS in creased over time in con trol samples made with cement only. Especially after the 60th minute, the increase accelerated. The viscosity increase rate was not as m uch as SYS. However, the machinability loss was not much (Figure 14 -a, b ). In FA -added CP mixtures, when the ratio s of W/B=26% and SP/B=1% were constant while th e FA ratio in creased from 20% to 35%, both SYS and viscosity values decreased. The decrease of the v iscosity and the SYS reve aled that the homogeneity of the material did not deteriorate, and the workability was preserved (Figure 14 -c, d ). In FA-added samples, when both W/B and FA ratios are maximum, and SP kept constant whil e FA increased, th e decrease of viscosity is less, and th e decrease of SYS is slightly higher. A situation with good workability has occurred (Figure 14 -e, f ). In SF-added mixtures, when W/B 30% and SP kept constant at 1.5% while SF increased fro m 5% to 10%, SYS increased while vi scosity decreased. This show s that the workability was redu ced (Figure 14 -g, h ). (a) ( b) 136 134 133 129 128 105 103 103 100 80 100 120 140 160 6 30 60 90 120 Spread ( m m ) tim e (min) CP22- CP23 num uneleri yayı lma ça pına SF etk isi CP22 CP23 1,61 1,7 1 1,95 2,3 1 2,96 4,2 7,97 7,9 9,13 0 2 4 6 8 10 6 30 60 90 120 Yayılma süresi (sn) tim e (min) SF effect on CP22-CP23 reaching 100 m m CP22 CP23 23 Figure 14 : Correlation between Vis-SYS (a) (b) (c) (d) (e) (f) (g ) (h) 5,17 16,40 24,05 41,85 0,51 0,5 3 0,56 0,6 1 0,0 0,2 0,4 0,6 0 10 20 30 40 50 60 6 min 30 mi n 60 min 90 min 120 min SYS (MPa) CP1 SYS-VIS VIS (Pa.S) SYS VISCOSITY 0,00 4,56 6,3 0 12,36 19,24 0,42 0,5 0 0,54 0,5 7 0,63 -0,1 0,2 0,5 0,8 0 10 20 30 6 min 30 min 60 min 90 min 120 min SYS (MPa) CP2 SYS-V IS VIS SYS VIS COSITY 7,58 7, 76 9,22 1 1,09 11, 74 0,27 0,35 0,3 7 0,40 0,3 8 -0,15 0,05 0,25 0,45 -5 5 15 25 6 min 30 min 60 min 90 min 120 min SYS (MPa) CP4 SYS-VIS VIS SYS VISCOS ITY 0,52 0,8 8 1,40 1,4 1 2,28 0,24 0,2 8 0,30 0,3 0 0,30 0 0,1 0,2 0,3 0,4 0 1 2 3 6 min 30 min 60 min 90 min 120 min SYS (MPa) CP5 SYS-V IS VIS SYS VISCOSITY 1,91 1,8 9 2,36 3,71 4,2 3 0,15 0,1 7 0,18 0,1 9 0,19 -0,08 0,02 0,12 0,22 0 2 4 6 6 min 30 min 60 min 90 min 120 min SYS (MPa) CP16 SYS- VIS VIS SYS VISCOS ITY 1,06 1,34 1,3 9 1,54 1,7 1 0,15 0,1 5 0,15 0,1 5 0,15 0 0,1 0,2 1 1,4 1,8 2,2 6 min 30 min 60 min 90 mi n 120 min SYS (MPa) CP17 SYS- VIS VIS SYS VISCOS ITY 11,63 14 ,85 14, 18 14,25 1 5,11 0,17 0,1 7 0,20 0,2 0 0,20 0,05 0,1 0,15 0,2 0,25 0 10 20 30 6 min 30 min 60 min 90 min 120 min SYS (MPa) CP22 SY S-VIS VIS SYS VISCOS ITY 16,40 20 ,06 22,1 1 23,72 2 3,77 0,17 0 ,16 0,16 0 ,16 0,16 -0,08 0,02 0,12 0,22 0 10 20 30 40 6 min 30 min 60 min 90 mi n 120 min SYS (MPa) CP23 SY S-VIS VIS SYS VISCOSITY 24 be am - to -c ol um n c o n n e c ti o ns of pr e c as t c on c re t e st r uc t ur e s – A n ex pe r i m en t a l a n a l y s is . E ng i ne e r i ng S t r uc t ur e s , 1 7 2 , 2 0 1- 2 1 3 . Me nd es , P. R . S. , & Du tr a , E. S . (2 0 04 ) . V i s c o s i ty fu nc ti o n f o r y i e l d- st r e ss li qu id s . Ap pl i e d Rh e o lo g y , 1 4 ( 6 ) , 29 6 - 30 2 . Mo nt go m e r y, D. C . ( 20 1 7 ) . D es i g n a n d a n a ly s i s o f e x pe ri m e n t s : J o hn w i l e y & s o n s. N o r n b e r g, J . , Pe t e r s on , Ö ., & Bi ll b e r g, P . ( 1 9 9 7) . Ef fe c t o f n e w ge ne ra t i on s u pe rp la s t ic i z er s on th e pr o p e r ti e s of fr es h c o nc r e t e , Su p e rp l as t i c iz er s an d O t h e r Ch e m i c al A dm i x t ur e s in C o nc r e t e . P ap e r pr e s e nt e d a t th e P r o c e ed i ng s . O k a m u r a , H . ( 1 9 9 7) . S e l f- c o m pa c t i ng h i gh- pe r fo r ma nc e c o n c re te . Co nc r et e i nt er na t io n al , 19 ( 7 ) , 5 0 - 54 . Ö z k u l , M ., D oga n, A ., Ç av da r , Z ., S a gl a m, A . , & P a rl ak , N . ( 2 00 0 ) . Ef fe c t s of s e lf c o m p a c t in g co n c r e te a dm i x tu r e s on f r e s h a n d ha r de n e d c o n c r e t e pr o p e r ti e s . Pa pe r p r es e n te d a t t he P r oc ee d i ngs . Ö z k u l , M. , Do ğa n , A. , Ç a vd a r, Z ., Sa ğ l a m, A ., & P ar l ak , N . (1 99 9 ) . P ro pe r t i es of f r e s h a nd ha r de n e d c on c re t e s p r e pa r e d by ne w g e ne r a ti o n s u p e r pl as t i c iz er s . I n M o d e r n C o n c re t e Ma t e r ia l s: Bi n de r s , Ad di t io n s an d Ad m i xt u r e s ( p p. 4 6 7 - 47 4) : T h om a s T e l f or d P u b li s h i ng . Pr in ce n , H. , & Ki s s, A. (1 98 9 ) . Rh eo l og y of fo am s a nd hi g hl y co nc e nt r a t e d e m u l s i ons : IV . A n e xpe ri me nt a l s tu dy of t he sh e a r v is c o si t y a nd yi e l d s tr e s s of c o nc e n tr a t e d em ul s i on s . Jo u r na l o f co ll o i d an d in te r fa c e sc ie n c e , 12 8 (1 ) , 17 6- 18 7 . R a m a n a th a n , P . , B a s ka r , I . , Mu t h u pr i y a, P . , & V e nk a t as u b r a ma ni , R . ( 2 01 3 ) . Pe rf or m a nc e of s e lf - c o m pa c ti n g c o nc r e t e co n ta i ni n g d if f e re n t mi ne r a l a d m i x t ur e s . K S C E j our n al o f C i v il E n g i n e er in g , 1 7 ( 2 ) , 46 5 - 4 72 . Sa dr m om t a zi , A. , Ga s h ti , S. H. , & Ta hm ou r e s i , B. (2 02 0 ) . Re si d u a l st re n gt h an d m i c r o s t ru c tu r e of fi b e r r ei nf o r c ed s el f - c om p a ct i n g co nc re t e ex p os e d to h ig h t e m p e r a tu r e s . Co ns tr uc ti o n a n d B u i l di n g M a t e r ia l s , 2 3 0 , 1 1 6 9 69 . Sh ar ba t da r , M . K. , A b ba s i , M. , & Fa k h a r i a n, P . ( 2 0 2 0) . I m p r ov i n g t h e pr op e rt i e s of s e l f - c om p a c t ed c o n c re t e wi th us i ng c o m b i ne d s i l ic a f um e a n d m e t ak a o l in . Pe ri od i c a P ol y t e ch n i c a C iv i l E n g i ne e r i ng , 6 4 ( 2 ) , 5 3 5 - 54 4. Sk ar e nd a hl , Å. , & Pe t e rs s on , Ö . ( 2 0 00 ) . Re po r t 23 : Se l f - C om p ac t i n g Co n c r et e – St at e - of - th e- A r t R e p or t of Ri le m Te c hn i ca l Co m m it t e e 17 4- SC C (V o l . 23 ) : R I L E M pu b l i ca t io n s . TS - EN - 197 - 1 . ( 20 1 2 ) . Ce m e nt – Pa r t 1: Co mp o s i ti o n , sp e c if i ca t i on an d co nf or m i t y c r i t e r ia f or c om m on ce m en t s. I n C em e nt – P a r t 1: C om p os i t i on , s pe c i fi ca t i o n an d co nf o r m i ty cr it e r ia fo r c om mo n ce m e nts (V ol . TS EN 19 7- 1 ) . An k a ra : Tu rk i sh S t a n da r ds I n s ti t ut e . 31 Tu ll in i , N . , & Mi ng h i ni , F. (2 01 6 ). Gr ou t e d sl e e ve c on ne c ti o ns us ed in pr e ca s t r e i n f o rc e d c o n c re t e c o n s tr u ct i o n – E xp e ri m en t a l i n v e s t ig a t i on o f a c ol u m n - to - c o l u m n j o i nt . E n gi n e e ri n g S tr u c t u r es , 1 2 7 , 7 8 4 - 80 3 . U c h i k a wa , H ., Ha ne h a ra , S. , & Sa wa ki , D. (1 99 7 ) . T he r o l e o f s te r ic r e pu l s i ve f or c e i n th e d i s p e rs io n of c e m en t pa rt ic l e s i n f r e s h p a s t e p r ep a r e d w i t h o r g a ni c a d m i x t ur e . C e m en t a nd C o n cr e t e R e s e ar c h, 2 7 ( 1) , 37 - 50 . V a s u m i t hr a n, M. , A na n d, K ., & Sa th ya n , D. (2 02 1 ) . E f f ec t s o f fi ll e r s o n t h e rh eo l og y of c e me nt g r o ut s . M at er i al s To d a y : P r o c ee di n g s , 4 6 , 5 15 3 - 51 5 9 . Y o s h i o ka , K. , Sa k a i, E. , Da im o n , M. , & K i t a h a ra , A. ( 1 9 97 ) . Ro le of s t e r i c hi n dr a nc e i n t h e p e rf o rm a n c e of s u pe r p l a st i c iz e r s fo r c o n c r e te . J o u r n al o f t h e A me r i c an C e r a m i c So c i et y , 8 0 ( 1 0 ) , 2 6 6 7 -2 6 7 1 . 32 Chapter 2 Formation Mechanisms and Deposition Processes of Pyroclastic Rocks Abdullah SAR 1 Mehmet Ali ERTÜRK 2 ABSTRACT The pyro clast is defined as crumbs throw n ou t of volcanic vents, regardless of the orig in of the grains and their eruption patterns. Pyroclastic rocks are formed by the transport, accumulation and consolidation of pyroclastic material produced by a volcanic eruption by air or water. Pyroclastic eruptions are examined in four sections: Hawaiian-ty pe, Stromboli -type, Vulcano -type and Plin ian-type eruptions, according to magma density, viscosity, temperature, gas content and chimney height. While Hawaiian eruptions with the lowest erup tion intensity are represented by basaltic lavas, Plinian erup tions with the highest eruptio n intensity are represented by dacitic lavas with high viscosity. Pyroclastic eruptions are deposited as debris, flows and turbulence deposits. The siz es and shapes of the debris tanks formed after the explosive rise of gas and tephra from the chimney reflect the eruption column heig ht, speed and direction of atmospheric wind s. As a result of the spreadin g of the risin g colu mn, the crumbs fall to th e gro und due to gravity and thus form "debris depots". The fo rmation of flow depots, which are formed due to the pyroclastic mass with high grain density flowing along the surface, is contro lled by gravity, and the pyroclastic material is hot and sometimes flui d. Pyroclastic material: Th e reservoirs are transported by a widespread, turbulent, low -grain density gas-grain cloud across the surface with turbulent motion. Keywords: Pyroclast, Py roclastic rocks, Pyroclastic eruptions, Pyroclastıc Eruptıon Deposites 1 Arş. Gör Dr..; Fırat University Engi neering Faculty Department of Geolo gical Engineering. [email protected] .tr ORCID No: 0000- 0002 -9752-7807 2 Dr. Öğr. Üyesi; Fırat University Engineering Faculty De partment of Geological Engineering . [email protected] ORCID No: 0 000 -0003-1197-9202 33 INTRODUCTION Pyroclastic rock is formed by the transport, accumulation and consolidation of pyroclastic material produced by a volcanic eruption by air or water (Sun et al., 1987, 2001; Chang et al., 2009; Huang et al., 2010; Wang et al., 2019 ; Zh ou et al., 2022 ). Regarding classification, pyroclastic rocks are lo cated in th e transition zone between volcanic and sedimentary rocks (Sun et al., 1987, 2001; Chang et al., 2009 ; Zhou et al., 2022 ). Although it has the characteristics of volcanic and sedimentary r ocks, it has a complex litholo gy. (Sun et al., 1987 , 2001; Chang et al., 2009; Huang et al., 2010; Wang et al., 20 19; Yuan et al., 2021). The mineral compo sition and cementation mode are different from th e other two species (Sun et al., 2001; Huang et al., 2010; Wang et al., 2019; Yuan et al., 2021). Pyroclastic rocks are mainly composed of pyroclastic material with some sedim ents or lava materials (Chang et al., 2009; Huan g et al., 2010; Wang et al., 2019 ; Zhou et al., 2022 ). Physically, these ro cks can be described as hard, semi-plastic or plastic (Sun et al., 1987, 2001; Chang et al., 2009; Huang et al., 2010; Wang et al., 20 19 ; Zhou et al., 2022). Typically, py roclastic rocks consist of a combination of rock debris, crystal debris, a nd volcanic glass debris (Huang et al., 2010; Wang et al., 20 19). ). Py roclastic rocks can also form from amorphous cooled molten mud, as pyroclastic material is subj ected to rapid changes in pre ssure and te mperature as lava advances towards th e surface (Sun et al., 1987, 2001; Ch ang et al., 2009; Wang et al., 2019 ; Zhou et al., 2022). Pyroclast is defined as fragments of grains thro wn out from volcanic vents, regardless of their origin and eruption form (Schmid, 1981 ). Pyroclastic clasts are clasts formed directly by volcanic means. Volcanic materials that have been involved in sedimentation processes are defined as volcanoclastic. Hydroclastic clasts are a type of pyro clasts formed fr om steam eruptio ns where magma -water interaction occurs, rapid cooling, and mechanical gr aining of lavas in contact with water or water-saturat ed sediments (URL-1) . ERUPTION TYPES Pyroclastic eruptions are divided into Hawaiian (Fig ure 1a), Stromboli (Figure 1b) , Vulcano (Figure 1c), and Plinian (Figure 1d)erup tions. Hawaiian-Type Eruptio ns Hawaiian erup tions are one of the types of volcanic eruptions named after Hawaiian volcanoes. These are among the calmest eruptions, characterized by intense eruptions of fluid basaltic lavas due to their low gas content. The volume of materials ejected in Hawaiian eruptions is less than half that in other eruptions. The continuous production of small amounts of lava creates the lar ge shape of a 34 shield volcano. Eruptions are not centred on the main summit as in other volcanic types but generally occur in cracks radiating fro m outside th e centre and in chimneys around the summit (URL-2 ). Figure 1: Pyroclastic eruptio n types a. Hawaii-type eru ption, b. Stromboli-type eruption, c. Vulcano-type eruptio n, d. Plinien-type eruption (URL-2). Hawaiian er uptions begin as an eruption line along cracks called "fire curtains." These are cut off over time as lava accumulates in the crevices. Centr al vent eruptions, meanwhil e, take the form of large lava foun tains that can reach hundreds of meters hi gh. Particles in lava fountains often cool in the air before falling to the ground, accumulating volcanic cinders. However, w hen the air is concentrated, especially with volcanic fragments, it does not cool quickly enough due to the surrounding temperature . The pieces f all ho t to the ground and form cinder cones (URL-2).. If eruption rates are high enough, they can prod uce splatter -fed lava flows. Hawaiian eruptions are often extremely long - lasting; Pu'u O'o, a cinder cone of Kilauea, has erupted continuously since 1983. Another feature of Hawaiian 35 volcanoes is active lava lakes. Currently, there are only 5 of th ese lakes in the world. Kilauea's Kupaianaha crater is o ne of them. The flows in the Hawaiian eruptio ns are basaltic, and their structural character is di vided int o two types. Pahoehoe lavas are fairly smooth lava flows that can be wavy or rope-shaped. A'a lava flows are den ser and more viscous than Pahoehoe lavas and tend to be transported more slowly. Flows can be measured between 2- 20 meters th ick. A'a l avas are so thick that their outer shell coo ls from the inside, like a rock mass that protects it from cooling and isolates the heat inside. Pahoehoe lavas can turn into A'a lavas as their viscosity increases , but A'a lavas never turn into Pahoeho e flows (URL-2) .. Hawaiian eruptions are responsible fo r several specific volcano logical formations. Small volcanic particles are formed and carried by t he wind, quickly cooling th e inside of teardrop -shaped glassy fragm ents known as Pele's tears (URL-2).. Especially during strong winds, these pieces can take the form of long striped hairs known as Pele's h air (Figur e 2). Stromboli-Type Eruptio ns Stromboli eruptions are one of the types of volcanic eruptions named after the Stromboli volcano, which has been erup ting contin uously for centuries. Stromboli eruptions are triggered by the explosion of ga s bu bbles within magma. These gas bubbles within the ma gma coalesce and accumulate into large bu bbles called gas slugs. These grow large enough to rise throughout the lava column. Once th ey reach the surface, differences in air pressure cause the bubbles to burst with a loud noise. Due to the high gas pre ssure associated with lavas, sustained activity usually consists of episodic explosive eruptions accompanied by distinctive high eruptions (URL -2). During an eruption, these explosion s occur every few minutes. The term stro mboli is used to describe a variety of volcanic erup tions, ranging from small volcanic eruptions to large eruption columns. True stromboli eruptions are characterized by the exp losive eruption of short -term and moderately viscou s lavas. Eruption columns can rea ch height s of hundreds of meters (URL - 2) . The lavas formed by these erup tions are partl y a form of high - viscosity basaltic lavas, and their fin al product is mostly scoria (Fig ure 3). 36 Figure 2: Samples of pyr oclastic Pele's hair Strombolian erup tions eject volcanic bombs and lapilli fragments (Figure 4 ) that travel in a parabolic orbi t before falling into a region around the crater. Th e continuous accumulation of small fragments forms cind er con es formed entirely by combin ing basaltic pyroclasts. Stro mboli erup tions are similar to Hawaiian eruptions, but there are some differ ences. Stromboli erup tions are louder and do not have a continuous eruption column. Pele's hair does not produce some volcanic products associated with Hawaiian volcanism, such as Pele's tears (Figure 2), and produces less molten lava flows (URL -2). Vulcano-Type Eruptio ns Vulcanian eruptio ns are one of the types of volcanic eruptions named after the Vulcan volcano, which gave the word volcano its name. In Vulcan -type eruptions, sep arating gases from the mag ma is difficul t due to their high viscosity. Similar to Stromboli eruptions, an increase in hi gh gas pr essure is observed in these eruptions. However, un like Stromboli eruptions, the lava pieces ejected in vulcano-type eruptions are not aerodynamic. This is due to the high viscosity of 37 the magma. Th ey are mu ch more exp losive than stromboli -type eruptions, with eruption co lumns reaching 5 to 10 km (URL-2 ). Figure 3: Samples of pyr oclastic scoria Vulcanian deposits are andesitic or dacitic rather than basaltic. Initial volcanic activity involves a series of short -liv ed eruptio ns lasting from a few minu tes to several ho urs, typically ejected volcanic bombs and bl ocks. These erup tions erode the lava domes that preserve the magma underneath and break it apart with numerous and continuous eruptions. Therefore, early signals of future Vulcanian eruptions are lava dome growth. As la va domes collap se, pyroclastic material forms on the volcano's slopes (URL-2). Deposits clos e to the crater contain large volcanic blocks and bombs (Figure 4), particularly commonly called "bread crust bombs". They are formed by rapidly cooling t he ejected lava's outer surface into a glass or fine -grained shell. However, cooling and void formation contin ue inside. The centre of the piece expands, cracking th e o uter surface. However, Vulcanian deposits consist of fine- grained ash. This ash is partially dispersed, and its abundan ce indicates high gas pressure within the magma and a hi gh degree of fragmentation (URL -2). 38 Figure 4: Samples of py roclastic bomb Plinian-Type Eruptio ns In Plinian -type eruptions, the process begins in the magma chamber, where dissolved volatile gases accumulate in the magma. Gases rise along the magma channel, accu mulate and form a void. Th ese bubbles coalesce an d bu rst when they reach a certain size (approximately 75% of the total volume of the magma conduit). Narrow sections of the channel put pressure on the gases that shape the eruption column . The gas content in the magma column controls the eruption rate, and low-strength surface rocks disintegrate under the eruption pr essure, forming a conical outlet stru cture (URL -2).. Large-diameter eruption columns are a distinctive feature of Plinian eruptions. They reach an altitude of between 2 and 45 km in the atmosphere. These hi ghly explosive eruptions are associated with rhyolitic or dacidic lavas, ri ch in volatile content, and are typically seen in stratovolcanoes. Eruptio ns can continue for days, with longer -lasting eruptions more commonly associa ted with fels ic volcanoes (URL -2). Alth ough associated with felsic magma, Plinian eruptions can also occur in basaltic volcanoes. Plinian erup tions are similar to Vulcani an and Strombolian eruptions, except for distinct explosive eruptions. Continuous eruption columns shape plinian eruptions. These erup tions are similar to the Hawaiian erup tion type. Bot h ty pes of erup tions form con tinuous eruption c olumns fu eled by the growth of bubbles that are transported at approximately the same spe ed as the surroun ding magma (URL-2).. Regions affe cted by Plin ian erup tions are exposed to dense pumice (ash) clouds, affecting an area of 0. 5 to 50 km3. Th e most dangerou s eruption feature is pyroclastic flows, which occur when material transp orted down the mountain slope at a speed of appr oximately 700 km per hou r collapses. PYROCLASTIC ERUPTION DEPOS İTES Pyroclastic deposits, fo rmed due to magm a or r ock's disintegration by explosive vo lcanic activity, are divided into three groups according to their 39 origin, transportation and storage methods. Th ese are (i) debris, (ii) flow, and (iii) turbulence (Helvacı and Erkül , 2001). Spill Deposite The size s and shapes of the debris tanks formed after the explosive rise of gas and tephra from th e chimney reflect the erup tion column height, speed and direction of atmospheric winds. As a result of the spreading of the rising column, the crumbs fall to th e ground due to gravity and thus form "debris depots". Larger pieces fly ou t of the chimney due to explosions, and the pieces called " ballistic crumbs or clasts" are unaffected by the wind. Pyroclastic flo ws partially form other fine-grained pyroclastic debris depots. They are fo rmed by separating from the upper part. These depots are called "debris dep ots derived from the ash cloud" (He lvacı and Erkül, 2001). Debris deposits that form overburden layers generally have equal thickness, except for areas with hi gh slop e topography. Although poor sorti ng is generally observed in pyroclastic deposits, debris deposits show good sorting due to their separation in air durin g transportation. In some cases, they show planar lamination or layering du e to the change of th e eruption column. However, they do not present erosion , cross-bed ding or load structures in the unde rlying layers. It originates from debris tanks near the chimney (Helvacı and Erkül, 2001). Flow Deposite These deposi ts are formed due to the pyroclastic mass with hig h gr ain concentration flo wing along the surface. Their formation is controlled by gravity, and the material is ho t and, in some cases, fluid. Th ey generally show topography- controlled settlement s that fill valleys and depression areas (Helvacı and Erkül, 2001). When the internal structure of py roclastics is examined, it is seen th at th ey are generally massive and poor ly sorted . Poor sorting in flo w tanks is due to high grain con centration and is no t related to tur bulence. The do minant flow mechanism is generally laminar. Wh en each flow unit overlaps, it appears as a layer. In pyroclastic fl ow reservoirs, sometimes, after the flow stops, "fossil fumarole chimneys" or gas ou tlet chimneys are formed due to the separation of fine ash-sized material by the gas effect. Structures formed as a result of th e enrichment of heavy crystalline, lithic and larger vesicul ar pieces in vents are one of the most important data in distinguishing primary py roclastic d eposits from epiclastic flows fo rmed as a result of the flow of volcanic materi al (Helvacı and Erkül, 2001). Pyroclastic flows settle at high temperatures. Pyroclastic flows are also mechanisms that preserve temperature w ell. Therefore, hot pyroclastic flows may 40 CONCLUSION ✓ The pyroclast is defined as crumbs thrown out of volcanic vents, regardless of the orig in of the grains and their eruption patterns. ✓ Pyroclastic rocks are fo rmed by the transport, accumulation and consolidation of pyroclastic material produced by a volcanic eruption by air or water. ✓ Pyroclastic e ruptions are examined in four sections: Hawaiian - type, Stromboli-type, Vulcano -type and Plinian-type eruptions, according to magma density, viscosity, temperature, g as content and chimney height. ✓ Pyroclastic eruptions are deposited as debris, flows and turbulence deposits. 47 REFERENCES Chang, L., Cao, L., and Gao, F. (2009). Handbook of Igneou s Rock Identificatio n , Geological Publishing House, Beijing, pp. 95 – 115. Crowe, B.M., Linn, G.W., Heiken, G. and Bevier, M .L. (1978). Stratigraphy of Bandelier Tuff in the Pajarito Plateau; Applications to waste management. Los Alamo Sci. Lab., New Mexico, Informal Rpt., LA - 72 25, 1-57. Gorshkov, G.S. (1959). Gigantic eruption of the volcano Bezym ianny. Bull. Volcanol., 20, 77 -109. Hay, R.L. (1959). Formation of the crystal-rich glowing avalanche deposits of St. Vincent, B. W. I. J. Geol. 67 , 540 -562. Helvacı ve Erkül, (2001). Volk aniklastik Kayaçların Oluşumu, Genel Özellikleri ve Sınıflaması, Dokuz Eylül Üniversitesi Mühen dislik Fakültesi Jeoloji Mühendisliği Bölümü, Ders Notları. Hoplitt, R.P. and Kellogg, K.S. (1979). Emplacement temperatures of unsorted and unstratified deposits of volcanic debris as determin ed by paleomagnetic techniques. Geol. Soc. Amer. Bull. Part I, 90, 633 - 642. Huang, Y., Wang, P., Shao, R. (2010). Porosity and permeabilit y of pyroclastic rocks of the Ying cheng Formation in Songl iao basin. J. Jilin Univ. (Earth Sci. Ed.), 40 (2), 227 – 236. Schmincke, H.-U. (197 3). Magmatic evolution of tectonic regime in Canary, Madeira and Azores Island Gro ups. Geol.Soc. Amer.Bul l., 84, 633 - 648. Sparks R.S.J. and Walker, G.P.L. (1977). The significance of vitric-enriched air- fall ashes associated with crystal-enr iched ignimbrites. J. Volcanol. Geotherm. Res., 2, 329 -341. Sparks R.S.J ., Self, S. and Walker, G.P.L. (1973). Produ cts of igni mbrite eruption. Geology, 1, 115 - 118. Sparks R.S.J. (1976). Grain size variations in ignimbrites and implications for the transport of pyroclastic flows. Sed imentology, 23, 1 47 - 188. Sun, S., Li, J., Zhu, Q., and Wei, H. (1987). History and present situation of classification and nomenclature of pyroclastic rocks i n China and abro ad. Earth Sci. — J. Wuhan Co ll. Geol. 12 (6), 571 – 577. Sun, S., Liu, Y., Zhong, R., Bai, Z., Li, J., Wei, H., and Zhu, Q. (2001). Classification of py roclastic rocks and trend of volcanic sedimento logy: a review. Acta Petrol. Mineral., 2 (3), 313 – 317+328. Taylor, G.A. (1958). The 1951 eruption of Mo unt Lamington, Papua. Austr. Bur. Min.Resour. Geol. Geophys. Bu ll., 38, 1 - 117. Walker, G.P.L. (1971). Grain size characteristics of pyroclastic deposits. J. Geol. 79, 696-714. 48 Walker, G.P.L. (1972). Crystal concentratio ns in ignimbrites. Contr. Mineral. Petrol. 36, 135- 146. Wang, Y., Wang , J., Wang, Q., Sui, F., Shi, H., Xu, Y. (2019). Diagenesis of volcaniclastic rocks and its control over reservoir performance: a case study of the Carboni ferous system in Chepaizi area, Junggar basin. J. China Inst. Min. Technol., 48 (2), 40 5 – 414. Yuan, Y., Rezaee, R., Yu, H., Zou, J., Liu, K., Zhang, Y. (2021). Compositional controls on nanopore structu re in different shale lith ofacies: a comparison with pure clays and isolated k erogens. Fuel, 303, 121079. Zhou, J., Li u, B., Shao, M., Yin, C., Jiang, Y., and Song, Y. (2022). Lithol ogic classification of pyroclastic rocks: A case study for the third member of the Huo shiling Fo rmation, Dehui fault depression, Song liao Basin, NE China. Journal of Petroleum Science and Engineering, 2 14,110456. URL -1 Vikipedi, Piroklastik Kayaçla r https://tr.wikipedia.org/wiki/Pirokl astik_kaya%C3%A7 adresinden 10 Aralık 2023 tarihinde alınmıştır. URL - 2 Wikipedia, Types of volcanic eruptions. htpp://en.wikipedia.org/wiki/Types_ of_volcanic_eruptions adresinden 10 Aralık 2023 tarihinde alınmıştır. 49 Chapter 3 Effects of Operating Parameters on NO X Emıssıons in Diesel Engines Adem TÜYLÜ 1 Kubilay HAN 2 Yasin AKIN 3 INTRODUCTION Diesel engines are preferred in the automotive sector, particularly in heavy - duty vehicles, du e to their high torque outp ut and low fuel consumption. Although electric vehicles are becoming more widespread, internal combustion engine vehicles continue to be used due to issues such as battery life and deficiencies in charging station infrastructure. Internal combu s tion engines release various exhaust gases that have adverse effects on t he environment and human health. Among these emissions, hydrocarbons (HC) and carbon monoxide (CO) are primary concerns fo r Otto engines, while nitro gen ox ides (NOx) and particulate m atter are majo r issues for diesel engines. The negative effects of NOx emissions include respiratory problems and lung diseases in humans, as well as the formation of acid rain through chemical interac tions with water, oxygen, and other compounds in the atmosphere. Legal regulations restrict these harmful emissions, with the upcoming Eu ro VII emission standards, exp ected to be effective by 2025, aiming for even stricter limits (Demir et al., 2023; Calam et al., 2022; Syed and Reng anathan, 2022; Mu lholland e t al., 2022; Böğrek et al., 2021). In diesel engines, the relatively high levels of NOx emissions stem from the operational conditions of the engine. Diesel eng ines operate with fu el -lean mixtures compared to Otto engines and have high er compression ratios. Consequently, more oxygen is involv ed in the combustion in diesel engines, leading to higher combu stion temperatures. These two factors contribute to the high levels of NOx emission s in diesel engines. However, operational parameters of diesel engines, fuel qu ality, and emission reduction technologies installed in 1 Arş. Gör. Adem TÜYLÜ Sakarya University Of Appli ed Sciences Faculty of Techno logy Mechanical Engineering, ademtu [email protected] ORCID No: 0000 - 0001 -9828 -1573 2 Arş. Gör. Kubilay HAN Sakarya University Of A pplied Sciences Faculty of Technology Mechanical Engineering, kubilayhan@subu .edu.tr ORCID No: 0000 - 0003 -1472-2832 3 Arş. Gö r. Yasin AKIN Sakarya University Of Ap plied Sciences Faculty of T echnology Mechanical Engineering, yasinakin @subu.edu.tr ORCID No: 0000 - 0003 -3201 -379X 50 the exhaust system have significant effects on the amount of NOx emissions released in the exhaust gases. Impro vements in the fuel, such as th e addition of various fuel additiv es, the use of alternativ e fuels, and th e utilization of low - nitrogen diesel fuel can reduce NOx emissions from diesel engines throug h pre - combustion enhancements. Additionally, post -combustion NOx emissions are reduced through the Selective Catalytic Reduction (SCR) technology installed in the exhaust system before being released into the ambient air (Çelebi et al., 20 21; Tüylü, 2021; Tü ylü vd., 2019 ; Koebel et al., 2000; Haşimoğlu and İçingür, 2000). In this study, th e types and formation mechanisms of NOx emissions were first explained. Subsequently, the effects of operational parameters in fluencing the combustion process on NOx emissions, particularly focusin g on reducing effects, were discussed. Studi es in the literature on the reduction of NOx emissions with operational parameters were co mprehensively evaluated i n subheadings. NOx EMISSIONS IN DIESEL EN GINES The most influential factors in the formation of NO x emissions in diesel engines are cylinder ox ygen concentration and cylinder temperatures. NO x emissions begin to form when cylinder temperatu res exceed 1800 K. NO x includes various nitrogen oxide compo unds such as NO, NO 2 , N 2 O, N 2 O 5 , and NO 3 . Approximately 95 % of diesel engine NO x emissions consist of ni trogen monoxide (NO), with the remaining 5% composed of other compounds (Varatharajan and Ch eralathan, 2012; Chen et al., 2018). NOx FORMATION REACTIONS As explained above, the vast majority of NO x emissions consist of NO emissions. In this section, the mechanisms and reactions fo r the formation of nitric oxide (NO) and nitrous oxide (N 2 O) are des cribed. Thermal NO Formation This mechanism is the pr imary source of NO x emissions. It occur s when nitrogen (N) and oxygen (O 2 ) react at cylinder temperatures above 1800 K. These reactions are kn own as the Zeldovich mechanism (Var atharajan and Cheralathan, 2012). N 2 + O ↔ NO + N N + O 2 ↔ NO + O N + OH ↔ NO + H 51 Prompt NO Formation It represents the formation of NO in th e combustion process where the mixture is fuel-rich, and temperatures are r elatively low inside the cylinder. The reactions for Prompt NO formation are provided below (Varatharajan and Cheralathan , 2012). CH + N 2 ↔ HCN + N C 2 + N 2 ↔ 2CN CN + O 2 ↔ NO + CO NO and N 2 O Formation Rea ctions The reactions belo w take place in conditions where the cylinder pr essure is high, and the cylinder filling is low, at high air/fuel ratios during the combustion process. Oxygen atoms react with nitrogen gases (N 2 ) to form N 2 O. Th e N 2 O formed in the initial reaction can later react with oxygen to produce NO (Varatharajan and Ch eralathan, 2012). O + N 2 + M ↔ N 2 O + M N 2 O + O ↔ NO + NO REDUCTION METHODS OF NOx EMISSIONS IN DIESEL ENGINES Exhaust Gas Recirculation ( EGR) EGR (Exhaust Gas Recirc ulation) is one of the most effective method s for reducing NO x emissions from diesel engines. It in volves recirculating exh aust gases containing inert, high heat capa city CO 2 , and H 2 O (water vapor) into the intake air. This results in a chan ge in the characteristics of the in take air, leading to a reduction in NO x emissions. Th e addition of these compounds to the intake air decreases th e O 2 content in the intake air. Additionally, these compounds with high heat capacity cause a reduction in peak combustion temperatures. The decrease in c ylinder O 2 concentration and post-combu stion peak temperatures due to EGR results in th e redu ction of NO x emis sions. However, it should be noted that the app lication of EGR leads to an increase in particulate matter emissions and a deterioration in engine performance. EGR can be implemented th rough internal and external systems. Many modern diesel eng ines are equipped wit h turbochargers. Internal EGR involves the inclusion of bu rned exhaust gases in the next cycle by modifying intake and exhaust timing s, valve opening and closing times, and valv e duration. This is achieved through the manipulation of valves, employing variable valve activation 52 technology. In cold EGR applications, exhaust gases are subjected to intercoo ling before being introduced into th e intake air (Figure 1). In hot EGR app lications, exhaust gases are mixed with the intake air without undergoing any cooling process. Cold EGR is mor e effective and efficient compared to hot EGR but is also more costly (Pradeep et al., 2007; Haşimoğlu et al., 2002) . Figure 1. EGR scheme (L ou et al., 2022) When implementing EGR, the percentage of EGR can be calculated usin g the following equation (Pierpont et al., 1995). Since the ambient % CO 2 is relatively small and is considered as zero in the equation, the EGR ratio is calculated by dividing the percentage of CO 2 in the intake air by the percentag e of CO 2 in the exhaust air. %CO 2(intake) − %CO 2(ambien t) %CO 2(exhaust) − %CO 2 (ambient) × 100 In conclusion, Exhaust Gas Recirculation (EGR) reduces NO x emissions by lowering peak temperatures in the combustion process through the high heat capacity compounds H 2 O and CO 2 , and by reducing the amount of O 2 introduced into the cylinder. However, EGR can lead to increases in other emissions, particularly particulate matter, and a deterioratio n in engine performance. Therefore, EGR is app lied by op timizing parameters such as eng ine load, turbocharging, intake air temperature, etc., in a combined and coordinated manner (Maiboom et al., 200 8; Hountalas et al., 200 8). NO x Emission Reduction thro ugh Combustion Strategies Combustion strategies wi th low -temperature comb ustion (LTC) such as Homogeneous Charge Comp ression Ignition (HCCI), Reactivity Controlled Compression Ignition (RCCI), and Premixed Charge Compression Ignition 53 (PCCI) result in combustion at lo wer temperatures compared to traditional diesel engines (Fig ure 2) . Particularly, in the HCCI strategy, combu stion occur s with fuel-lean mi xtures and at lower temperatures, providing an opportunity to simultaneously reduce soot and NO x emissions (Kutluata, 2002; Dong et al., 2018; Krishnam oorthi et al., 2019). Creating a ho mogeneous fu el -air mixture in combustion s trategies can be achieved by making changes in fuel injection timings. In addition to the main fuel injection timing in traditional diesel eng ines, pilot, early, a nd late fuel i njections (Figure 3) are used to create a homogeneous charge (Zhao, 2007). Figure 2. Low temperature co mbustion (LTC) strategies op erating ranges (Duan vd., 2021) Figure 3. Fuel injection timing types for homogeneous fuel -air mixtur e (Zhao, 2007) 54 Effect of Fuel Injection Stra tegies on NO x Emissions One of the parameters that significantly influences the reduction of NO x emissions in diesel engines is fuel injection strategies. Particularly, performing multiple fuel injections per cycle results in notable reductions in NO x emissions compared to a single main in jection scenario. Moreover, the multiple injection strategy has the potential to simultaneously redu ce both NO x and soot emissions without compromising engine performance (To w et al., 1994; Sindhu et al., 2018). On the other hand, delaying the fuel injection timing , in other words, reducing the advance leads to a decrease in ignition delay resulting in a redu ctio n in NO x emissions (Shundoh et al., 1992; Cheng et al., 2016). In numerical stud ies, Wang et al. (2007) investigated the effects of fuel injection advance and multip le injection strategies on engine perfo rmance and emissions. They found that in single, 3 -stage, and 5-stage injection strategies with the same start of f uel injection, as the number of stages increased, NO x emissions decreased. In other word s, multiple injections resulted in lower NO x emissions compared to a single injection. Additionally, they noted that reducing the injection advance from -10 CA to 5 C A for fuel spray strategies resulted in NO x emission reduction . In conclusion, multiple injection s and reducing fuel in jection advance have a mitigating effect on NOx emissions. Effect of Fuel Injection Pressur e on NO x Emissions In diesel engines, as the fuel injection pressure increases the diameter of the fuel particles sprayed from the injector decreases leading to a reduction in the penetration area s within the cylinder. As the injection pressure increases, a relatively homogeneous fuel-air mixture is formed i n in cylinder, resulting in a decrease in ignition delay. Th erefore, an increase in injection pressure leads to a reduction in NO x emissions (İçing ür and Altiparmak, 2003). However, studies using biodiesel as fuel in diesel engin es have shown different trends in NOx emissions in response to increasing injection pr essure (Jindal et al., 2010 ; Deokar and Harari, 2021). Effect of Intake Air Characteristi cs on NO x Emissions The physical and compositional characteristics of intake air pl ay a crucial role in diesel engine performance and emissi ons. The effects of intake air temperature, pressure, and oxygen content on combustion and emissions have been investigated through expe rimental and numerical studies. Jeevahan et al. (2019) examined the in fluence of intake air oxygen (O 2 ) con centration on the performance and emissions of a single-cylin der di esel engine. They adjusted the intake air O 2 concentration to 21%, 23 %, 25%, and 27% un der no rmal conditio ns. 55 Under full -load condi tions, they ob served NO x formations of 2435 pp m when the intake air O 2 concentration was 21% and 5599 ppm when it was 27%. Th ey noted that the improvement in combustion and the increase in post -combustion temperatures with hig her oxygen concentration led to increased NO x emissions. Li et al. (1997) conducted experimental studies on a direct-injecti on, water- cooled diesel engine to i nvestigate the effects of intake air pressure and oxygen concentration on eng ine performance and emissions. To clearly observe the effects of these two fa ctors on emissions and performance, they maintained the engine speed at 1800 rpm, intake air temperature at 300 K, and th e injected fuel quantity per cycle at 30.2 mg/cycle. They set the intake air pressure to 1.1 bar, 1.5 bar, and 2 bar, and the oxygen concentration in the inhaled air to 21%, 19.5%, and 18.8%. T hey diluted the oxygen conce ntration in the inhaled air to 19.5% by adding carbon diox ide to the intake air. Similarly, by add ing argon and nitro gen gases to the intake air, they reduced the normal 21% oxygen concentration to 18.8%. They fo und that increasing intake air pressure led to a decrease in NO x emissions, and they associated this decrease with the decrease in ignition delay due to in creased inhaled air pressure. On the other hand, add ing inert gases to th e intake air resulted in reduced oxygen concentrations, leading to a decrease in NO x emissions. Particularly, under operating conditions with an intake air pressure of 2 bar and an oxygen concentration of 18.8%, they achieved significant reductions in NOx emissions. Increasing intake air temperatures in diesel engines through various methods lead to higher peak temperatures at th e e nd of combustion. The increase in peak temperature values has an enhancing effect on NO x emissions (Haraldsson et al., 2002; Gowthaman and Sathiyag nanam, 2018). Effect of Air-Fuel Ratio on NO x Emissions The air-fuel ratio (AFR) is one of the most influential paramet ers affecting combustion and emissions in internal combustion engines. As indicated by the equation below (Chatlatanagulchai et al., 2010), excess air coefficient ( 𝜆 ) denotes whether the mixture in the cylinder is fuel -rich, fu el-lean, or stoichio metric. There are many publications in the literature that discuss the changes in emissions according to the excess air coefficient. NO x emissions are observed to be at their maximum when 𝜆 =1.1, and they decrease when 𝜆 is belo w or abo ve 1.1 (Figure 3). The trends in NO x emissions can be explained by the combustion efficiency of fuel-rich and fu el-lean mixtures, which leads to a decrease in combustion temperatures. 56 44. Varatharajan, K., & Cheralathan, M. (2012). Influence of fuel properties and compo sition on NOx emissions from biodiesel powered diesel engines: A review. Renewable and sustain able energy reviews, 16(6), 3702 -3710. 45. Wang, D., Zhang , C., & Wang, Y. (2007). A numerical stud y of multiple fuel in jection strategies for NOx reduction from DI diesel engines. Internatio nal Journal of Green Energy, 4(4), 453 -470. 46. Zhao, H. (2007) . HCCI and CAI engines for the auto motive industry. Elsevier 47. Zhu, L., Zhang, W., Liu, W., & Huang, Z. (201 0). Experimental study on particulate and NOx emi ssions of a diesel engine fueled with ultra low sulfur diesel, RME -diesel blends and PME-diesel blend s. Science of the Total Environment, 40 8(5), 1050-1058. 63 Chapter 5 In -Situ Hydrogen Peroxide and Hydrogen Production in Wastewater Treatment with Fenton-Fenton Like Oxidation Ayşe Elif ATEŞ 1 Sinan ATEŞ 2 1- I NTR ODUCTI ON Purifying water and reusing it as both i ndust rial and drinking water i s of great importance in preventing water scarcity. However, with increasing industrialization in recent years, efforts to provide clean energy production during wastewater treatm ent are increasing. Biogas, biodiesel, and hydr ogen energy can be gi ven as examples of clean energy (Hu, L., 2023 : 177 ). Due to the rapid increase in population, th e need for energy and water has in creased globally, and according ly, energy and water res erve s are facing difficulties in meeting the need (Wang , Y., 2023 : 3 07 ). In addi tion, the fact that polluting gases due to indu strialization accelerate climate cha nge and that the need for water and energy will increase in the next 30 years has encouraged researchers to develop methods that can solve both crises simultaneously (Sun, J., 2022 : 168) (Hu, L., 2023 : 177 ). However, the studies carried out are generally on a laboratory scale and are in the testing ph ase for use in large -scale industries. The priority in th e stud ies is generally to provide energy supply from renewable energy. Here, when choosing a renewable energy supply system, variables such as th e geological, meteorological, material and social situation of th e region should be taken into consideration. Researchers ge nerally recommend add ing en ergy storage syste ms to the process to improve the system (Ch eng, S., 2021: 46 ). Hydrogen energy has been one of the important fields of study in recent years, both in terms of its ability to be obtained du ring water treatment and as renewable en ergy. Th e important advantages of hydrogen energy are that it is storable, has a high calorific value, and does not create po lluting gases. Despit e these advantages, the fact th at hydrogen fuel canno t be produced directly is a significant disadvantage. Generally, gasification , electrolysis, and reformin g o f 1 Res. Asst.. Gör.; İstanb ul Üniversitesi -Cerr ahpa ş a Mühendislik Fakültesi Çevre Mühendi sli ğ i B ölümü, [email protected] ORCID No: 0000 -0001-5391-7478 2 İstanbul Üniversitesi - Cerrah paşaMühendislik Fakü ltesi Çevre Mühendisliği Bölümü, [email protected] ORCID No: 0000 -0003-0967-2367 64 fossil fuels are used in the production of hydrogen energy (Chen, Y.,2022: 81 ) (Hoang, A. T., 2022: 47 ) (Zhang, H., 2022:104). Although it is challenging to use these met hods in the productio n of hydrogen ener gy, they have been tur ned into an advantage by researchers because they are methods used in water purification. Hydrogen energy prod uction pr ocesses integrated with water treatment are advanced oxidation processes and in clude method s usin g hydrogen peroxide (H 2 O 2 ), ozone (O 3 ), electrolysis a nd ultraviolet lamps (Liu, C. , 20 2 3: 52 ). In these advanced oxidation systems, pollutants are oxidized as a result of electron transfer or chemical interaction. In addition, studies have shown that electrochemical methods ar e more effecti ve in oxidizing pollutants. This can be said to be due to the high er number of radicals fo rmed during the process. Electro-Fent on and Photoelectro -Fenton ox idation methods are advanced oxidation processes frequently used in wastewater treatme nt because H 2 O 2 is produced by cathodic reduction (Behrouzeh, M.,2022 : 15 ). In studies conducted in the literature, Electro -Fenton oxidation's low op erating costs and high wastewater treat ment efficiencies are among its critical advan tages. It is also one of the advanced oxidation processes that can be used on an industrial scale (Campos, S., 20 23:169). However, although wastewater treatment can be done by Electro -Fenton oxidation , desalin ation cannot be do ne. It is seen that the electrodialysis method is widely used in the literature for desalination (Jia , Y., 203:48). Fenton Oxidation It is stated in the literature that the redox po tential of the hy droxyl radical (•OH) formed as a result of the reaction in adv anced ox idation processes is 2.8V. Compared to other advanced oxi dation processes, Fenton oxidation provides the formation of more hydroxyl radicals through the decomposition of H 2 O 2 . In addition, the formation of hydroxyl radicals in this process is rapid and easy to op erate (Liu, Y., 2021: 404) . In Fenton oxidation, H 2 O 2 is a chemical us ually added externally. However, transportation and storage of H 2 O 2 is a costly and risky process, which limits the use of this process on large scales. To overcome this disadvantage , researchers provide oxygen activation so th at H 2 O 2 can be produced in situ during Fenton oxidation. Thus, the process can be carried out in a less costly and safe ma nn er with out reducing the hy droxyl radicals that will be produced during Fenton oxidation (Asghar, A., 20 15: 87 ) (Yang, Z., Zhang, X. , 20 19: 250) (Pi, L., 20 20: 189) (Zhou, W., 2019: 225). By integrating ox ygen activation into electrochemical, photochemical and chemical methods, H 2 O 2 can be produced in situ. These processes can operate homogeneously or heterogeneously . In electroche mical methods, oxygen is 65 reduced to H 2 O 2 by taking electrons from th e cathode. In photocatalytic oxidation, photoelectons coming from semiconductor materials un der UV light activate ox ygen. This situation is directly affected by oxygen activ ation and environmental con ditions in th e on -site production of H 2 O 2 (Pi, L., 2020: 18 9) (Liu, Y., 2021: 404). Alt hough ir on-containing chemicals are ge nerally used as catalysts in Fenton and Fenton -like ox idation processes where H 2 O 2 is produced on -site, different catalysts t hat do not contain iron are also used. However, iron - containing catalysts are frequently used in studies du e to their low cost and high growth efficiency ( Bokare, A. D., 2014: 275 ) (Su, P., 2019 . 245) . H 2 O 2 PRODUCTION IN THE FEN TON OXIDA TION PR OCESS Iron, a zero -valent metal, is frequ ently preferred in Fenton and Fenton -like oxidations due to its low cost and ease of applica tion. In Fenton oxid ation, which is carried out with the on -site productio n of H 2 O 2 , the iron required for the reaction to occur is provid ed. Other zero-valent metals used in the stud ies are Al, Zn , Mg and Cu (shown in Figure 1) . In addition, by using iron electrodes in Electro -Fenton oxidation, the necessary iron is given to the environment in situ and the reaction tak es place. Fenton and Fenton-like oxidation occurs under acidic environment (p H=2 -4) condi tions (Liu, Y., 2021: 404) (Liu, Y., 2019: 671). Figure 1: Reactions of zero -valent metals in in -situ production of H 2 O 2 Studies have shown that the reduction capacity of zero-valent copper is weaker com pared to iron and aluminum. However, considerin g th e redox potential, it has been exp lained in these studies that it is thermodynamically possible to produce H 2 O 2 in situ with the presence of sufficient oxygen in the en vironment . In addition, when cop per is used, s uper oxide radicals (O 2 .- ) are 66 formed along with hydr oxyl radicals, unlike other zero -valent metals, with th e activation of oxygen (Wen, G., 2014: 27 5) (Liu, Y., 2021: 404). Ano ther advantage of using copper in the treatment of wastewater is that it dissolves in wide pH ranges and hi gh efficiency results can be obtained in neutral pH conditions . Anot her advantage of using copper in the treatment of wastewater is its stability and its ability to dissolv e in wide pH ranges, resulting in highly efficient results in neutral pH con diti ons ( Do ng, G. , 2014: 66). To enh ance the efficiency of Zero -Valent Metals (ZVMs) in O 2 activation, bi - met als consisting of two metals with different redo x potentials are synthesized. This can ex pedite O 2 reduction in aqueous solu tions by establishing corrosion cells. Incorporating Fe 0 was found to notably enhance the activity of Al 0 for O 2 activation. Additionally, Fe 0 doped with Cu 0 accelerated the degradation of or ganic contaminants, e xhibi ting greater reactivity compared to Fe 0 alon e (Fan, J., 2015: 26 3) (Fan, J., 2016 : 23 ). D eta ile d equations for the reactions in Fenton and Fenton - like oxidation processes are provided below (Liu, Y., 2021: 4 04). Fi gure 2: Production of H 2 O 2 in Electo-Fenton oxidation of Fe 2+ (aq and s) and its use in the reaction The Electro-Fenton/Fenton -like process involves activating O 2 electrochemically, generating H 2 O 2 on the cathode surface thr ough the 2 - electron O 2 reduction pathway. This process employs Fe -based catalysts, both homogeneous and heterogeneous, for the catalytic breakdown of H 2 O 2 into hydroxyl radicals (•OH) throu gh the electrode reaction. Th e Fenton process, rooted in electrochemical O 2 activation, is versatile, with classifications like electro-catalysis activation of O 2 , fuel cell activatio n of O 2 , and corrosion cell activation of O 2 . O 2 reduction on the cathode surface can yield H 2 O thro ugh the direct 4-elect ron path way or H 2 O 2 th rough th e 2 -electron pathway, depending on the cathode material's ty pe and characteristics (Liu, Y., 2021: 404). 67 The crucial role of cathode ma terial selectivity in facilitating the in-situ generation of H 2 O 2 on the cathode surface is evident in various advanced oxidation processes, particula rly in electro-Fent on/Fenton -like systems. To achieve this, a diverse array of cathode mate rials has been harnessed, including noble metals, metal alloys, and carbon -based materials. Carbon -based materials , with their distinctive attributes such as hi gh stability, low to xicity, cost - effectiveness, and pronounced selectivity toward the 2-electron pathway of oxygen (O 2 ) reduction, have emerged as pivotal candidates for in -situ H 2 O 2 generation (Zhuang, S., 2019:253) (Liu , Y., 2021: 404). In electro- Fenton/Fent on -like processes, O 2 in the solution can be obtained from O 2 gas, air aeration, or generat ed in-situ on an anode through water electr olysis. Two main methods supply Fenton catalysts: direct addition of homogeneou s catalysts (Fe 2+ or Fe 3+ ) or immobilizati on of iro n on el ectrode materials for O 2 reduction and H 2 O 2 generation, actin g as a source fo r catalyti c br eakdown into hydroxyl radicals (•OH) (Liu , H., 2007 : 41) (Yang, S., 2018 :8). These processes, offering cost savin gs and reduced risks of H 2 O 2 handling, maintain Fenton catalyst activity by reducing ferric ions (Fe 3+ ) to ferrou s ions (Fe 2+ ) a t the cathode. However, ch allenges lik e hi gh energ y consumption and the need for supporting electrolytes hind er practical implementation (Liu, Y., 2021 : 404). The production of H 2 O 2 is calc ulated with the faradic current efficiency formula given in the e quation belo w (Garza-Campos, B., 2018:2 69) (Zhang, C., 201 5: 160). C H2O2 = H 2 O 2 concentration, mol/L F= Faraday constant (96,485 C/mol) n=Number of electrons transferred during the reduction o f oxygen to H 2 O 2 . V= Volume (L) I= current (A) t = time (s) H 2 PRODUCTION IN T HE FENTON OX IDATION PROCESS Water electro lysis, commo nly known as water splitting, is a primary method for hy drogen (H 2 ) production within the context of a fu turis tic sustainable energy system. Water electrolysis is a fundam ental process that entails the decomposition of water into its constituent elements, H 2 and oxygen, and holds significant promise for a diverse range of energy applications, encompassing 68 electricity ge neration, transportation, heating, and chemical production. This process hinges on the orchestrated movement of electrons within a closed circuit. An electrolysis unit comprises key compo nents, including an ano de, a cathode, an electrolyte, and a pow er suppl y (refer to Fig ur e 1 for a sche matic representation). The field of electrolyzer technology recognizes three pr imary types: polymer electrolyte membr ane electrolyzers, alkaline electroly zers, and solid oxide electrolyzers, each offering dist in ct advantages and applications in the realm of sustainable energy systems. (Aydin, M. I., 2021: 279 ) (Tak, S. , 2022:47). In a con ventional water electroly sis process driven by electricity, the transformation of water occurs, leading to the generatio n of oxygen g as at the anode electrode and H 2 at the catho de electrode (Yi, S., 2023 :91). This fundamental electroche mical proces s serves as a versatile method for H 2 production, playing a crucial ro le in th e realm of sustainable energy. Alternatively, there exists a no ther method based on the ox idation of iron, which presents a distinctive app roach with potenti al advantages ov er the traditional water electrolysis process. This iron oxidation process is characterized by its reduced energy requirements compared to standard electrolysis. The utilization of iron oxidation as an alternative pathway for water electrolysis highlights the diverse strate gies employed to harness H 2 as a clean and renewable energy source. Ferrous ion may be pr oduced using the iron oxidation proces s (Nuengmatcha, P., 2023) . When ferrous ion is exposed to anode potential, it can be converted to ferric ion (Hu, L., 2023:177) . Contrasted with the energy demand of the oxygen evolution reaction, th e preceding electrochemical reaction demands a remar kable 69% less energy, underscoring its energy efficiency and potential as an economically viable process for H 2 production. This noteworthy reduction in energy consumption opens avenues for more sustainable and cost -effective approaches to electrolytic H 2 generation. Delving into the specifics of the chemical reaction occurring o n the cathode electrode of an elec trol yzer utilizing the iron oxidation process provides valuable insights into the mechanisms driving this en ergy -efficient reaction. Th e elucidati on of this electrochemical reaction not only contribut es to our understandin g of the fundamental pr ocesses involved but also sheds light on the distinctive features that make the iron oxidation - based electrolysis method a 69 promising contender in the landscap e of H 2 production technologies (Hu, L., 2023:177). In contrast to the conventional water electrolysi s method, the chemical reaction described above boasts a noteworthy 38% redu ction in energy consumption for H 2 production. Th is substant ial decrease in energy requirements not on ly positio ns the process as a more enviro nmentally sustainable alternative bu t also introdu ces the possibility of harnessing renewable energy sources, such as solar energy systems, to power th is H 2 generation technique. The piv otal role of H 2 O 2 in the formation of a Fent on-type reagent at the anode add s a layer of comple xity to the electrochemical processes involved. As long as a suffi cient supply of H 2 O 2 is maintained, the anode becomes a site for the con tinuous generation of the Fenton -type reagent, accentuating the self-sustaining nature of the electrochemical system. This intricate interplay of chemical reactio ns and renewable energy integration highlights the multifaceted po tential and versatilit y of the described H 2 production method in the realm of sustainable energ y technologies .Iron ions can be obtained electroche mically. via contrast, H 2 O 2 is created via an electro - Fenton process by an electrochemical reaction involving t he cathodic reduction of dissolved oxygen (Brillas , E. , 2020:250) . The electro-Fenton technique is a highly recommended advanced oxidation method for wastewater treatment applications. Furthermore, the oxidizing power of H 2 O 2 can be increased by adding Fe to treated wastewat er (Shok ri, A., 2023:172 ) (Hu, L., 2023:17 7) . In the literature, The rate of H 2 production is calcu la ted based on Faraday's law (Hu, L., 20 23:177) (Shen, Y., 2021: 4 7). q= electrical charge M= molar mass of H 2 70 F= Faraday constant (96,485 C/mol) t cell = overall operation time o f the cell H 2 production efficiencies in light and dark conditions have been compared in the literature. In this study, it is see n that H 2 production i ncreases with increasing voltage. Additionally, H 2 production increases when the syst em operates in bright conditions . In the stud y, the H 2 production rate increases approximately 10 times as the voltage in creases from 1.7V to 2.5V ( Aydin, M. , 2022: 256). RESULT In comparison to the tradi tional water electrolysis app roach, the chemical reaction elucidated above not only manifests a significant 38% reduction in energy consumption for the production of H 2 but also establishes itself as a compelling option for environmentally sustainable practices (Navarro- Solís, I., 201 0:35). This marked decrease in energy requirements not only signifies the method's potential fo r reduced environmen tal impact but also opens up avenues for exploring renewable energy sources, with a pa rticular emph asis on solar energy systems, as viable power in pu ts for this H 2 generation techn ique (Hu, L., 2023:177 ). The intricate dynamics of H 2 O 2 in facilitating the formation of a Fenton -type reagent at the anode introduce a nu anced layer to the un derlying electrochemical processes. The continuous gen eration of the Fenton -type reagent at th e anode, contingent upon maintaining an ample sup ply of H 2 O 2 , underscores the i nherent self-sustaining natu re of the electrochemical system (Liu, Y., 2021: 404) (Liu, Y., 20 19: 671). This complex interplay of chemical reactions and the integr ation of renewabl e energy sources not only showcases the method's multifaceted potential but also underscores its adaptabili ty and versatility within the realm of sustainable energy technologies (Fan, J., 2015: 263) (Fan, J. , 2016: 23) (Dong, G., 2014: 66). The synergistic relationship between energy efficiency, environmental impact, and renewable energy integration positions this H 2 production method as a promisin g con tributor to the on going pursuit of sustainable and clean energy solutions. Furthermore, due to limitatio ns in the environment, the sector is compelled to adequately treat wastewater for reuse. In the stud ies carried out, if H 2 O 2 is used in the treatment of wastewater, on-site productio n can be carried out to reduce the cost and overcome the difficulties in sto ring and transp orting th e chemical ( Wen, G., 2014: 275 ) (Liu, Y., 2021: 404) (Liu, Y., 2019 : 671). One of the important reasons why advan ced oxidation methods usin g H 2 O 2 are widel y used is tha t 71 high treatment efficiencies can be achieved in the treatment o f resistant industrial wastewater (Hu, L., 20 23:177). New studies enable the pr oductio n of H 2 energ y, which is a renewable e nergy, while producing H 2 O 2 on site. Although H 2 production seems possible in studies, studies on its use as energ y in the industry are quite new and stor age and usage technologies are being developed (Ayd in, M. I., 2021:279 ) ( Lu , Y. , 2011: 36 ). 72 Parameter Unit Value COD mg /L 189.600 BOD 5 mg /L 993 TN mg /L 215 TP mg /L 0,45 Oil Grease mg /L 31 TSS mg /L 118 pH - 6,5 Since the DMSO content causes intense foam after the chemicals to be added for the Fent on reaction, the wastewater was aerated for 2 hours before the Photo-Fenton oxidation. For Photo-Fenton oxidation, the wastewater pH wa s adjusted to approximately 3 usin g 0.1 N H 2 SO 4 . For the process, 250 ml sample was us ed and FeSO 4 an d H 2 O 2 were added at variable concentrations determined in respo nse surface model ling. The variables used for response surface modeling are given in Table 2. Table 2: Actual values and coded values used in response surface modeling Variable Unit Actual Value Co ded Value Low High -Alpha +Alpha Low High -Alpha +Alpha Time (A) M in . 45 75 30 90 -1 1 -2 2 FeSO 4 (B) g/L 1.5 2 .5 1 3 -1 1 -2 2 H 2 O 2 (C) g/L 3 5 2 6 -1 1 -2 2 A schematic representation of the process setup is g iven in Figure 1. It was stirred under UV light for 1 hour to ensure th at the Fenton oxidation reaction occurred at high yi elds. A 40W UV-A lamp was use d as UV light. At the end of 1 ho ur, the pH was adjusted to>7. 5 using 0.1 N NaOH to terminate the rea ction. The chemicals used in the stud y are Merck b rand. After the study, the samples were centrifuged at 2000 rpm fo r 4 minutes and the COD removal efficienc y was calculated by taking the upper phase. Figure 1: Scheme of treat ment of DMSO-containi ng pharmaceutical industry wastewater by Photo -Fenton oxidation 79 RESULT AND DIS CUSSI ON FeSO 4 and H 2 O 2 concentrations and time were determined as variables. The ranges of these variables were chosen according to studies in the literature. In th e study, the FeSO 4 concentration is between 1-3 g/L and the H 2 O 2 con ce ntration is between 3-6 g/L. Th e duration was 90 minutes and samples were taken at di fferent times. Additionally, a 40w UV -A lamp was used for P hot o-Fenton. Studies were carried out at constant pH value (pH = 3). Modeling of COD removal from raw pharmaceutical industry wastewater was done with RSM. The exp erimental design and COD removal efficiencies required for RSM in the stud y are given in T able 3. Figure 2: Normal Plot o f residuals and Predicted vs Actual Table 3: Actual values and coded value s used in the experimental study for response surface modelling Run Actual Value Codded Value COD removal ef ficiency (%) A:Time (min) B:FeSO 4 (g/L) C:H 2 O 2 (g/L) A B C 1 45 1,5 5 -1 -1 +1 25 2 60 1 4 0 -2 0 23 3 45 2,5 5 -1 +1 +1 36 4 60 2 4 0 0 0 45 5 75 1,5 5 +1 -1 +1 28 6 60 2 4 0 0 0 46 7 60 2 4 0 0 0 45 8 45 1,5 3 -1 -1 -1 18 9 75 1,5 3 +1 -1 -1 21 10 60 2 4 0 0 0 46 11 75 2,5 5 +1 +1 +1 38 12 45 2,5 3 -1 +1 -1 26 13 60 2 4 0 0 0 45 14 60 2 6 0 0 +2 34 80 15 90 2 4 +2 0 0 57 16 60 2 2 0 0 -2 19 17 60 3 4 0 +2 0 41 18 30 2 4 -2 0 0 21 19 75 2,5 3 +1 +1 -1 23 20 60 2 4 0 0 0 46 The model formulation obtained in the surfac e respo nse modeling probe is given in equ ation 1. The equation expresse d in coded factors allows us to make predictions about the response b ased on specific levels of each factor. COD removal =+6,61 +0,4017A+0,3848B+0,4 175C-0,3528 B² -0,4789 C² Eq ( 1) Table 4: Adequacy of the model tested Source Sequential p- value R 2 Lack of Fit p-value Adjusted R² Predicted R² Linear 0,0428 0,3908 <0.0001 0,2765 0,0994 Suggested 2FI 0,9778 0,3997 <0.0001 0,1226 -0,8757 Quadratic 0,0133 0,7850 <0.0001 0,5915 -0,7371 Suggested Cubic 0,3865 0,8824 <0.0001 0,6275 -23,0793 Aliased Source Sum of Squares df Mean Square F-value p-value Mean vs Total 663,19 1 663,19 Linear vs Mean 7,74 3 2,58 3,42 0,0428 Suggested 2FI vs Linear 0,1768 3 0,0589 0,0644 0,9778 Quadratic vs 2FI 7,63 3 2,54 5,97 0,0133 Suggest ed Cubic vs Quadratic 1,93 4 0,4820 1,24 0,3865 Aliased Residual 2,33 6 0,3884 Total 683,00 20 34,15 Table 5: ANOVA results o f the study according to the quadratic m odel Source Coefficient estimate Sum of Squares df Mean Square F- value p-value Model 15,55 9 1,73 4,06 0,0198 S Intercept 6,61 A- Time 0,4017 2,58 1 2,58 6,06 0,0335 S B-FeSO 4 0,3848 2,37 1 2,37 5,56 0,0400 S C-H 2 O 2 0,4175 2,79 1 2,79 6,55 0,0284 S AB -0,0963 0,0742 1 0,0742 0,1741 0,6853 NS AC 0,0524 0,0220 1 0,0220 0,0516 0,8249 NS BC 0,1004 0,0807 1 0,0807 0,1894 0,6726 NS A² -0,2361 1,40 1 1,40 3,29 0,0997 NS B² -0,3528 3,13 1 3,13 7,35 0,0219 S C² -0,4789 5,77 1 5,77 13,54 0,0042 S 81 Residual 4,26 10 0,4258 Lack of Fit 4,25 5 0,8500 515,65 <0.0001 S Pure Error 0,0082 5 0,0016 Cor Total 19,81 19 In ANOVA analysis, a P-valu e less than 0.05 indicates that th e valu e is significant (S), while a P-value greater than 0.1 indicates that it is not significant (NS). Accordi ngly, wh en table 5 is examined, it is seen that A, B, C, B², C² are significant. Figure 3: Graphical repres entation of the quadratic m odel and th e coefficient of determination (R 2 ) for model terms associated with Chemical Oxygen Demand removal. a. 82 b. c. Figure 4: Graphs o f COD removal efficiency from raw ph armaceutical indu stry wastewater of H 2 O 2 and FeSO 4 concentrations and time variables , a.) FeSO 4 (mg/L)- Time (min.), b .) H 2 O 2 (mg/L)- Time(min .), c.) H 2 O 2 (mg/L)- FeSO 4 (mg/L) The use of UV lamps with Fenton oxidant increases the optical reduction of ferric io n. It is a lso an agent that increases the photolysis of hydrogen peroxide. Photo-Fenton oxidation is on e of the widely used meth ods for the degradation of different organic pollutants in wastewater . This is due to the formation of hydroxyl radicals resultin g from both the photolysis of hydrogen peroxide and the reduction of iron ions in acidic environments (p H2 -4). In literature studies, it was stated t hat the amount of iro n ions wa s recovered under UV light and did not decrease durin g the reaction (Eq 2 - 6) . Eq (2) Eq (3) Eq (4) 83 Eq (5) Eq ( 6) When gr aph 4 a,b is examined, COD removal efficiency increases with increasing time, regardles s of the FeSO4 and H 2 O 2 concentration. However, increasing the time fro m 30 to 90 did no t cause a significant increase in the yield. In addition, the low FeSO 4 concentratio n reduced the treatment efficiency. Th is is because the concentration required for th e reaction with H 2 O 2 cannot be achieved. Alth ough high concentration increa se s the purification efficiency, bein g above the optimum H 2 O 2 /FeSO 4 ratio causes coagul ation. In the H 2 O 2 - FeSO 4 graph in figure 4 c , it can be seen that the efficiency decreases at concentrations other than the optimum ratio. The optimum H 2 O 2 / FeSO 4 concentration was det ermined as 2. In addition, the high est purification efficiency, 46 %, was r eached after 60 minutes, and running the proces s for 90 minutes for the reaction i ncreases the cost. Th e inert of the chemicals in the wastewater r educed the treatment efficiency. How ever, in the study where Photo-Fenton oxidation was used for DMSO degra dation, it was observed that although the To tal organic carbon (TOC) removal efficiency was low, the degradation of DMSO was at high efficien cy (Behrou zeh, M. , 20 22:15) (de Luna, M. D. G., 20 13: 232). As seen in Figur e 5, after adding FeSO 4 and H 2 O 2 for photo-Fenton oxidation, an in tense amount of foam was formed. In addition, figure 5c sho ws that the foam decreases after the process but do es not disappear completely. When Figures 5 a and 5 c are compared, color appeared in the wastewater after Photo-Fenton oxidation. In this case, a different treatment process must be applied for color removal after the process. Th e Photo -Fenton oxidation process alone was not found suitable because the low pu rification e fficiency and the color caused after the process were du e to the high amount of solvent. 84 a. b. c. Figure 5: Wastewater images before and after Fenton oxidation a.) raw wastewater, b.) Before Pho to-Fenton oxidation, c.) After Photo-Fent on oxidation CO NCLUSION In the study, COD removal by Photo -Fenton ox idation in crude pharmaceutical industry wastewater containing DMSO was modeled with RSM. In the stud y, wastewater was aerated for 2 hours before Photo -Fenton ox idation. This is because aeration-fr ee Photo-Fenton oxidation causes dense foam when chemicals are added. At the end of the study, the optimum H 2 O 2 /FeSO 4 ratio was foun d to be 2 at pH 3. In addition, the highest treatment efficiency, 46% COD r emoval, was achieved after 6 0 minutes. Although the increase in efficiency does not contradict the literature, ox idation should be tried after at least 5 hours of ventilation to increase the efficiency. In addition to the UV process applied as a hybrid with Fenton o xi dation, it is recommended to add an electro process and try it in future studies as Photo -Electrofento n oxidation will increase hydroxyl radicals. Since t he increase in th e power of the UV lamp is another factor that increases hy droxyl radicals, a lamp w ith a higher power should be used in stead of a 40w lam p. 85 REFERENCES 1. Behrouzeh, M., Parivazh, M. M., Dan esh, E., Dianat, M. J., Ab basi, M., Osfouri, S., ... & Akrami, M. (2022). Application of Photo -F enton, Electro-Fenton, and Photo -Electro-Fenton proc esses for the treatment of DMSO and DMAC w astewaters. Arabian Journal of Chemistry, 15 (11), 104229. 2. Dalrymple, O. K., Yeh, D. H., & Trotz, M. A. (200 7). Removing pharmaceuticals and endocrin e‐disrupt ing compounds from wastewater by photocatalysis. Jou rnal of Chemical Techn ology & Biotechnolog y: International Research in Process, En vironmental & Clean Tec hnology, 82(2), 121 -134. 3. de Luna, M. D. G., Colades, J. I., Su, C. C., & Lu, M. C. (2013). Comparison of dimethy l sulfoxi de degradation by different Fenton processes. Chemical engineering journal, 232, 418 -424. 4. Gadipelly, C., Pérez - González, A., Yadav, G. D., Ortiz, I., Ibáñez, R., Rathod, V. K., & Marathe, K. V. (2014) . Pharmaceutical i ndustry wastewater: review of the technol ogies for water treatment and re use. Industrial & Engineering Chemistry Re search, 53(29), 11 571 -11592. 5. Guillette Jr, L. J., Crain, D. A., Gunderson, M. P., Kools, S. A., Milnes, M. R., Orlando, E. F., ... & Woodward, A. R. (2000). Alligators and endocrine disrupting contaminants: a curre nt perspective. American Zoologist, 40(3), 438 -452. 6. Goossens, H., Ferech, M., Coenen, S., Stephens, P., & European Surveillance of Antimicrobial Consumpt ion Project Group. (2007) . Comparison of outp atient systemic antibacterial use in 2004 in the United St ates and 27 European countries. Clinical infectious diseases, 44(8), 1091 -1095. 7. Kessler, R. (20 10). INDUSTRY ISSUES: pharmaceutical factories as a source of drugs in water. 8. Khetan, S. K., & Collins, T. J. (2007). Human pharmaceuticals in the aquatic environment: a challeng e to green chemistr y. Chemical reviews, 107(6), 2319 -2364. 9. Kümmerer, K. (2009). Antibiotics in the aquatic environment – a review – part I. Chemosphere, 75(4), 417 -434. 10. Klavarioti, M., Mantzavinos, D., & Kassinos, D. (2009) . Removal of residual pharmaceuticals from aqu eous systems by advanced oxidation processes. Environment in ternational, 3 5(2), 402-417. 86 11. Larsson, D. J., de Pedro, C., & Paxeus, N. (2007). Efflu ent from drug manufactures contains extremely high levels of pharmaceuticals. Journal of hazardous materials, 148 (3), 751 -755. 12. Mompelat, S., Le Bot, B., & Thomas, O. (200 9). Occurrence and fate of pharmaceutical products and by -products, from resource to drinking water. Environment internatio nal, 35(5), 803 -814. 13. Rice, E. W., Bridgewater, L ., & American Public Health A ssociation (Eds.). (2012). Stan dard methods for the examinatio n of water and wastewater (Vol . 10 ). Washington, DC: American public health association. 14. Orlando, E. F., Kolok, A. S., Binzcik, G. A., Gates, J. L., Horton, M. K., Lambright, C. S., ... & Guillette Jr, L. J. (2004) . Endocrine -disrupting effects of cattle feedlot effluen t on an aqu atic sentinel species, th e fathead minnow. Environmental health p erspectives, 112(3), 353 -358. 15. Van der Aa, N. G. F. M., Kommer, G. J., Van Montfoort, J. E., & Versteegh, J. F. M. (2011). Demographic projections of futu re pharmaceutical consumpt ion in the Netherland s. Water Science and Technology, 63(4), 825 -831. 16. Vieno, N., Tuhkanen, T., & Kron berg, L. (2007). Elimin ation of pharmaceuticals in sewag e treatment plants in Finland. Water research, 41(5), 1001-1012 . 87 Chapter 6 Energy Management Strategies and Techniques in Hybrid and Electri c V eh icles Bayram KILIÇ 1 Emre ARABACI 2 INTRODUCTION Energy policies of developing countries aim at economic growth, energy security and climate acti on together. Energy, which is the most fundamental in put of production, is a necessary condition f or societies to surviv e. Th e use of energy occurs in the direct manufacture of a product or in supporting the production process. While these processes occur, some problems arise, such as the decrease in natural resources, environmental pollution, climate chang e and high energy costs. However, considering the cur rent state of existing energy resources, it is a fact that the increasing ene rgy demand in the world cannot be met forever. In addition to the decrease in conv entional energy resources, the problem of glob al warming, which is one of the most impo rtant environmental problems, necessitates the efficient and effective use of renewable energy sou rces and currently prod uced energy. To increase energy efficiency, currently implemented regulations include measures such as burning fuels efficiently in combustion processes, perfor ming thermal insulation in facilities a nd systems, using applications that will in crease heat transfer efficiency, using heat recovery systems, and automatic control applications. In addition to these applications, especially in newly installed systems, it is required t hat the machines have high technologies, have thermal insulation, create energy efficiency mon ito ring systems, keep emission values to a minimum and pay attention to combined heat and power production. The decrease in available energy resources day by day has increased the tendency towards altern ative energy sou rces in energy production and use. Today, energy saving is seen as an alternative energy source. Energy savings in production an d use are extremely important for environmental problems as well 1 Assoc.Prof. ; Burd ur Mehmet Akif Ersoy Univ ersity, Technical Sciences Vo cational School, Department of Electricity and Energy , Burdur, Turkey, bay [email protected] ORCID No: 0000 - 0002 -8577-1845 2 Assoc. Prof. ; Pamuk kale University, Faculty of Technolog y, Automotive Engineering Department, Denizli, Turkey, [email protected] .tr ORCID No: 0000 -0002 -6219-7246 88 Figure 4. Illustrate the road network CONCLUSI ON Energy management in electric vehicles plays a critical role in terms of sustainability and vehicle efficiency. Technological advances and the development of energy management strategies will s hape the future of electric vehicles. Energy management not only increases the perfo rmance and efficiency of vehicles, but also contributes to an environmentally friend ly transportation future. 95 REFERENCES 1. Altındemir, E. (2008). Hibrid elektrikli taşıtlarda r ejeneratif frenl eme. Yüksek lisans tezi, İstanbul Tekn ik Üniversitesi Fen Biliml e ri Enstitü sü. 2. Denton, T. (2020). Electric and hybrid vehicles . Rout ledge. 3. Erjavec, J. (2012). Hybrid, electric, an d fuel-cell vehicles . Cengage Learning. 4. Halderman J., and Martin, T. (2011). Hybrid and Alternative fuel vehicles . Pearson Prentice Hall. 5. Husain, I. (2011). Electric and hybrid vehicles: design fundamentals . CRC press. Scientific Studi es on the Edge of Global Warm ing 6. Khajepour, A., Fallah, M. S., and Goodarzi, A. (2014). Electric and Hybrid Vehicles: Technolog ies, Modeling and Control -A Mechatronic Approach . John Wiley & Sons. 7. Kural, E. (2015). Hibrid Elektrikli Araçlar İç in Enerji Yönetim Sistemleri. Dok tora Tezi , İsta nbul Teknik Üniversitesi Fen Bilimleri Enstitüsü. 8. Mariem , S., Lilia, R., Mohamed, A . D., Yasmine, A ., Lasaad, B. , Lamjed, B . S. (2022). Optimal Electric Vehicle s Route Planning with Traffic Flow Prediction and Real -TimeTraffic Incidents, Journal o f Electrical and Computer En gineering Research , 2 (1), 1- 12. 9. Mi, C., and Masrur, M.A. (2 017). Hybrid electric ve hicles: principles and applications with practical perspect ives . Jo hn Wiley & Sons. 10. Yuzheng, Z., Xueyuan, Li ., Qi, Liu ., Songhao , Li ., and Yao, Xu . (2022). Review article: A comprehensive review of energy management strategies for hybrid electric vehicles, Mechanical Sciences, 13, 147 - 188 . 96 Chapter 7 ENV IRONMENTAL BIOTECHNOLOGY PROCESSES IN THE TREATMENT OF LIVESTOCK WASTES Büşra YAYLI 1 İlker KILIÇ 2 1. Introduction Organic wastes generated from various activities are thrown in to the environment, stored, incinerated, or used inefficiently with out an effective transformation process. As a result, waste cannot be thorough ly degraded and threatens the environment, ecosystem, and hu man health, although it has an essential place in national economies. Unco ntrolled storage and decomposition of waste lead to th e formation of gases such as CH 4 and CO 2 , which are harmful to human health; odor, flies, and pathogen s are formed, and the hygi ene conditions of the environment deteriorate. Nitrate accumulation resultin g from decomposition can cause deterio ration of soil struct ure and micr obiology and pose a threat to humans and other li ving things through vegetable and fruit consumption and drinking water as a re sult of nitrate mixing with surface and groundwater [1, 2 ]. Due to the increase in the world population, the livestock sector has grown and caused the accumulation and formation of animal waste that caus es environmental pollution in developed and developing countries. These wastes are very harmful to the e nvironment and difficult to dispose of. In recent years, environmental waste caused by livestock and animal waste has become on e of the most critical env ironmental problems. Manure, wet organic, and animal wastes are non-resident pollution sources from the lives tock in dustry. It reaches surface waters or groundwater, deteriorating the water quality and making it unusable [3]. Livestock industry waste can also be used in fertilizer and feed production areas. Thus, the evaluation of wastes in th e livestock industry both reduces environmental pollution and ensures econo mic recov ery of these wastes. However, applying waste directly to agricultural fields or streams without any 1 Research A ssi stant.; Bursa Uluda g University Faculty of Agriculture Depa rtment of Biosystems Engineering . bu [email protected] ORC ID No: 0000 -0002-0198-35 50 2 Prof. Dr.; Bursa Ulu dag University Faculty of Agriculture Departmen t of Biosystems Engineering . [email protected] .tr ORCID No: 0000 - 0003 -0087-6718 97 fermentation process negatively affects the product productivity of the soil as well as environmental pollution [3]. Nitrate accumulation resulting from decomposition can cause deterioration of soil structure and microbiology and threaten humans and other liv ing things through veg etable and fruit consumption and drinking water due to nitrate mixing with surface and gr oundwater. Biotechn ological methods find an essential area of use in the evaluation a nd elimination of wastes at the point of environmental protection . Biotechnology has recently enabled modern tools and approaches in various fields such as agriculture, food, healthcare, and environmental protection. Suppose there is not a very serious po llution burden in treating hazardous wastes and controlling pollution. In that case, applying environmental biotechnology techniques using living organisms can offer solutio ns. This paper examines en vironmental biot echnological application s that can be applied in evaluating, removing, and treating farm animal manure. 2. Uses Area s of Environmental Biotechnol ogy in Livestock Wastes Treatment 2.1. Treatment of wastes Excessive nutrient accumulation occurs in soils where unreasonable or excessive fertilizer is applied. Thi s situation causes heavy metal pollution in the ground, creating a toxic effect on living things in the ecosystem. At the same time, it disru pts th e soil's flora and affects the soil's biological and biochemical reactions. Thanks to bioremediation methods, highly toxic pollutants are transformed into less harmful forms thanks to the metabolic activities of microbes (such as transformation, mineralizatio n, and immobilization) [4]. Bioremediation is a process that includes the capacity to clean th e environmen t by removing pollutants in water and soil through degradation, detoxification , and retention by macro and microorganisms such as plants, bacteria, earthworms, and fung i [5]. Bioremediation is a more per manent method because pollutants do not transform fro m one phase to another but are changed into harmless end products such as carbo n dioxide and water through biological activities. In bior emediation methods, two app roaches, in -situ and ex-situ , are based on transporting or removing wastes to a different lo cation for pollu tant removal. In in -situ application, the contaminated materi al is cleaned on -site. Bioventing, biostimulation, biodegradation, biosparging, and bio -augmentation are in-situ methods. In the ex -situ process, pollu tant removal is carried ou t by physically 98 removing the contaminated material from its location. Land farming, composting, bioreactors, and soil biopiles are exa mples of ex -situ bioremediation methods. The ex -situ bioremediation method, the remediation technologies that canno t be appl ied in the soil environment, gives faster and more effective results than the in -situ method [6]. The bior emediation method is called phytoremediation if plants are used to remove pollutants in soil and water. If plants are used to remove heavy metals from the soil with the phytoremediation method , the plants must be removed from the soil. Plants and macro and micro creatures are used in biorem ediation applications. In the studies conducted, it is thought to be a valu able alternative for the treatment of he avy metal pollution in the soil, with its features such as accumulating heavy metals in the tissue s of earthworms, contrib uting to the development of plants by increasing plant nutrition al elements in the soil , providing aeration of the soil and supporting microbial activity [7 ]. However, there needs to be more information on how and by which methods the heavy metals in earthworms can be removed fro m the soil since heavy metals in their bodies can be mixed back into th e soil after they die. There is a need for fu rther research on this subject. Microorganisms are also used i n the biore mediation method. Microorganisms are trans ferred to the soil, and conditions are controlled to optimize their metabolic activity and gr owth. Environmental fa ctors such as temperature, pH, and inorganic nutrien ts such as ni trogen and phosphorus are modified for op timization. With another method, by looking at the microorganismic structure of the soil, microorganisms transf er nutrients to the area wh ere w aste is in the soil. Thus, microorganisms existing in the soil ar e activated. Creatures such as fungi and bacteria are also microorganisms used in bioremediation. Thank s to mycelial str ucture and fung al enzymatic systems, fungi are more suitable for the bioremediation method. Thanks to their biochemical capacities and morphologies, fung i play an essential role as decomposers, including o rganisms in soil and water [8]. In cases of excessive pollutant loads, natural microorganisms may be unable to clean pollutants. In such cases, stud ies are bein g conducted on genetically modified microorganisms (GEMs). 2.2 . Biyoenergy Products From Li vestock Wastes 2.2.1. Biomass The world's most important energ y source is oil, but as oil reserves gradually decrease, alternative energy sources have become even more critical. Biomass 99 is all organic materials of plant and animal origin that are not fossils. Biomass energy is ob tained from all natural materials of animal and plant origin, th e main compo nents of which are carbohydrate compounds. Biomass production from animal waste can be converted into liquid and gaseous fu els due to biotransformation pr ocesses, and it can also be used fo r heating and electricity generation. An economic study of the energy that can be obtained should be conducted when ag ricultural biomass resources are characterized to determine their chemical and ph ysical pr operties. If the feasibility and operation of the process a re economical, biofuel can be produced by app lying thermochemical methods to agricultu ral biomass. If the techno -economic evaluation is not applicable due to the examinatio n, it can be use d in applications such as compost, animal feed, soil impr over, and natural fertili zer [9 ]. In addition, minimizing gas emissions from animal waste, pathogens, microorganisms associated with waste, and odor suppo rts its conversion in to useful energy sources and helps reduce environmental impacts. It will be achieved by increasing the energy prod uction from biomass by applying advanced technologies to convert electricity, liquid, gas, or unprocessed solid fuels from raw biomass into suitable en ergy carriers [10]. As the nu mber and weight of animals increase, th e amou nt of waste generated also increases, which is related to the biomass energy po tential. Since biomass resources of a nimal origin are generally rich in CH 4 and CO 2 , biogas production involving anaerobic digestion is prioritized. The pr oducts resulting from biogas prod uction are also converted and used for electricity and heat generation, as valuable fertilizer, and even as bio fuel. Physical, biochemical, and thermochemical processes c an be used in biomass conversion processes. Physical methods such as grinding, dr ying, pelletizing, and accumulation can be applied in bioconversion [11]. Applying physical tech niques before thermochemical or biochemical proce sses increase s the applicability of biomass. Thermochemical conversion processes to convert biomass into products are gasification, pyrolysis, and combustion. The most commonl y used chemical processes in biomass conversio n ar e combustio n, gasification, pyrolysis, fermentation, and transeste rification [12]. The combustion process is applied to convert the chemical e nergy in biomass into mechanical, electrical, or heat energy. Materials with more than 50% moisture content are not preferred because they must be dried before combustion. Especially since the moisture content of animal man ure is usu ally more than 50%, the comb ustion process is not app lied. It is also undesirabl e because it creates problems in terms of lo w energy efficiency and air p ollution. 100 The gasification process is applied to obtain gas from carbon -containing materials to produce fuel. It is carried out by heating the biomass in the an aerobic en vironment at 700 -1000 ºC. With the gasification techniq ue from biomass, a gaseous fuel can be obtained with a high efficiency to be used in oil - fired turbines that provide power and heat. Using gas fuel obtained by gasification of biomass can be expanded by making sm all arrangements in places where natural gas is used [13 ]. Pyrolysis of biomass is a thermochemical process carried out in the absence of oxygen and at hi gh tem peratures to break down organic molecules to ob tain gas. The clas sical working rang e of pyrolysis is between 300 - 600ºC. It can be realized in 3 ways according to the change of these temperatures and heating rates: slow, fast, and flash . Th e most well -known pyrolysis process is biochar production, which is realized by slow pyro lysis. The main ob jective of fast pyrolysis is to obtain a high amount of liquid fr om biomass. Flash pyro lysis occurs at very high temperatures within milliseconds compared to other pyrolysis types. Bioethanol and biogas are prod uced as a result of the fermentation of biomass in an oxygen -free environment. Since the transesterificatio n process produces biodiesel from biomass, this p rocess is examined under b iofuel. 2.2.2. Bioga s Biogas, a clean energy source, is obtained du e to the anaerobic tr eatment of some speciall y grown plants, agricu ltural, and or ganic wastes, espe cially animal manure, with suitable bacteria [2]. I n parallel with the interest in energy recovery fro m waste, interest in anaerobic biotechnolo gy has also increased. Biogas production is the breakdown of organic substances containing biodegradable substances under anaerobic condi tions by successive multistag e reactions [14] . Biogas applications, which have sign ificant advantages, especially in regions with intensive agricultu ral production, attract considerable interest in agriculture waste management worldwide due to their env ironmental and econo mic benefits. After biog as prod uction in biogas plants, the remaining organic wastes can be used in agriculture as high -quality fertilizer by composting [15]. Biogas production is based on the formation of methane gas (CH 4 ) and carbon dioxide (CO 2 ) as th e end product as a result of the breakdown of organic matter [16]. One m 3 of bi ogas provides a heat value in the range of 4700 -5700 kcal and has the equiv alent of 0.62 liters of kerosene , 1.46 kg of charcoal, 3. 47 kg of wood, 0.43 kg of butane gas, 12 .3 kg of dung and 4.70 kWh of electrical energy [17]. 101 Biogas production factors include temperature, pH, or ganic matter loading rate, MRS (m icroorganism retention time), C/N, toxicity, and hydra ulic feeding time [18] . Depend ing on the operating temperatur e in biogas plants, the hydraulic waiting time varies between 20 and 120 day s. Th e C/N ratio in wastes producing bi ogas from animal manure varies between 15/1 and 30/1. If the C/N ratio provid es 15 /1 to 30/1, there is no need to adjust the livestock manure separately. C/N calculations are alw ays based on dry matter. The optimum C/N ratio can be achieved by mixing different organic substances. Min eral ions, heavy metals, and deterg ents have a toxic effect by inhibiting the growth of microorganisms in anaero bic treatment. While small amount s of mineral ions (sodium, potassium, calcium, magnesium, a mmonium, and sulfur) improve the growth of bacteria, heavy metals create a toxic effect [18] . Biogas production occurs in 3 stages: Fermentation and hydrolysis, acetic acid formation, and methane formation (Figure 1). During the fermentation and hydrolysis phase, th e fir st phase of bi ogas production, bacterial g roups called fermentation and hydroly sis bacteria break down carbohydr ates, proteins, an d fats, the three essential elements of or ganic matter. Organic substances transform into CO 2 , acetic acid, and soluble volatile organic substances. Since most volatile organic substances in the last group are volatile fatty acids, this stage is called the formation phase of vo latile fatty acids. In the acetic acid formation stage, ace togenic (acid -forming) bacterial groups, which are released as a result of the first stage and convert volatile fatty acids into acetic acid, are activated, and some aceto genic bacteria convert volatile fatty acids into acetic acid and hydrogen. Another group of acetogenic bacteria uses the released carbon diox ide and hydrogen to form acetic acid. However, the acetic acid formed this way is less than the first pathway. In the m ethane formation stage, methane-forming bacteria use CO 2 and H 2 to pr oduce methane (CH 4 ) and water (H 2 O). In contrast, another gr oup of methane-formi ng bacteria uses the aceti c acid released from the second stage to produce CH 4 and CO 2 . Of all the methane pr oduced, 30 percent is made in th e first pathway and 70 percent in the second. 102 I. phase II. Phase III. phase Fermentative Bacteria Acetogen ic Bacteria Methanogenic Bacteria Figure 1. Biogas produ ction stages [3] Qi et al. [19], examined a biogas sys tem in Northern Chi na where pig manure and veg etable waste wer e used together and found that th ere was a decrease in the emissions of air pollutants such as H 2 S, SO 2 , NO 2 , NH 3 , CO, and C 2 H 4 released into the atmosphere with the use of the system, and also that manure and vegetable waste were released into the atmosphere. It has been determined that harmoniou s service provides a 32 .4% increase in efficiency. White et al. [20], conducted a study on a small -scale biogas system in cattle farms in Ontario. Th ey foun d th at the syste m cou ld produce 120 MW of electricity and that changes in the feeds tock used in biog as production affected the biogas yield between 10 -80%. In the study condu cted by Kurt [15], the animal ferti lizer production results of Düzce province were examined, and the annual animal manur e production amount was 369,421.18 8 tons, the biomass calorifi c value was 10,266 .95 TEP (ton equivalent oi l), the biogas amou nt was 10,323,786 m 3 , and the bi omass an d bioenergy potential. It has been determined that research and develop ment studies on energy production from biomass shoul d be disseminated, and technological desig ns should be made. 2.2.3. Composting The composting process is the biological decomposition of organic ma terials under aerobic or anaerobic conditions into CO 2 and H 2 O togeth er with a humus - Bacterial mass H 2 , CO 2 , acetic acid Organic waste, carbohydrates, fat, protein Propionic acid, butyric acid, various alcohols and other compounds Bacterial mass Bacterial mass H 2 , CO 2 , acetic acid CH 4 , CO 2 103 like substance that is harmless to health [21, 22]. The compost material should have high biod egradability and or ganic matter content, con tain ideal concentrations of trace nutrients that plants can benefit fro m, and be free from harmful substances. The moisture content of the compost produced should be 65 %, nitrogen content should be 1.8 -2%, and pH value sho uld be around 7. Since the organ ic matter i n the compo st increases t he soil's max imum water - holding capacity, it prevents soil erosion by ensuring that the earth abso rbs water in high amounts of rainfal l [22]. The composting process aims to con vert biodegradable organic m aterials in to stable end products and reduce waste volume, eliminating undesirable organisms such as pathog ens and fly eggs that may be present in soli d waste, eliminating existing or po tential odor problems, maintaining maximum macronutrient (N, P, K) and micronutrient (Zn ) content, obtain products that have fertilizer val ue and can be used as soil con ditioners [23]. Different methods are applied in composting, windrow composting, passively aer ated piles, aerated static piles, and compostin g in reactors. Composting is faster than mixing the heap because the composting process is faster when plenty of air reaches the microorganisms. During composting in reactors, it shoul d be ensured that th e raw material con tinues to be in contact with oxygen. The most essential di fference betwe en open field and bioreactor composting is th e use of enzymes in bioreactors. The most import ant advantage of this method, known as enzymatic co mposting, is that it saves time. Aerobic composting is an odorless process and is widely preferred in compost productio n. It ha s advantages such as short fermentation time and elimination of pathogenic microorganisms and disadvantages such as the need for continuous oxygen supply and moisture control. There must be enough oxygen to provide aerobic conditions for decomposition without creating an odor problem. Anaerobic compo sting is a process that takes a long time to complete and may requ ire extern al heat in some cases. Bad o do r fo rmation is observed. Biogas can be obtained as a by-prod uct during anaerobic conversion [24]. Common factors affecting composting in all forms are grain structure, C/N ratio, pH, temperature, aeration, and water content [25]. Moistu re is essential fo r the growth and reproduction of microorganisms in the compost. The moisture content is approximately 40 -45% in the lower rang e. The upper range is determined by keeping the pores open so oxyg en can reach the microorganisms. Th e optimal pH of the bacteria used in composting is 6 -8. When the environment starts to warm up during the process, the pH dr ops t o 4 - 104 biomass. In Adv ances in eco-fuels for a sustainable env ironment (pp. 187 -210). Woodhead Publishing. 27. Pereira, C. O., Portilho, M. F., Henriques, C. A., & Zotin, F. M. (2014). 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Transactions of the ASAE , 47(5), 1625 -1633. 33. Zhang, H., & Wang, J. (2008). Identification of stored -grain age using electronic nose by ANN. America n Society of Agricultural a nd Biological Engineers , 24(2), 2 27- 231. 34. K ızıl, Ü., Genç, L., Genç, T. T., Rahman, S., & Khaitsa, M. L. (2015). E - nose identification of Salmonella enterica in po ultry manure . British Poultry science , 56(2), 149 - 156. 35. Gupta N., Renugopalakrishnan V., Liepmann D., Paulmurugan R., & Malhotra, B.D. (2019) . Cell-based biosensors: recen t trend s, challenges and future perspectives. Bi osensors and Bioelectronic s , 141 (1), 111435. 36. Kırkıncı, S . F., Maraklı, S., Aksoy, H . M. , Özçimen, D., & Kaya, Y., (2021). Antarctica: A r eview of Life Sciences and Biotechnol ogy Researches . International Journal of Life Scien ces an d Bio technology , 4(1) , 158-177. 111 Chapter 8 ENVIRONMENTAL IMPACT ASSESSMENT OF LAYING HEN PRODUCTION SYSTEMS THROUGH LIFE CYCLE ASSESSMENT Büşra YAYLI 1 İlker KILIÇ 2 1. Introduction Egg production is easy and economical, the protein con tent is high, and the fat content is low despite b eing an animal protein. The vast consumption are a can be consu med quickly and is offered to the consumer at a mo re affordable price than other animal-derived prot eins in retail sales. For these reasons, the increasing demand for eggs has played an active role in developing th e egg poultry sector. Developments such as the widespr ead use of i nd ustrial egg poultry and auto mation in the poultry house have also sign ificantly accelerated the realized production potential. China is the largest producer of chick en eggs in the world, pr oviding 36 . 4% alone in 2021. In the same year, 6.8% was supplied by America, 7.5% by India and 7% by Indonesia. Turkey supplies approx.1 .2% of the world's egg production with 1 243 633 tons of eggs, ranking it 10 th . In the world of egg export, after the Netherlan ds (3 51 224 tons), Tu rkey ranks second with 221 215 tons [1] . In the first ten month s of 2023, 16 million 975 thousand eggs were produced. In the January -Octob er peri od, chick en egg production increased b y 4.0% compared to the same period of the previous year [2]. According to 2021 data, 121 302 869 laying hens and 4975 commercial laying hen houses in Turkey. In the same perio d, 19 billion 788 millio n eggs were produced in the commercial e gg sector, and 23 9 eggs were prod uced per person [3]. Turk ey is a significant producer and exporter with its egg po tential. Today , the technical and technological developments in the egg indu stry have prog ressed at the same level as in Eu ropean countries. As th e egg is one of the essential export 1 Research Assistant.; Bu rsa Uludag University Faculty of Agriculture Department of Biosystems Engineering . bu [email protected] ORC ID No: 0000 -0002-0198-3550 2 Prof. Dr.; Bursa Ulu dag University Faculty of Agriculture Departmen t of Biosystems Engineering . [email protected] .tr ORCID No: 0000- 0003 -0087 -6718 112 products and its consumption in creases, the productio n potential mostly made by intensive enterprises also increases the amount of waste to be generated. Along with the increase in egg production, waste and emissions such as manure, urine, and gas outputs app ear in addition to the product obtained. In cases where these cannot be contro lled w ithin the enterprise, they affect th e employees' efficiency, animal welfare, and health . At the same time, if th ey reach the env ironment, they cause various environmental problems. To develop prevention and control strategies against ecological effects, it is essential first to determine which effects th ey cause and their effect si zes. Lif e cycl e assessm ent, a holistic system to assess the environmental perfo rmance of pr oducts or services, is a reliable analysis used fo r multip le purposes. Life cyc le assess ment evaluates ecological impacts by qualitatively and quantitatively defining t he use of raw mater ials, energy requirements, emissions, and wastes released to the environment throughout the life cycle of a produ ct, process, or activity [4]. 2. Environmental Effects of Laying Hens Productions Consumption of resou rces and raw materials such as feed production, water, and land use throughout the egg production process (cradle - to -grave); The coal, fuel, and electricity consumptions used in the operating proc ess; and the manure and urine from chickens a re the main factors causing environmental problems. The overall environmental impacts caused by pollutants from laying poultry can be described as follows: Climate change: It causes climate change with the emiss ions of greenhouse gases that cause gl obal warming (especially CO 2 , CH 4 , and N2O, which are the most critical greenhouse gases) to the atmosphere. I t is expressed in kg CO 2 , which is the equiv alent of CH 4 and N 2 O gases, according to the emission factor s de termined by the IPP C. For a 100 -year timeline, methane (CH 4 ) has an estimated global warming potenti al of 27 - 30 times CO 2 , and nitrous ox ide (N 2 O) has 273 times that of CO 2 [5 ]. The concept of carbo n footprint is also an effective method to determine the impact of a product or service on climate change and uses these equivalences in c alculations. Energy u se : In egg farming, energ y use in cludes a si gnificant share before production, during the productio n period, and in the stages after production. Diesel fue l use, coal us e, and electricity consumption of machinery, tools, and equipment used during production in the po ultry house are evalu ated in energy use. Energy uses are usually exp ressed in MJ. Water use: In th e rearing of layer hen s, the amount of water u sed to gr ow the product is the stage of feed production that causes the most water consumption. In addition, th e water consumed by chickens in the poultry house and the water 113 used for clean ing are evalu ated within the water use. Th e water con sumed is calculated as m 3 , ton, or liter. The concept of water footprint has emerged to determine the water consumption and the extent of pollution in the water in the formation of production or pro duct. Acidification and eutrophication: The most crucial gas emission in poultry farming originates fro m ammonia (N H 3 ). NH 3 gas emission causes acidification and eutrophication [6, 7]. Acidifi cation is the emission of gases that harm the environment by reacting with other compoun ds such as sulfur dioxide (SO 2 ), nitrogen ox ides (NO x ), and ammonia (NH 3 ) arising from various sources in the air and return ing to th e surfaces as acid rain [8 , 9, 10] . In acidification, the reference gas is expressed in term s of SO 2 The primary sou rces of eutrophication are emissions of NO 3 - (nitrate) and PO 4 -3 (phosphate) in water and NH 3 (ammonia) in air. Eutrophication can measures be measured by reference gases NO 3 - or PO 4 -3 equivalents. Nitrification and denitr ification: N gas in nitrogenous compounds in the air is first converted to NH 4 by bacteri a and released into the soil. Bacteria in the soil first convert NH 4 (ammonium) to NO 2 (nitrite) and then to NO 3 (nitrate), and this is called nitrification. NO 3 leaks from the soil, leaching with surface waters and underground drinking water, causing NO 3 accumulation. The process of reducing NO 3 to N gas by microorg anisms is called denitrification . NO 3 , gaseous by denitrification, causes environ mental effects such as the greenhouse effect, global warming, acid rain, and ozone degradatio n. Land u se: In general, as in all aqu aculture, while most land use is realized in feed production in laying hen farming, the op eration structure establish ed on a specific land also cause s land use. The m 2 equivalence is used as the reference unit. 3. Life Cycle Assessment ( LCA) The rapid increase in consumption and the increasing population over time, the decrease in resources, the concern of bein g unable to me et future needs, and the potential environmental effects it creates hav e re vealed the concept of life cycle analysis in which ecological sustainability is evaluated. Life cycle analysis is an all-pu rpose analysis that enables the calculation, evaluation, and reporting of the effects, risks, and their in teractions throughout the entir e life cycle of an activity or product. In various studies, the definition of life cycle analysis has been made: Guinee [11] , stated that lif e cycle assessment is a gen erally accepte d method for evaluating the environmental impacts of a product throughout its life cycle. 114 According to Baumann and Arvidsson [12], life cycle assessment is a systematic methodology that deals with th e material and energy flo ws used in processes su ch as raw material inpu t, pr oduction, use, and waste gen eration related to a product or process and their env ironmental impacts. According to Gulli [ 13] , Life cycle asses sment is a quantitative analysis that can be used with other models to identify and evaluate potential environmental impacts duri ng the life cycle of a process or pr oduct, to improve production methods, and to predict the behavior of various production cycles, including agricultural production. According to th e In ternational Organization for Standardization (ISO), life cycle assessment is the collection of inputs and outputs throughout the life cycle of a product system and th e assessment of its potential environmental impacts. The life cycle assessment methodology has been standardized with ISO 14040:2006 and ISO 1404 4:2006, a series of environmental managemen t standards created by th e International Organizatio n for Standardization [14]. The phases within which a product, service, or process's life cycle analysis will be presented with four different approaches: 'cradle to grave,' 'cradle to gate,' 'cradle to cradle,' and 'gate to gate.' According to ISO standard s, life cycle an alysis consists of four stages. These; - Definition of aim and scope - Inventory analysis - Impact assessment - Interpretation 3.1. Definition of Aim and Scope The first stage of life cycle analysis is definin g the aim and scope. The aim and scope of th e product, service, or process to be analy zed should be clearly stated. While LCA analysis can be applied for short -term studies, it can also be used for long -term studies. The target public to which the research results will be pr esented may vary . Factors such as working time, target audience, and databases suitable for the study influence choosing the LCA type. The available database is selected for the data and s tandards used in the study. The database chosen may chang e depending on the geographical region where the study is conducted, the content, and th e purpose of the study. The defined functional unit is taken as a basis in the life cycle assessmen t while limiting the scop e. A refer ence is an op erating unit that reveals th e environmental effects of a productio n system or a service. Wiedemann and McGahan [15] stated th at the definition of an available unit is "a reference unit 115 that enables the comparison of in puts and outputs in productio n and different system op erations in a similar structu re." The functional unit is determined by considering the enviro nmental impact categories and the aim of the research. [16, 17]. The production or process must be limited while estimating in the life cycle assessment. I n determini ng th e system bound aries, which stages and processes of the life cycle of the pr oduct or service will be included, which will be excluded, and their justification s are taken into account [18]. 3.2. Life Cycle Inventory In the inventory analysis phase, which is the third par t of the life cycle analysis, the limits and product system of the work who se purpose and scop e are determine d are defined. Th e life cycle Inventory step includes data on raw material inputs, resource use, energy requirements, liquid and solid waste, atmospheric emissions, and leakage to aquatic environments. A dditionally, it aims to collect qualitative and quantitative data, to express the product outputs as a r esult of production numerically, to obtai n and evaluate all the data-related data, and to determine the calculation procedures. Th e inventory phase of the life cycle is th e primary phase for analyzing the method . The data's details, accuracy, and consistency directly affect the accu racy of th e results in determining the impact cat egories and th e resu lts for the future stages. In th e ISO-14044:2006 stand ard, the formation steps of inven tory analy sis are specified as ob taining th e data, calculatin g the data, and distributing the data (allocation) (Figur e 1). 3.2.1. Obtaining Data Data collection is th e most challeng ing and long -time phase of life cycle analysis. Qualitative or quantitative data collected, measured, calculated, or estimated for each pr ocess of inpu ts and ou tputs at the w orking system boundaries are obtained. Lo cal or glob al sources are used if da ta cannot be accepted or reached. The main headings in which the data can be classified can be listed as follows: - energy inputs, raw material inputs, auxiliary in puts, and other ph ysical inputs - products, by-prod ucts and wastes - air, water, and so il emissions - other environmental degradation s 116 Figure 2. Flow chart of li fe cycle inventory assessment 3.2.2. Calculation of Da ta At this stage of th e inventory analysis, the calculation methods should be clearly stated, and the same c alculation procedures should be applied consistently throughout the study. Data needs to b e valid ated t o ensu re data quality in computation. Validation of data is relate d to being consistent with each other and making comparative analysis. Cal culatio ns of inputs and ou tputs should be made by creating flow charts in unit processes, considering the study's un it function . Based on its purpose, syste m bo unda ries can be revised according to the sensitivity analysis of essentia l inpu ts and ou tputs in processing data obtained in life cy cle analysis. 3. 2.3. Allocation This stage includ es data distribution to the relevant processes. Di stribution should be avoided if the unit process is split into two or more sub -stages, by- products are prod uced, and th e production process is expanding. Supp ose data allocation cannot be avoided in the production process. In that case, it must be distributed in a way that reflects the fund amental physical relationship between different products or functions. If the physic al con nection between the development or processes canno t be established in the distribution, it is done by Aim and scope Preparatio n to obtain data Data collection Confirma tion of data Associating the unit process with data Associating the functional unit with d at a Data assessmen t Completio n of inventory Refining the system boundary Allocation includes reuse and recycling Additional data or unit processes required Revision of collected data 117 decoupling it with other relationship s. For example, the econo mic value of the products is allocated among th e by -products in proportion. 3.3. Life Cycle Impact A ssessment As stated in ISO [ 14] , since life cycle assessment is a relative app roach based on unit function, it differs from other techniques such as env ironmental performance assessment, environmental impact assessment, and risk assessment in th is respect. At this stage of the life cy cle analysi s, t he po tential effects of the inventory data collected for system inputs (raw material, energ y, water, and resource uses) and system outputs (product, was te, by -products) on humans and ecology are ev aluated. Th ere are som e compulsory and optional elements to carry out an impact assessment . Required factors includ e defining impact categories and category i ndicators, impact classification (classification), and characterization. 3.3.1. Identification o f impact categories and indi cators In the life cycle assessment, impact catego ries indicate environmental problems (climate chang e, acidification, eutrophication) related to the production system or process examined to reflect the purpose and scope of the work done (Table 1). Each impact category has a specific env ironmental mechanism, and impact indicators vary according to the types defined within these ecological mechanisms. Table 1. Environ mental Impact Categories and Units Impact Category Uni t Climate Change kg CO 2 eq Ozone Depletion kg CFC-11 eq Terrestrial Acidification kg SO 2 eq Freshwater Eutrophication kg P eq Marine Eutrophication kg N eq Human Toxicity kg 1,4-DB eq Photochemical Oxidation Formation kg NMVOC Particulate Matter Formation kg PM10 eq Terrestrial Ecotoxicity kg 1,4-DB eq Freshwater Ecotoxicity kg 1,4-DB eq Marine Ecotoxicity kg 1,4-DB eq Ionizing Radiation kBq U235 eq Agricultural Land Use m 2 a Urban Area Use m 2 a 118 3.3.2. Impact classification Classifications are grouped by associating the determined impact categories and indicators with the da ta collected durin g the life cycle inventor y analysis. For example, SO 2 (sulfur dioxide) gas emissions cause acidification. Therefore, SO 2 is classified in the acidification effect category. 3.3.3. Characterization Whichever data obtained in the inven tory analysis contributes to the same impact category, these data are multiplied by specific coefficients and converted into a standard unit, revealing the total impact of that impact category. The characterization stage enables compari son between inventories within the same impact categ ory. E.g., CO 2 , CH 4 , and N 2 O are the most impo rtant greenhouse gases that cause climate change. Calculatin g the effects of th ese gases on climate chang e in kg CO 2 equ ivalents ov er the standard unit characterizes th eir impact on climate change. After the compulsory stages in the life cycle impact assessment are carried out, optional steps can also be carried out within the scope of the study on the inventory data. These stag es are no rmalization, grouping, weighting, and data quality analysis [14] . 3.3.4. Normalization An in ventory analy sis tool eliminates the un its by dividing the impact indicators by a selected r eference value and comparing them between different impact categories [ 19] . For the reference to be determined, reference values such as the sum of inputs and outputs for a specif ic area globally, regionally , nationally, or locally, the sum of inputs and ou tputs per capita for on e particular area, and the information and ou tcomes of the alternativ e scenario presented to the product system can be selected. 3.3.5. Grouping Impact categories within the defined purpose and scope of the work are assigned to one or more predefined groups. The grouping stage pr ovides ease of interpretation and evaluation of impact categories fo r studies to be carried out in certain areas. For example, w hen examining the chemicals of a service that Natural Area Transformation m 2 Water Consumption m 3 Metal Consumption kg FE eq Fossil Consumption kg oil eq 119 cause env ironmental pollutio n in the aquatic env ironment, grouping them as water emissi ons pr ovides ease of mon itoring and evaluating th e impact category. 3.3.6. Weighting At this stage of the life cycle analy sis, different impact categories are graded according to their valu es using numerical values. Weighting the impact categories with the weigh ting process reveals which class has a more sign ificant impact. The same indicators or normalized indicator results can differ depending on the country, region, organization, or society where the weighting process is performed. 3.3.7. Data quality anal ysis Additional information and techniques may be needed to understand better and demonstrate the importance, un certainty , and sensitiv ity of inventory analysis results. Different analy ses are used to reveal the accuracy of the data to carry out the purpose and scope of life cycle analysis. Gravity Analysis is applied to identify the data that contributes the most to the r esult. Uncertaint y Analysis is applied to reveal un certainties in data and calculations. Sensitivity Analysis is used to decide how changes in data and methodological choices affect the inventory results. 3.4. Life Cycle Interpreta tion Interpretation is the final stage of life cycle analysis. The data, findings, and results obtained in the inventory analysis and impact assessment step are evaluated by the purpose and scope of the study and suggestions pr esented. Regarding the purpose of the study, interpre tations should be made using the definitions of system functions, functional un its, and system boundaries, usin g the data obtained and within the limitations determined by sensitivity analysis. There are some po ints to be considered in t he interpretation p hase of an LCA study [14]: • According to the fin dings obtained from the in ventory analysis and impact assessment phase, it is ne cessary to determine and e mphasize the critical issues that affect the study. • The evaluation should involve the subject and e nsure the results are sensitive and consistent. • In the interpretation phase, the final work should be concluded, and the precautions and limitations that can be taken for the current situation should be put forward. 120 close this gap, there will be an increase in industrial enterp rises that pr oduce more eggs per un it area. This change in cultivation system s also brings environmental effects. In order to achieve sustainable production, environmental impacts must be pr edicted, and necessary precautio ns must be taken. When the studies in the literature are examine d, it has been seen that the environmental effects of egg poultry production systems can be predicted successfully. Therefore, as a result of the stud y, it was conc luded that the life cycle assessment method is beneficial in determining th e environmental impacts of egg poultry production systems. 127 References 1. FAO, (2021). Fo od and Agriculture Organization of the Unit ed Nations, Crops and livestock products . Retrieved Octob er 13 , 2023, from https://www.fao.org/faostat/en/ 2. TUIK, (2023). Turkish Statistical Institute, Livestock Statistics . Retrieved October 13, 2023, from https://d ata.tuik.gov.tr/Bulten/Index?p=Kume s- Hayvanciligi-Uretimi-Eki m- 2023 -49416 3. YUM - BİR, (2021). Yumurta Üreticileri Merkez Birliği, Yumurta Tavukçuluğu Verileri . 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Life cycle assessment of Canadian egg products, with di fferentiation by hen housing system type. Jou rnal of Cl eaner Production , 152, 167-180. 37. Abín, R., Laca, A., Laca, A., & Díaz, M. (2018). Environmental assesment of intensive egg production: A Spanish case study. Journal of Cleaner Production, 179, 160-168. 38. Estrada-Gonzalez, I. E., Taboada - González, P. A., Guerrero -G arcia- Rojas, H., & Marquez- Benavides, L. (2 020). Decreasing the Environmental Impact in an Egg -Producing Farm thro ugh the Application of LCA and Lean Too ls. Applied Scien ces , 10(4), 1352. 131 Chapter 9 Material strength tests with electrical approach Emrah Kaplan 1 Dursun Ekmekci 2 Abstract – This review article di scusses the important con nections between mechanical analysis meth ods and electrical measurement me thods in materials. In particular, it focuses on how condu ctivity, resistance and capacitance measurement method s can be used to determine the mechanical properties of materials. The role of these methods in evaluating material durability and elastic properties is considered. Additionally, electrical investigation of mechanical tests is exa mined as an important approach that allows ma terial testing processes to obtain more detailed and precise result s. This stud y also high lights the advantages and potential con tributions of using electrical met hods in bullet proofness analysis. This review aims to make a sig nificant contribution to the existing literature by emphasizing the importance of the electrical approach in material durability tests. It demonstrates the potential of how the electrical approach can be used to evaluate mechanical properties of materials quickly and precisely . Keywords – Electrical measurements, mechanical properties, ballistic resistance, material testing metho ds I. I NTRODUCTION Material str ength and durability are one of the main properties that determine the perfo rmance of a material. Accurate evaluatio n of the mechanical properties of materials is of critical importance in many industries such as industrial design, constru ction, automotive, aerospace and defence [1]. Properties of materials such as electrical conductivity, resistance and capacitance can provide important information about their mechanical durability. Electrical measurement methods are important tools widely used in materials science and engineerin g in the charact erization and perfo rmance 1 Department of Electrical an d Electronics Engineering, Gümü şhane University, Turkey 2 Department Departmen t of Mechanical Engineerin g, Gümüşhane University, Turkey * (dursunekmekci@gumushan e.edu.tr) Email of the correspo nding author 132 improvement of materials. Electrical measurement methods can also be used without applying impact or load to examine material strength and durability. This potential is important for predicting the long -term performance of materials and assessing their suitability fo r specific applications [2]. Additionally, it should be noted that electrical approaches enable fast, economical and repeatable measurements. This article specifically examines the relationship between electrical measurement methods and th e mechani cal du rability of materials. The role, advantages a nd limitations of electrical me thods in the process of evaluating the mechanical properties of materials will be discussed and their potential impact in industrial applications will be discussed. Th e abili ty of electrical approaches to provide greater insight in to material strength and durability highlights th e importance of research in this area. This review article aims to provid e a guide for researchers and industry professionals in the field of materials science and engineering on how mechanical testing as well as el ectrical measurement methods can be used in materials charact erization. II. M ECHANICAL A NALYSIS M ETHODS IN M ATERIALS They are common meth ods used to study different mechanical prop erties and behaviors of materials in both commercial and military fi elds. Which method to choose depends on the properties and material type you want to measure. Commonly used destru ctive and non -destru ctive analysis methods are given in Fig 1. Fig. 1 Commonly used material testing methods This review focuses on mechanical and electrical m ethods. In these tests, the stress (lo ad) value applied to the material is associated with deformation (shape 133 change). The data ob tained as a result of these tests is used to determine important mechanical properties of the material, suc h as elastic modulus, yield strength, and tensile streng th. It is used to measure stress, strain rate and elastic/plastic zone in th e plastic defor mation of the material [3 ]. The tensile te st shown in Fig. 2 is the most common test used to measure mechanical properties. It is a widely used test to examine the mechanical behavior of a material. This curve shows the elastic beh avior o f th e material, its plastic deformation and the moment o f final fracture. Fig. 2 Tensile stress-strain curv e. Reprinted from [4] Hardness tests are used to evalu ate the material's properties such as resistivity, durability and wear resistance. There are different methods such as Rockwell, Brinell and Vickers hardness tests. In these tests, the tensile fo rce applied to a material sample is used to determine the properties of the material such as br eaking strength, modulus of elasticity and tensile strength. Compression tests are used to determin e the compressive force applied to a material sample and its prop erties such as compressive strength, mod ulus of elasticity and tensile strength. Impact tests are used to measure the impact resistance of a material. In these tests, a standard impact is applied to the material and the energy absorption abili ty, crack resistance and fracture behavior of the material are evaluated. There are different methods such as Charpy and I zod impact tests. Fatigue tests are used to evaluate how a material behaves when subjected to repetitive loading. In these tests, repetitive stresses are applied to the materi al sample and the prop erties of the material, such as 134 fatigue strength and fracture behavio r, are determined. Th e thermal behavior of the material can affect its mechanic al properties. Therefore, th ermal analysis methods are used to study the thermal beh avior of the material. Add itionally, changes in the temperature of the material may occur during plastic deformation. The temperat ure profile of the materia l can be examined using thermal cameras or temperature sensors [5], [6]. When the materi al undergoes plastic deformation, changes in its magnetic properties may occur . Magnetic field measurements can be used to detect these chang es and monitor the intensity of plastic deformation. Acoustic emission tests capture sound waves emitted by micro -cracks or ot her signs of plastic deformation occurring in the material. These audio signals can be used to evaluate th e presence and intensity of plastic deformation on the material [7 ]. III. E LECTRICAL M EASUREMENT M ETHODS Electrical method s are an effective to ol used in material characterization and these method s are used to monitor electrical chang es due to mechanical effects on th e material [8]. In this way, it is possible to determine and analyze th e plastic deformation, crack formation and similar mechanical changes of the material. Add itionally, these methods offer the possibility of testing before and after impact, thus providing comprehensi ve information about the durability and changing pr operties of the materi al. These electrical tests allow analysis without applying a bullet or other impact, which is a great advantage fo r evaluating the material’s potential applications such as armor steels. However, specific mechanical tests that require direct measurem ent of mechanic al properties ar e also used a nd generally provide more accurate results. Th erefore, while electrical methods play an important role in material characterization , combining them with mechanical testing for a complete evaluation is of ten the preferred approach. A. Electrical Resistance Mea surement Resistivity is a physical property that measures the electrical resistance of a material. Resistance ( ρ ), on the other hand, is a characteristic feature of a material independent of geometry and size, and is an important parameter expressed acco rding to the electrical resistance ( R ) and volume ( V ) of th e material. Resistance is calculated by the formula given below and is a fundamental tool in both electrical and mechanical charact erization of the material. In this context, the prod uct of the paramete rs W ( width) and L (length) expresses the volume of an object. In addition to evalu ating the electrica l behavior of the material, this property also pl ays a critical role in understand ing 135 the structu ral and mechanical properties of the material. Using current ( I ) , voltage pr obe range and cross - sectional area of the sample, th e ρ value (resistance) of the sample is determined (Fig . 3). Material cross -section and resistance values are calculated with the help of Eq. (1) and Eq. (2). Fig. 3 Diagram and formula about resistiv ity: This diagram, which shows the definition of material resistivity , visualizes the resistivity fo rmula. A: Cross - sectional area, t: Material thickn ess 𝐴 = 𝑊 ∗ 𝑡 (1) 𝑅 = 𝜌 ∗ (𝐿 𝐴 ⁄ ) (2) Electrical re sistivity can provide information about the material's conductivity, density, and internal structural pr operties. In their research, Miyajima et al. reported the changes in the resistan ce of commercially pure aluminum and discussed the relationship between resistance and crystal defects [9]. Again, in di fferent studies and rese arches important results have been obtained to understand th e complex electrical behaviour of various materials which occur after physical effects ap plied on them such as, shape memory alloys [10], [11], metals [12], concrete parts [13], [14], carbon fiber reinforced plastics [15], [16], ceramic matrix composites [ 17], uniaxial ro ck [18], nanocomposites [19], conductive fabrics [20], wearable electronics [21] and even carbon nanotub e threads [22], [23]. Each of the four different basic methods described below offers a different approach to the process of measuring the electrical properties of materials and includes different measurement techniques. The aim of these methods is to precisely and reliably evaluate the elect rical properties of the material, such as resistance, conductiv ity and contact resistance. Different analysis approaches 136 corrosion. This ensures long -term stability of the electrical properties. Such materials are resistant to impact and mechanical stress and keep electrical connections stron g. This again ensures the stability of the electrical properties . Shockproof materials are not generally used for insulation purposes becaus e they are good conductors of electricity. However, electrical insulation can be achieved by combining it with some s pecial coatings or insulating materials. Fig. 8 shows the measured characteristi c p oints of the 12 -layer composite at 24 J on the impact fo rce-displacement curve and the high -speed camera images of the characteristic po ints. The electrical prop erties of such materials may vary depending on the design objectives and the specific prop erties of the material used. Particu larly in electronic or military application s, determining electrical properties is an important part of the material selection and design process. It is therefore important to consider the electrical requirements when choosin g the most suitable material for a particular appl ication. Fig. 8 Impact force-di splacement performance graph obtained as a result of impact tests performed on a 12 -layer composite and high -speed camera images of these measured points [5 7] C. Non-destructive Evalua tion of Mechanical Properties of Materials Electrical measurements are an important tool for damage detection, for example in fiber reinforced polymer (FRP) materials [7]. In carbon fiber reinforced polymers such as CFRP, carbon fibers provide electrical conductivity, so it is possible to monitor the state of the material under load. When a matrix filli ng material such as carbon black is used in m aterials such as GRP, vo ltage and damage monitoring can be performed using the direct current 143 method. Direct current electrical resistance, alternating current capacitance and loss characteristics change as a resul t of applied load or voltage. These measurements can be use d to evaluate the condition of composite parts even when the componen ts are in use, and these methods are considered a non - destructive evaluation technique. However, more fund amental studies are required to better understand the effect of alter nating curren t electrica l properties on the material [58 ]. D. Intensity Measurement of Mechanical Impact It may be possible to indi rectly measure the effect of mechanical action on a material by using electrical methods, especially th rough pi ezoelectric sensors . In fact, the data obtained here is in tended to measure the magni tude of the impact applied to that material rather th an the change in the mat erial caused by the impact. At this po int, piezoelectric materials produce an electrical charg e in response to mechanical stress or deformation. This feature makes them suitable for pu rposes of sensing and measuring mechanical effects or vi brations in a variety of application s. These sensors are made of piezoelectric materials (e.g. , quartz crystal s, piezoceramics) that prod uce an el ectrical charge wh en subjected to mechanical stress [ 59 ]. The amount of charge produced is proportional to the force or impact applied to the material. In some case s, mechanical effects can lead to pr essure changes. Electrical pressure sen sors can detect these pr essure chang es and con vert th em into electrical signals [60]. This information can be used to extract the force or intensity of mechanical action. These electrical metho ds indirectly measure the effects of mechanical effects by detecting changes in electrical properties or signals caus ed by th e impact. Data obtained from t hese s ensors can prov ide valuable information abo ut th e mechanical behavior o f materials, especially to external forces or vibratio ns. E. Armor Material Testing Process The results of bullet resistance tests determine the performance and durability of the tested material. The following analyzes are performed on the material after the bullet impact. If the bullet has penetrated the material, this is called "penetratio n" and the bullet proof level is considered as failed. If the bullet has no t penetrated the materi al, the speed at which the bullet remains in the material is determined. This data shows how much energy the material absorbs. It is also evaluated whether the bul let damages the material. Holes , cracks or deformations on th e material are observed and recorded. The results show how much protection the material provides against whi ch types of 144 projectiles and according to which standards [6 1]. Ev aluation results can be used in performance enhancing processes such as changing material structure or components. These results are critical for the develop ment of military equipment, ballistic vests or armor, and civilian security applications. In Fig. 9, the Euro pean EN 1522/1523 standard is taken into consideration fo r the target plate used in ballistic tests, th e distance betwe en the accelerometers and the gun, and the bullet speed. Before the tests, the bullet speed was adjusted by the amount of gunpowder in the cartridge cas e and it was tried to be kep t at 820 ± 10 m/s for the 7.62 Ball type bullet and 8 30 ± 10 m/s for the 7. 62 AP type b ullet [6 2 ]. Fig. 9 The mechanism where ballistic t ests applied to armor steels are performed In bullet proof tests, various mechanical measurement methods are used to evaluate the material's resistance to bullet or ballistic threats. Mechanical measurement methods commonly used in these test s. They form the basis of bullet proof tests. In these tests, impacts are simulated in which the material is struck at a c ertain speed and angle. The beh avior of the material under the influence of impact is observed an d recorded. V. CONCLUSION Electrical measurements can often be made quickly. Especially when automatic data collection systems are u sed, processes can be acc elerated and more data can be obtained. These devices are suitabl e for real -time monito ring, which can increase the abili ty to understand rapidly changing properties of the material. Particularly for simple devices, invest ment costs are low and maintenance requirements are usually limited. This can redu ce long -term costs. Bullet proof tests perfor med by electrical method s offer a versatile and effective way to measure the material's resistance to ballistic threats and impacts. These tests provide valuable information about the material' s mechanical strength and structure by precisely monitoring changes in th e material's electrical pr operties. 145 Additionally, these electrical tests can be perfo rmed without damaging the structure of the material, allowing tests to be perfo rmed while maintainin g the inviolability of the material. Therefore, electrical tests offer the opportunity to perform analysis without applyin g a bullet or other impact and can make a positive contribution to the evaluation of potential materials for armor construction. As a result, electrical methods gen erally have the adv antage of making rapid measurements and obtaining data at low cost, but it is always necessary to evaluate the c ost, especially for a specific application, and to verify measurements made by electrical measurement by common mechanica l measurements. 146 R EFERENCES 1. Dobrzański LA. Sig nificance of materials scien ce fo r th e future development of societies. 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Eng Sci Technol an In t J 2021;24:9 90 - 995. 151 Chapter 10 Effects of the Use of Nanofluids in Solar Collectors on Thermal- Hydraulic Performance Dr. Fatma OFLAZ 1 Abstract The use of nanofluids in solar collectors includes a technology that aims to increase the efficiency of collectors. Nanofluids consist of liquid particles at the nan ometer sca le, and the ir pr operties enable more efficient heat condu ction. Th e high thermal conductivity, low viscosity, and chemical stability prop erties of nanofluids allow for increased heat transfer in solar collectors, improving temperature control, and, as a result, increasing efficiency. These features, w hen ut ilized in the liquid cooling systems of solar collectors, effectively cool the pan el and optimize performance by controlling temperature increase s. The implementation of these technologies can contrib ute to making solar collectors more effective, efficient, and du rable, thereby encouraging the wider adoption of solar energy systems. However, it is crucial to keep in mind that each technology has its advantages and disadv antages. Therefore, factors such as the features, cost implications, and enviro nmental impacts of the chosen technology shoul d be considered. This study includes detaile d examinations of th e use of nanofluids in solar collectors. Th e research aims to prov ide valuable insights for future studies in the field of solar energy by thoroughly explo ring these app lications. The characteristics, cost implications, and environmental impacts of these technol ogies have been examined to consider both their advantages and di sadvantages. The comprehensive analysis of nanofluids in solar collectors may pave the way for advancements and innovations in the future, encouragin g the development of more effective, efficient, and durable solar energy systems. Keywords Solar collectors, Nanofluids, Thermal an d hydraulic performances 1. Introduction The use of fossil fuels, greenhou se gas emission s, and environmental issues such as climate ch ange hav e led many countries to review their 1 Firat University, Automotiv e Engineering Email: [email protected] , ORCID NO: 000 0-0002-9636- 5746 152 et al., 2022) . Nevertheless, the inadequate management of waste, particularly in developing nations, hinders ef ficient treatment measures. Consequently , the duration required for waste disposal is substan tial, and the inadequately regulated disposal of waste presents a significant peril to both the marine ecosystem and populous urban areas worldwide (Ferronato & T orretta, 201 9). The main purpose of SWM is to efficiently han dle the collection, separation , treatment, and dumpin g of solid waste produced by vario us metropolitan populations. This purpose aims to ensure that these activities are c onducted in a sustainable manner , taking into consideration env ironmental and social considerations, while ut ilizing th e most econo mically feasible resources available (Khatiwada et al., 2021). The utilization of waste as both main and secondary raw materials for the manufactur ing of consumer products within urban areas needs to be prioritized (OECD, 2 021) . The issue of SWM in developi ng nations is further compo unded by the indiscriminate dispo sal of waste, r endering it a sign ificant env ironmental contaminant (A. H. Khan et al., 2022). The most po pular methods of processin g and managing waste in developing nations are landfilling, incineration, open dumping, and composting (Hajam et al., 2023a) . Open burning and dumping are still often used fo r wast e dispo sal, desp ite their many negative effects on the environment (Barbhai & Sh arma, 2023) . Inadequate waste manag ement practices can lead to significant environmental issues. Th e accumulation of waste in op en landfills has deleterious effects on soil contamination and poses a threat to the in tegrity of the adjacent gr oundwater (Hasthi et al., 2023). The implementation of ef fective solid waste management practices has the potenti al to mitigate or eradicate adv erse ef fects on both the environment and the health of hu mans. Additionally , it can serve as a catalyst fo r growth in the economy and enhance ove rall living standards (Das et al., 2019; Singh Rawat et al., 2020 ). This study focuses on the following objectives: assessing the effects of soli d waste disposal in open dumps and investigating rehabilitation strategies fo r open dumping sites in order to mitigate enviro nmental and economic consequ ences. 2. Global W ast e Production Global production of waste is defin ed as th e cumulative quantity of waste generated via human activities on a global scale within a designated timeframe. This waste might originate from several sources, encompassing municipal, industries, farming, medical centres, and other sectors (Höglund-Isaksson et al., 2020) . The prod uction of waste is a significant concern fro m both an environmental and social standpoint due to its potential to result in a range of 255 adverse effects, includ ing contamination, th e destruction of habitats, and threats to the health of people (Marín-Beltrán et al., 2 022). The gen eration of waste on a glob al scale exhibits a con sistent up ward trend, encompassing dev eloped nations as well as dev eloping nations. Notab ly , a substantial volume of waste is generated annually in cou ntries belongi ng to the Or ganisation for Economic Co -operation and Development (OECD) (Parfitt et al., 2021). The issue of glob al waste production is of great significance, as evidenced by estimates suggesting that the col lective worldwide wast e production reached ov er 20 billion tons in the year 2017. Th is equates to an average of 2. 63 tonnes of waste prod uced per person annually (Maalouf & Mavropoulos, 2023) . MSW prod uction, expressed in kilograms per capita, is illustrated in Figure 1 (URL 1). Figure 1. MSW generated per year (in kilog rams per capita) (URL 1) According to projections based on the st atus quo, it is anticipated that global waste prod uction will reach 46 billion tons in the year 2050 (Mendoza et al., 2022) . The quantity of municipal solid waste (MSW) constitutes a relatively smaller part, estimated to be between 2.3 and 3.1 billion tons in the year 2019, and is projected to rise to a range of 2.89 to 4.54 billion tons un til 2050 (He et al., 2022) . Similarly , based on a report published by the W orld Bank, it is projected that th e yearly production of municipal solid waste cou ld reach a staggering 3.4 billion tons by 2050 (Kaza et al., 2018) . 256 On the other hand, the challenge of accumulating unmanaged plastic waste has become increasingly worrisome. According to estimations, the global production of unmanaged plastic waste rang ed from 60 to 99 million tons in 2015. Furthermore, projection s indic ate that the qu antity might potentially trip le to reach 155 -265 millio n metric tons annually in 2060 (Lebreton & Andrady , 2019). In developing natio ns, the majority of waste is primarily derived fr om household activities and predominantly consists of organic matter derived from plants. The escalating urbanization of communities is a promin ent component that is progressively implicated in the generation of trash stemming from industrial and agricultural activities, residual chemicals, and the discharge of hazardous metals (F . F . Robert et al., 2023). 3. W aste Manag ement The field of solid waste management encompasses the effective management and app ropriate disposal of waste materials, with the aim of mitigating adverse ef fects on both human health and the natural enviro nment (S. Kh an et al., 2022) . For the purpose of maximizing practical advantage, the waste management hierarchy presents the preferred sequence of steps fo r waste r eduction and management. Land fills are the fin al resort in waste management; prevention, reduction, recycling, and ener gy recovery are prio ritized in t he was te hierarchy (Kabirifar et al., 2020 ; URL 2) (Fig ure 2). Figure 2. W aste hierarchy (URL 2) Before being processed, MSW must be separated into recyclable, biodegradable, combustible, and non -recyclable categ ories in order to lessen the 257 negative ef fects (Ugwu et al., 2021). Th e waste materials, including paper , glass, and metals, have the po tential to be repurposed in order to reduce the demand for primary resources (David et al., 2019). Furthermore, the process of remediating biodegradable waste involves the conversion of such waste into stable organic molecules, which can serve as an e nvironmentally benign source of ener gy , such as biogas (Srivastava et al., 2020). The present condition of waste management in both developed and dev eloping countries is cause for concern, particularly in develop ing countries, because there is a lack of waste management methods , necessitating the implementation of environmentally sustainable and cost-effective approaches for its management and disposal (Arenib afo, 2023; Debrah et al., 20 21; ULUSOY et al., 20 23) . Several strategies and technological approaches are employed in the field of solid waste management, encompassing incineration, recycling, landfilli ng, composting, and reduction (Istrate et al., 2020; Karimi, 20 23). Nevertheless, the implementation of efficient waste management metho ds encounters various problems, includin g insufficient financial resources, inefficient collecting methodologies and equipment, irresponsible dispo sal procedures, and a lack of educated pr ofessionals in managing waste (Kurniawan et al., 2022; Li et al., 2021; Shi et al., 2021) . The current emphasis is on prioritizing reducing waste as th e primary approach to address this issue, as opposed to the former emphasis on recovering, recycling, and disposing objectives (Parfitt et al., 2021). In addition to the traditional solid waste management techniques such as vo lume reduction and landfilling, high-income countries (HICs) ar e also implem enting alternativ e methods includ ing vermicompo sting, sustainable development strategies, and waste- to -energy systems (Alshehrei & Ameen, 2021; Hajam et al., 2023b; Usmani et al., 2020) . These waste- to -energy systems encompass various processes such as incineration, pyrolysis, gasification, and anaerobic digestion, as well as the production of biodiesel, biohydrogen, biomethane, bioethanol, and butanol (Barua & Hossain, 2021; S. Y . Lee et al., 2019; Manikandan et al., 2023) . One potential strategy involves th e utilization of waste biorefineries, which have the capability to trans form municipal solid waste (MSW) into sustainable ener gy sources, as well as value-add ed commodities and chemical compoun ds (Molina-Peñate et al., 2 022; Pérez et al., 2020 ). 4. Open Dumping for W aste Manag ement Open du mping and landfilling are often employed method s for the management of MSW according to their cost -effectiveness and minimal treatment requirements (A l-W abel et al., 2022) . The utilization of landfills is 258 suitable for waste that cann ot be recycled or incinerated. Nevertheless, it requires vast expanses of land. Th e leachate generated from the anaerobic and aerobic decomposition of th ese waste materials contains componen ts that are detrimental to the environment (El -Saadony et al., 2023; Pazoki & Ghasemzad eh, 20 20) . Accordingly , landfilling becomes the worst op tion when its negative ef fects on the environment, human health, the qu ality of the land, and the ground water are all taken into account (Blair & Mataraarachchi, 202 1; Pires & Martinho, 2019) . Landfilling has witnes sed significant expansion in low- and middle-income countries (LMICs) during the past decade. One of the outcomes resulting from this expansion is the emergence of open land fills as a means of soli d waste management in various regions across the glob e (Idowu et al., 2019). In LMICs, landfilling is a prominent repository for a substantial portion of waste, posing a potential threat to biogas releases caused by the anaerobic decomposition of waste (Chisholm et al., 2021). Additionally , the movement of leachate in these landfills may pollute all surface and groundwater sources. The scenario becomes increasingly concerning in nations that lack protective measures and have landfills situated in close proximity to lakes (Parvin & T areq, 20 21; Zhang et al., 2021) . Fortunately , developed countries have started disabling solid waste dumping by stringent regulations, waste reduction, and reuse. In these countries the waste manag ement pri nciple known as "R educe, Reuse, and R ecycle" (ofte n referred to as the '3 R') is widely adopted and implemented, making it less probable for this scenario to o ccur (Batista et al., 2021; Nanda & Berruti, 2021) . 5. Composition of MSW W aste is the byproduct of any human action, be it the routine tasks of daily living or the more involved activities of industries like manu facturing and farming. W as te encompasses a diverse range of components, which exhibit variations am ong nations and areas, contingent upon t he prevailing cultura l practices and lifestyles (Ela min Abbass et al., 2023). The MSW is comprised of several types of waste, including recyclable, organic, combustible, and materials that aren't recyclable. In LMICs, th e proportion of substances that decompose in MSW ranged from 46 % to 53%. Similarly , the quantity of reusable waste in LMICs was fo und to be comparatively smaller than that in HICs (UNEP , 2015). MSW , with a high concentration of organic materials, is a major contributor to atmos pheric pollution because it releases gree nhouse gases (GHG) and leachate, which contaminate grou ndwater (Cheng et al., 2020; Mor & Ravindra, 2023) . Figure 3 shows th e compositio n of MSW on a global scale (S harma & Jain, 2020 ). 259 Figure 3. Global MS W Composition (Sharma & Jain, 20 20) 6. Envir onmental Impacts of M SW Open Dumping The phenomenon of urbanization has led to environmental degradation, posing a significant issue that warrants careful examinatio n (S. Robert et al., 2023) . Potential factors contributing to environmental degradation encomp ass the release of wastewater and effluents, runoff from agriculture, as well as unregulated disposal of solid waste in close pr oximity to water bodies (Jurado Zavaleta et al., 2021) . The impacts on the ecosystem from du mping waste in the open are serio us. It causes contamination in a wide vari ety of env ironments, from the ocean to the air to the groundwater (Sid diqua et al., 2022) . The practice of open disposal of MSW results in the generation of hazardous compounds that pose risks to both human health and th e environment. These compounds, including dioxins and dioxin -like substances (specific ally polychlorinated dibenzo-para-diox ins and polychlo rinated di benzofurans), in addition to harmful heavy metals such as nickel and cadmium, are transported into t he water , soil, and atmosphere (Roy & T arafda r , 2022). The con tamination of water and soil resources on a worl dwide scale is a consequ ence of various factors, including the transfer of leachates containing toxins, the relea se of GHG, and the productio n of odou r and dust thro ugh open dumping and landfilling practices (Al-W abel et al. , 2022) . This section will cov er the neg ative effects of open dumps for MS W on soil, air , water , and the health of h umans. 6.1 W ater an d Soil Contamination According to several research, open dumps con tinue to be the leading cause of water and soil pollution ( Alao, 2023; Mekonnen et al., 2020). Additionally , the 260 unregulated accumulation of MSW at landfills has detrimental con sequences for soil quality , leading to a predominance of acidic and sandy conditions, as well as impacting microbial populations (Mouhoun -Chouaki et al., 2019). An issue arising from the dumping of solid waste is the deg radation of organic content inside the waste, resulting in the production of leachate. The very dissolved leachate has the ability to infiltrate into the soil and into water (de Cassia Silva Bacha et al., 2021) . Over and above, the process of leaching, whereby or ganic, inorganic, and other deleterious compounds are released from solid waste and infiltrate the sub terranean water , has the potential to result in the contamination of sources of water (Abdel-Sh afy et al., 2023) . Moreover , metals including cobalt (Co), cadmium ( Cr), cop per ( Cu), lead (Pb), and zinc (Zn) may contaminate soi l at landfills, which can subsequen tly be taken up by plants and earthworms and pose a threat to bo th human and environmental health (Aendo et al., 2022; Morita et al., 2021) . At the same time, Contamination of surface water sources by heavy element accumulation in soil , such as Cd, Zn, and Pb, may result in biomagnification in the food chain (Gupta et al., 2019). Another research showed that the dispo sal of solid waste r esulted in a substantial rise in many water para meters, including conductivity , T otal Dissolved Solids, hardness, and alkalinity . Additional concerns include malodorous odor , microbiological pollution, and water discol oration. Th e abundance of ni trogen and ph osphorus led to the occurrence of elevated algal blooms in rivers and streams (Mohan & Joseph, 2 021) . 6.2 Air Pollution The presence of airborne particulate matter and the accumulation of solid waste from ur ban areas may lead to the occurrence of contaminants in the air and the generation of smells that are unpleasa nt (Al-W a bel et al., 2022). As well as the practice of open dumping MSW results in the unregulated generation of landfill gases, predominantly composed of methane and carbon dioxide (Chandra & Ganguly , 2023). Moreover , current numbers imply that over 20 years methane has a gl obal warm ing potential of 81.2 , while carbo n dioxide only has a po tential of 27.9 du ring 10 0 years (IPCC, 2019). The International Panel on Climate Change (IPCC) has also noted in its most recent reports, that th e level of methane has risen to above 1000 ppb during a period of the last twenty years (IPCC, 2019). In light of a substantial rise in methane emissions from MSW , comprehensive investigations have been conducted to analyse the possibility of production from MSW and explore ef fective methods for converting it into ener gy fo rms. Thes e ef forts aim to mitigate its release into the environment (Hai et al., 20 23; 261 Naveenkumar et al., 2023; Y ang et al., 2023) . Increased gr eenhouse gas emissions are directly attribut able to the widespread practice of open waste du mping in developing countries (Ferronato & T orretta, 2019) . Specifically , landfill gases are released when biological waste is decomposed by bacteria in anaerobic environments (US EP A, 2023 ; Mey er -Dombard et al., 2020) . On the other han d, several varia bles influence how much methane gas is released from an open dumpsite, like the overall am ount of garbage dumped, the weather , and the way the waste is collected (Pu jara et al., 2023) . In a recent report conducted by the United States Environmental Protection Agency (USEP A), it is emphasized that landfill methane emissions in the Unit ed States con tribute to around 17% of the overall methane productio n (US EP A, 20 22). By 2030 and 2050, developing countries are projected to account for 64 and 76% of glob al greenhouse gas emissions, up fro m their 29% share in 2000 (Rafiq et al., 2018). 6.3 Impacts on Human Health Moreover , the in discriminate disposal of MSW through open du mping practices has the potential to engender adverse health con sequences for individuals residin g in close pr oximity to th ese dumping sites. Such health risks encompass diseases such as skin and ocular irritatio n, elevated body temperature , respiratory distress, gastrointestinal disturbances, and a range of other ailments (Dixit et al., 2023) . Open dumping additionally exposes people's health at risk since it can contaminate subterranean water supplies and release gases that can af fect nearby populations in ways that can cause canc er . Moreover , this type of illegal landfill has the potential to trap various creatures and establish favo urable conditions fo r the proliferation of pests, notably mosquitoes, so exacerbating both health and environmental risks (Chireshe et al., 2023) . 7. Open Dumping Rehabilitation: A W ay to Reduce Env ironme ntal and Financial Impacts Extensive environmental degradation on Earth has prompted significant stud y ef forts toward contamination mitigation and rehabilitation. The rehab ilitation procedure encompasses the transformation of pollu ted areas into gardens and the establishment of nurseries for ornamental plants. The economic benefits of collecting biogas and leachate from the MSW treatmen t process can be significant for governments. In addition to the econo mic advantages, the implementation of suitable method s for the extraction of haz ardo us compounds from MS W has th e potential to yield societal benefits. In contrast, the 262 implementation of suitable waste removal solu tions necessitates a larger investment and incurs higher costs for m aintenance and op eration. The implemen tation of rehabilitation solutions for open dumping areas i s crucial in addressing th e risks to health and the env ironment that are inherent to these unregulated and filthy waste disposal regions. These sites have the potential to contribute to the contamination of soil and water , t he devastation of habitats, and the di ssemination of illnesses. Below are a f ew commonl y employed techniques for rehabilitating open du mping sites: landfill mining, soil capping process, lan dfill gas collection system, bior emediation, revegetation, and phytoremediation. 7.1 Landfill Mining (LFM) Landfill mining is a method that involves extracting valuable materials fro m dumping sites. This method has the potential to be a viable alternative for promoting environmental development and managing waste ef fectively (Zoungrana et al., 2022) . LFM entails the removal of waste from a landfill site that has bee n closed for a lengthy time, typically span ning many years . Throughout this time, the dump has ceased to receive waste and the natural breakdown of waste has significantly decreased (Somani et al., 20 20; Zari et al., 2022) . In the current world situation, with its expand ing demands for resources, increasing prices of raw materials, dwindlin g natural reserves for critic al commodities, and worseni ng env ironmental issues, LFM presents an opportunity for obtaining resources fr om alternative sou rces (Jain et al., 2023) . Extracting resources from bo th current and upcoming landfills can result in the utilization of secondary materials and energy , hence minimizing its spatial footprin t (Singh & Chandel, 2020). The afo rementioned demonstrates that LFM aligns with the EU Roadmap for a Resource-Efficient Europe, which aims to minimize the need to acquire new lands by 2050 (Pitak et al., 2023). Although there has been growing attention towards LFM and its progress over the past twenty years, the release of dust from mining and la ndfill mining activities into the environment continues to be a significant problem for public health (Article Author et al., 2019; Capp ucci et al., 2020 ; Qarahasanlou et al., 2022) . This is particularly important in cases where old landfills possess the ability to create pollution (H. Lee et al., 2023). The qualities of the mining waste components are influenced by the level of deterioration, kind, and age of the waste. The waste that has been retri eved primari ly comprises of soil -like substances, pl astic, metal, glass, textile, cera mics, and stones. The predominant 263 constituent of the extracted waste is a substance resembling soil (Cheela et al., 2023; Han et al., 2024) . 7.2 Soil Capping Process This step would occur as the initial corrective measure that s hould be implemented while the landfills are finally decommissioned. A landfill cap is a complex structure consisting of multiple layers that are desig ned to limit the amount of water that seeps into the waste dumped in the landfill. It also helps to minimize th e generation of leaches and prevent the unrestricted dischar ge of landfill gas through the enviro nment. In addition, physically separating waste from organisms such as animals and plants (Ahmed S. et al., 2022) . The choice of cappi ng form fo r a site is contingent upon various aspects, such as th e nature and levels of pollutants, the site's dimensions, the precipitation levels in the lo cation, and the exp ected later utilization of the land. 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In Cir cula r Economy in Municipal Solid W aste Landfilling: Biomining & Leachate T r eatment (pp. 1–23 ). 96. Saljnikov , E., Mu eller , L., Lavrishchev , A., & Eulenstein, F . (2022). Advances in Understanding Soil Degrad ation Innovatio ns in Landscape Resear ch . https://link. springer .com/boo kseries/161 18 97. Scheutz, C., & Kjeldsen, P . (2019) . Guidelines for landfill gas emission monitoring using the tracer gas dispersion method. W aste Management , 85 , 351–360. https://doi.org/10.1016/j.wasman.2018.12.048 98. Sekhohola‐dlamini, L. M., Keshinro, O. M., Masudi, W . L., & Cowan, A. K. (2022). Elaboration of a Ph ytoremediation Strategy for Su ccessful and Sustainable Rehabilitation of Disturbed and Degraded Land . Minerals , 12 (2). https://doi.org/10.3390/min120201 1 1 99. Selvarajan, R., Ogola, H., Kalu, C. M., Sibanda, T ., & Obize, C. (2 022). Bacterial Communities in Informal Dump Sites: A Rich Source of Uniq ue Diversity and Functional Potential for Bioremediation Applications. Applied Sciences (Switzerland) , 12 (24). https://doi.org/10.3390/app122412862 280 structures were ob served to chang e into flakes and spheroids. Fig ure 3 show s the structural changes in powders with the change of gas pressu re. When the powders taken from Bakelite were ex amined, it was seen that the high est hardness was 73 HV0.0 25 in pr oduction at 35 bar. Th is hardness value was found to be high er than the hard n ess of the AM60 alloy in ingot fo rm (67 HV0.025) ( Çetin, et al, 2020). Figure 3: Production s made with a)5, b)15, c)25, d)35 b ar pressure (Çetin, et al., 2020) In the study carried out by Urtekin, Ünal and Özer, bronze and c op per powder were pr oduced us ing water and gas atomization. These bron ze and copper powders are intended to be used in self -lu bricating bearing pressing. CuSn10 was produced by water atomization metho d. Cu powder was also produced by gas atomizatio n. The s ize of the Cu Sn 10 powder pr oduced by water atomization was determined as 41.5 μm, and the powder size of the Cu powder produced by the gas atomization method was deter mined as 41.9 μm. Figure 4 shows the copper powder ob tained by gas atomization, and Fig ur e 5 shows the bronze image obtained by water atomization. A self -lubricating bearing was produced by pressing the resulting powders. This product was subjected to sinterin g at 780 ºC in a pro tective atmosphere mixed with hydrogen and nitrogen (Urtekin, et al., 2020). Comlicated Flaky Sp herical Droplet Flaky Spherical Spherical Droplet Complicated Droplet Spherical Spherical Droplet Droplet 287 Figure 4: Cop per powder produced by gas atomization method (Urtekin, et al. , 2020) Figure 5: Image of bro nze powder produced by water atomization method (Urtekin, et al., 2020) In the study conducted by Akkaş, Akra, Çetin a n d Boz, AZ31M g alloy powder was pr oduced by the gas atomization method. In these productions, th e effect of changing the gas pressure parameter on the po wder shape and size was examined. In the exp eriments, the alloy was melted at 790 ºC. 5, 15, 25 and 35 bar gas pressu re was used. The nozzle diameter is determined as 2mm. XR D and XRF analysis were p erformed using a scanning elec tron microscope to see the shape of the powders and the states of the phases occurri ng in the internal structure. A laser measuring device was also used to determine powder sizes. As a result of production by gas atomization, ligamentous, rod -like, droplet- like, flaky and spherical powder shapes were det ected. As the gas pressure increased, an increase in flake and spherical struct ures was observed. SEM images of po wders produced under different gas parameters are shown in Figure 6. The finest powder was ob tained at 35 bar, which is the highest pressure. As a result of this study, it was o bserv ed that with the increase in gas pressure, the powder size decreased and the powder structu res began to take a spherical shape (Akk aş, et al ., 2018). 288 Figure 6: Powder images o btained with a)5, b)15, c)25 , d)35 bar gas pressure (Akkaş, et al., 2018) In the study conducted by Akkaş, Çetin and Boz, Al12Si alloy powder was produced by the gas atomization method. The aim of the study was to examine the effects of chang es in temperature, dif ferent no zzle diamet ers and different gas pressure parameters on powder sha pe and size. As a result of the study, by reducing the no zzle diameter and increasing the gas pr essure, the powder size decreased an d the powder structures generally had lig amentous , droplet-lik e, rod-like and complex shapes. The finest powder was obtained at the hi ghest pressure of 35 bar (Akkaş, et al ., 20 18). Droplet Spherical Droplet Droplet Spherical Spherical Ligament Ligame nt Ligament Ligament Ligament Ligament Comlicated Flakly 289 Figure 7: Production images with a)5, b) 10, c )15, d) 20, e)30, f)3 5 bar gas pressure (Akkaş, et al ., 2018) In the study conducted by Küçü k, Öztürk and Kılıçarslan, th e recycling of lead, which is among the heavi est met als in na ture, was stud ied. In th is study, waste lead was cooled wit h a cold no zzl e gas ato mization tower and turned into powder. Powdered lead is con sidered to be used a s a fastener to be used in pipe connections. At the s ame time, it is ai med to improve the me cha nical p roperties, corrosion and wear resistance of this product and susta inability. A do uble-sided press was used to pr ess the powders. The pressing process was do ne with 100 bar pressure. Fig ure 8 shows the optical microscope image aft er pressing. Th e pro duct, shaped by pressing, was subjected to sintering at 240 ºC for 15 minutes. Figure 9 shows the optical microscop e examinatio n image after sintering. ( Küçük , et al., 2018) 290 Figure 8: Optical microsc ope image after press ing (Küçük. , et al., 2018) Fig ure 9: Optical microscop e image after sintering (Küçük, et al., 2018) In the study con ducted by Li u et al., Fe - Si -B-C-P powders were prod uced by water atomization method. The morphological structures, chemical compositions, phases and magnetic properties of the obtained powders are discussed. Powder structures wer e generally detected as dendritic and spherical, as shown in Figure 10. Compared to gas atomization, high amounts of oxygen were ob served in th e powders. It is thought that the Fe content in the m aterial may increas e magnetization. It has been stated that water atomi za tion is suitable for industrial applications due to its low cost. (Liu , et al., 2011) 291 Figure 10: App earance of Fe-based powders a) General app earance, b)Dendritic powders, c) Sp herical powders, d ) Microstructure (Liu, et al., 2011) In the stud y conduct ed by Aydın and Ünal, nozzle structure, which is one of the factors affecting the powder structure in powder production by gas atomization, was emphasi zed. Within th e scope of the stu dy, a supersonic nozzle with a circular slot was designed. In the study where tin was used as the metal, exc essive heating was applied up to 430 ºC and production was carried out with gas pr essures of 0.54, 0.9, 1.23, 1.31 and 1.47 MPa. When the po wder structures are examined, the powders have a smoo th surface and sphe rical shape, and the average powder size d 50 is measured to be 11.39μm. As seen in Figure 11, there are also satellites in th e dust. ( Aydın and Ünal , 2 007) Figure 11: Tin po wders produced by gas atomization . ( Aydın and Ünal , 2007) 292 In the research conducted by Ak kaş, Çetin and Boz, powders obtaine d with AM60 metal were examined using the gas atomization method. In this study, nozzles with diameters of 2, 3, 4, and 5 mm w ere used. In the study where argon gas was used, it was work ed at 770 ºC and 35 bar gas pressur e. It was observed that the general shapes of the po wders were rod -like, drop-like, ligamentous, complex and spherical. As shown in Figure 12, it was determined that the powder shapes changed into droplet -like and spherical as the nozzle diameter decreased. (Akk aş, et al. , 201 8) Figure 12: SEM image of AM6 0 powders (Akk aş, et al. , 2018 ) RESULT In or der for the sintering and pressing of the products to be more successful, powders with a spherical structure a re required. Th is is one of the most important a dvantages of the gas atomization me thod in obtaining spherical powder. Reducing the cost of glob al powder prod uction is possible by adjusting the optimum parameters of gas atomi zation variables. It has been observed that as the gas pressure used in atomizatio n processes increases, the powde r size decreases and moves from a complex , ligamentous and rod -like structure to a spherical structure. Literatu re research has sho wn that gas pressure greatly affects powder structure. At the same time, an increase in hardn ess values was observed with i nc reasing pressure. However, it has been observed that the effect of pressure on reducing powder size after a certain level is no t at the desired rate. Howeve r, it has been determined that th e effect of gas pressure varies depending on the type of metal used . It has been observed that as the nozzle diameter decreases by a certain amount, the spherical powder in the powder content increases. 293 REFERENCES 1. Akkas, M. , Çetin, T., Boz, M., (2018). Al12Si P owder Produ ction an d Characterization by Gas Atomization Method , Dicle University Journ al of Engineering , 9 (2 ): 795 -804. 2. Akkaş, M. Çetin, T. , Boz, M. (2018). AM 60 Magnesiu Alloy Powder Production and Characterization by Gas Atomization Me th od, SDU International Journal o f Technological Sciences , 10( 3), 1 - 9. 3. Akkas, M. (2019 ). Investigatio n of the Effect of Ga s Pressure on AZ31 Mg Powder Production by Gas Atomization Method, GÜFBED/G UST IJ , 9(2 ): 215-221. 4. Aydın, M., Ünal., (2007). 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(1972) Modern Atomizing Techniques, Powder Metal , 15(29), 67 - 94 . 10. Gündeş, A., Yaykaşlı H. v e Özger , H., (202 1). Comparison of Structural and Thermal Properties of AgCu Alloys Pro duced by Mechanical Alloying and Newly Dev eloped Gas Atomization Me thod, Bitlis Eren Üniversitesi Fen Bilimleri Dergisi , 10 , 1220 -1231. 11. Küçük, Ö., Öztürk, B., Kılıçarslan M. F., (2018). Production Of Fittings Materials With Powder Mettalurgy Meth od For Recycling And Sustainability Of Contaminant Plumbic Material With Gas Atomization, Karadeniz Chemical Science an d Technology , 2 , 11- 14 . 12. Liu , Y., Niu, S., Li , F.i., Zhu,Y., He, Y. (2011). Preparation of Amorphous Fe-based Ma gnetic Powder by Water At omization, Powder Technology, 213 (1 - 3) , 36- 40. 294 13. Sheikhaliev, S . M., and Dun kley, J. J. (1996). A Novel Internal Mix ing Gas Atomiser for Fine Powder Production, in: Advances in Powder Metallurgy and Particulate Materials, vol .1 , Part 1 , pp. 16 1-170 MPIF and APMI International, Princeton , NJ, USA. 14. Urtekin. L, Ünal , R . an d Aydın. Ö. (2 020). Effect of Powd er Processes on Lubricated Bearings, Dicle University Jo urnal of Engineering , 11 (2), 657 -652. 295 Chapter 20 The response of soil properties to global climate change Fatma Olcay TOPAÇ 1 INTRODUCTION Climate change, a gl obal phenomenon, has been an ongo ing process since the inception of the Earth. Over the last decade, it has evolved into a prominent subject of both scientific inquiry and political discourse. While di scernible cold and hot cycles punctuate the Earth's climatic history, the pace of these alterations has notably accelerated in the past 15 0 -200 years on a global scale (Fauchereau et al., 20 03). In the contempor ary discourse on environmental sustainability, the focal ch allenges of climate change and global warming have risen to promin ence, demanding immediate attention and concerted efforts. The persistent elevation of greenhouse gases (GHGs) arises from a multifaceted interplay of human-indu ced activities — such as industrialization , urbanization, and intensive agricu lture — and natural phenomena like fo rest fires, volcanic eruptions, and alteration s in vegetation and snow cover. This complex in terplay instigates unprecedented alterations in the global environment, encompassing modifications in atmospheric gas composition, spatial and temporal shifts in global temperatures, and variations in precipitation patterns, as underscored by Abbass et al.(2022). Attributed to these combined hu man and natural factors, the average global te mperature has been estimated to have risen by approximately 1 degree Celsius, with a likely range of 0.8 to 1. 2 degree s Celsius, compared to the pr e- indu strial period. To avoid exceeding a 1. 5 °C temperature rise, it is imperative to halve net carbon dioxi de emissions within the coming decade, with the remaining half mitigated between 2030 and 2050. Climate mod els indicate that achieving a world with net -zero carbon emissions by 2055 is crucial for a r ealistic chance of meeting the 1.5 °C target. If this mi lestone is delayed until around 2070, the glob al warming objective shifts to 2 °C, resulting in graver consequences for human bein gs and exceptional climatic conditions, resembl ing an apocalyptic scenario (Varghese 202 3). Minor variations in the overall gl obal temperature can trig ger notable environmental anxieties, setting the stage for substantial chang es in climate and weather 1 Prof . Dr.; B ursa Uludağ Ün iversitesi Mühen dislik Fakü ltesi Çevre Mühendisliğ i Bölümü. [email protected] ORCID No: 0000 -0002-6364- 4087 296 SOIL ORGANI SMS Among the potential impacts of climate change on s oil, th e most significant considerations pertain to subterranean biodiversity, encomp assing bacteria, microbes, fungi, microscopic invertebrates, and larger invertebrates lik e earthworms, ants, and termites. The influence of climate change on soil biodiversity is twofol d: direct effects stem from alterations in soil temperature and moisture, while indirect effects arise from changes in vegetation communities, productiv ity, and the rate of organic matter de composition. Notably, not all soil biota will experience the same deg ree of impact from climate change. In an investigation, the response of soil communities to deliberate warming (+4 °C) and increased atmospheric CO 2 levels (800 ppm) was examined within a two-year field experimen t carried out in the boreal forest. The initial year of the study aimed to assess the effect of t hese simulate d climate change factors on community composition, wealth of species, diversification and similarity. Surprisingly, in the first year, exp erimental practices had minimal effects on the fauna. However, during the second year, oribatid mites exhibited responses to both warming and elevated CO 2 levels. Additionally, there was an increase in the richness and diversity of sprin gtails, accompanied by alterations in the composition of the soil community (Meehan et al., 2020). The modification of microbial soil respiration rates, induced by global phenomena like warming, is a direct consequence of the temperature sensitivity inherent in soil microorg anisms and th e processes th ey mediate. DeAngelis et al. (201 5) observed that under con ditions of a 5 -degree Celsius temperature increase in a temperate forest, alterations occurred in the proportional representation of soil bacteria. Fu rthermore, the community 's bacteria - to -fungus ratio demonstrated an increase. Elevated atmospheric CO 2 affects soil microbes by increasing mycorrhizal colonization. CO 2 enrichment is expected to boost mycorrhizal biomass because plants req uire more nitrogen and phosphorus, which aligns with in creased carbon assimilation rates. So , at high CO 2 levels, mycorrhizal bi omass increases as C becomes relatively less limiting and soil nutrients become more limiting for plant growth (Drigo et al., 20 08). A study focused on alpine forest ecosystem s employed soil column experiments to assess the impact of climate chang e on soil microbes. The study simulated climate warming and cooling, mimickin g temperature changes within the range of ±4.7°C. The fin din gs indicated that warming induced structural alterations in microbial communities across all soil layers. Conversely, cooling did not exhibit a notable influence on the structure of bacterial communities in the various soil layers (0 –10 cm, 10 –20 cm, and 2 0 –30 cm), but it significantly 303 impacted fung al communi ties throug hout these layers. The study concluded that variations in soil fungal community structure were primarily driven by soil moisture con tent and temperature, while soil bacterial community struct ure exhibited a closer associati on with overall soil cond itions (Fu et al., 2023). SOIL ACIDIFICATION AND SALINIZATI ON Climate change, characterized by global warming and al terations in precipitation patterns, can significantly influ ence soil acidity . Cl imate chang e often brings more intense and frequent rainfall. Th is increased precipitation can lead to greater leaching of base cations. Elev ated temperatures linked to climate change expedite the breakdown of organic material within the soil . Th is process releases organic acids, further contributing to soil acidity. Faster decomposition can reduce the buffering capacity of the soil, maki ng it more susceptible to changes in acidi ty (Gelybo et al., 2018 ; Gupta and Upadhyay, 20 23). In the investigation assessing pH variations in Tibetan Plateau grassland areas between 2000 and 2020, alongside temperature, precipitation, and radiation data, findings revealed that climate change in duced soil alkalinization at depths of 0-10 cm and soil acidification at depths of 10 -20 cm and 20-30 cm. The study determined that, under conditions of climate change, soil alkalinization occurred in 23.71% to 36.84% of the surv eyed regions, while soil acidi fication was observed in 21.43 % to 45.52% of the examined areas (Sun et a l., 20 23 ). On the ot her hand, a rise in temperature combined with reduced rainfall can trigger capillary water movement and the evaporation of groundwater. This process, as highlighted by Varallyay (2007), may give rise to the accumulation of salts in the soil, a phenomenon commonly referred to as salinization. In a study conducted by Khamidov (2022), the salinity dynamics of irrigated lands in the Khorezm region (Uz bekistan) under the influence of climate change wer e assessed, and projections for salinity increa ses were made using statistical methods. Th e results of homogeneity tests indicate that by the year 2100, there will be an in crease of 32.5% and 15.1% in areas classified a s mod erately and highly saline, respectively, while areas c lassified a s sl ightly salin e are projected to decrease by 52.4%. The study concludes that salinity levels across the examined region will sig nificantly increase as a result of climate ch ange. In a study conducted by Bann ari and Al-Ali (2020), the enduring impacts of a 30 -year peri od characterized by escalating temperatures and diminish ing precipitation were investigated. The results underscored a po sitive correlation between these climatic changes and soil salinit y, particularly in arid regions where reduced soil leaching occurs. Mor eover, the ongoing trend of global warming may intensify salinity con cerns in agricultural lands situated in coastal 304 areas, primari ly attrib uted to the melting of ice she ets and th e conse quent rise in sea levels. In alignment with these findings, Rahman et al. (2018) ob served a noteworthy surge in the salinit y rate within coastal agricultu ral regions, escalating from 1% to 33% o ver the past 25 years. CONCLUSION AND RECOMME NDATI ONS In con clusion, th is chapter has prov ided a comprehensive exploration of t he multifaceted impacts of climate change on soil s. Th e intricate interpl ay between rising temperatures, unstable precipitatio n patterns, and extraordinary weather events has been thoroughly examined, sheddi ng light on the intricate dynamics influencing so il processes. Fro m alterations in soil temperature and moisture content to the consequential changes in soil structure a nd microb ial activity, the effects of climate change resonate a cross various layers o f the soil ecosystem. The studies discussed highlig ht the vulnerability of soils to climatic shifts, with implicatio ns extendi ng beyond mere changes in physical and chemical properties. Soil erosion, salinizatio n, and shifts in microbial communities underscore the far-reaching consequences th at climate chang e imposes on soil health and fertility. Mo reover, the interconnection between soil health and broader environmental considerations, such as agriculture, biodiversity, and ecosystem functioni ng, emphasizes the ur gency of under standing and mitigating these impacts. The un certainties inherent in climate change, its impact on long -term soil dynamics, and the complex interactions with agricultural practices all emphasize the importance of continued scientific inquiry. To address these uncertainties and sup port ambitio us goals, future stud ies may focus on the following areas: - Investigating how climate change in fluences soil processes over the long term, includ ing aspects such as nu trient cyclin g, microbial activity, and soil structure. -Understanding ho w climate chang e interacts with di fferent agricultural practices, such as crop rotation, irrigation methods, and soil management techniques, to identify sustainable and resilient approaches. -Assessing the consequ ences of variou s adaptation op tions, con sidering factors such as their effectiveness, economic vi ability, and environmental sustainability. -Examining the complex in terplay of factors that affect the outcomes of adaptation strategies, including socio-economic factors, technological advancements, and po licy changes. 305 -Investigating how changes in markets, technological advancements, and policy frameworks can impact soil -related adaptatio n strategies. 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T o increase the efficiency of the system a nd to reduce cost of the system, PV pan els must be o perated at the maximum power poin t. In this study, modeling and simulation studies of the fuzzy logic MPPT method were carried ou t to increase the system efficiency by operating the PV panel fed DC/DC boost converter at the maximum power point under variable temperature and irradi ation. Modeling, simulation and verification of the me thod used were carried out in the MATLA B/Simulink program. The simulated circuit consists o f PV pan el system, DC/DC boost converter, fuzzy logic control block and measurement blocks. Solar irradiation intensity was applied to the panel input as 600W/m 2 , 800W/m 2 and 10 00W/m 2 , and the ambient temperature was 25 °C. While 380V constant voltage is obtained at the PV panel ou tput, 550V, 62 0V and 700V are obtained respectively at the boost converter output . Throughout the simulation, system effi ciency was achi eved at 94.5% and abo ve. The results obt ained show that the photovoltaic system with the fuzzy logic MPPT method monitors the maximum power point with high efficiency in changing environmental conditions. Keywords : MPPT method , PV system, Fuzzy logic algorithms, DC/DC boost converters. 1 Doç. Dr.; Bilecik Şeyh Edebali University Elect ric -El ectronic Eng ineering Department, Gulumbe Campus, Bilecik, Turkey, yasemin.on [email protected] , ORC ID ID: 0000 -0003-0173- 0948 311 INTRODUCTION Todays technol ogy is largely dep endent on fossil fuels as an energy source fo r heating, production, transportation and all ot her activities. However, the use of fossil fuels causes an increase in costs due to the decrease in fuels such as oil and natural gas with limited reserves, and causes har mful emissions and negative effects of greenhouse gases on the environment as a result of burning f ossil fu els. Due to the drawbacks of using fo ssil fuels, renewable energy sources such as wind, solar, geothermal an d biomass have begun to be used. Ph otovoltaic (PV) systems, which convert solar energy into electricity and provide environmentally friendly and sustainable energy production, have an important pla ce among renewable energy sou rces. However, achieving the ma ximum power ou tput of PV systems is a challenging process du e to the in fluence of environmental factors such as variable solar irradiation levels and temperature (Benner and Kazmerski, 1999:9). The current and voltage characteristics and the power and voltage characteristics ob tained from the PV panel system have only one maximum power point (MPP). In addition, the location of the MPP changes according to the changing solar ir radiation level, temperature level and environmental conditions such as clouds, rain, snow, dust and humidity. The power inequality between sources and load characteristics restricts the maximum power draw from the PV panel system, cau sing some large power losses. This reduces the efficiency of PV panel systems and increases syst em costs (Hepzibah and Premkumar, 2020 :15). MPP monitoring in PV systems increases efficiency by ensuring that the panel operates at the optimum operating point. Th ere are many traditional MPPT methods in the literature to achieve this point. S ome of these traditional methods are Perturb -and-Observe (P&O) (Jubaer and Zainal , 2015:1 2; Alik and Juso h , 2017:12), hill climbing (Saharia and Saharia, 2016 :9 ), incremental conductance (IC) (Safari and Mekhilef, 2010:8) and incremental resistance metho d (Mei et al ., 2010:8). Traditional methods usually use fixed measurement techniques or some optimized algo rithms. However, these methods are limited in their ability to provide stable perfo rmance under variab le weather con ditions and variable solar radiation, and the system ef ficiency is greatly reduced (Dadfar et al., 2 019:19 ). In order to solve these problems in the literature, ar tificial neural netwo rk (ANN) (Elobaid 2015:21; Fathi and Parian, 2021:11), fuzzy lo gic (FL) (Nabipour et al., 2017:23; Al Nabulsi and Dhaouadi, 2012:12), artificial intelligence-based methods such as neuro-fuzzy (NF) (Hassan et al., 2017:16) and genetic algo rithm (GA) (Joshi and Arora , 2017:24; Had ji et al., 2015:15) hav e been dev eloped (Seyedmahmoudian et al., 2016:21) . The MPPT method usin g a fuzzy neu ral 312 fixed at 25 ° C, the decrea se in irradiance greatly reduces the current of th e PV panel. However, when the irradiance valu e decreases, the PV panel voltage changes very little. PV panel system parameters us ed in the study are given in Table 3.1. (a) (b) Figure 3.3 . (a) Variable ir radiance I-V characteristic, (b) Variable irradiance P - V characteristic, 319 Table 3.1. PV panel syste m parameters Parameters Value Maximum power , P max 3060W Current at point MPP I mpp 24.96A Voltage at point MPP V mpp 122.6V Short circuit current, I sc 26.85A Open circuit voltage, V oc 151.2V I-V and P -V curves fo r different temper ature values a re shown in Figure 3.4 . As can be seen from the fig ure, when the solar irradiation is constant at 1000 W/m 2 and the panel temperature increases, the voltage of th e PV panel decreases. However, when the temperature value increases, the PV panel current changes very little. (a) 320 (b) Figure 3.4. (a) Variable temperature I-V characterist ic, (b) variable temper ature P-V characteristic SYSTEM SIMULAT ION AND RESULTS The simulatio n of the PV DC/DC b oost converter was carried out in th e MATLAB/ simulink environment using the FL MPPT algorith m. The po wer circuit of the PV panel system and DC/D C boost converter is seen in Figure 4.1 . In the first stage of modeling, it is necessary to select the PV panel and determin e the parameters. At this stage, the PV pan el “ So ltec 1STH -215p ” model was selected. The parameters of the panel are shown in Table 4.1 . In order to ob tain the desired voltage level and power from the PV panel system, it must be converted into a module. For this purpose, a total of 24 panels were used, 12 panels in series and 2 panels in parallel. Th e total power of the created panel system is 5115.6 W, current is 15.68 A and voltage is 4 35.6 V. Table 4.1 . PV panel para meters used in DC/DC boost converter Panel ID MPP P mpp (W) I sc (A) V oc (V) MPP I mpp (A) MPP V mpp (V) Soltec 1STH-215p 213.15 7.84 36.3 7.35 29 321 Figure 4.1 . PV panel system and DC/D C boost converter power circuit By connecting a capacitor parallel to the PV panel sy stem output, the vol tage produced in the PV panel is transferred to the capacito r. The voltage on the inpu t capacitor is amplified at the DC/DC boost converter output and transferred to the output capacitor and th e load. The PWM switching signal of the IGBT used in the boost converter is produced at the output of the FL control circuit and the DC voltage is increased at the outp ut of the boost converter. Curr ent and voltage information of the PV panel was used f or th e FL control circuit. The power is calculated and its previous value is subtracted from t he current valu e. Then, th e error signal was produce d by subtracting th e previous value from the current value and dividing it. Error and error change were applied as input to th e FL block and comparison was made according to the fuzzy logic rules seen in Table 4. 2. The signal obtained at the output of t he FL block was used to gener ate the PWM signal. Table 4.2 . Fuzzy logic rule table 322 Figure 4.2 shows FL control and measurement block s. Her e, FL block was created to obtain the duty ratio and D C/ DC PWM block was used to obtain PWM signals. Th e op timum load poin t required to operate the PV pan el in MP P un der the environmental conditions must be found, it must be operated at this load point and the active switch in the boost converter must be triggered at this angle valu e. Solar irradiation applied to th e system, temperature, PV panel curren t I PV and voltage V PV , boost converter ou tput current I out and voltage V out , P V panel ideal power P id eal , PV panel po wer P P V and bo ost converter po wer P out are obtained using the measurement block, Figure 4.2 . FL control and measu rement blocks of the PV fed DC/DC bo ost converter Current and voltage signals were obtained at the PV panel output and boost converter output from th e MATLAB simulatio n for different irradiance an d constant temperature values . Figure 4.3 shows the irradi ation and temperatur e signal shapes. Solar irradiation was chan ged to 600 W/m 2 at 0s, 80 0 W/m 2 at 0.5s and 1000 W/m 2 at 1 s, and the temperature v alue was kept constant at 25 °C. 323 Figure 4.3 . Different irradiance and con stant temperature signals app lied to the PV panel input Figure 4.4 shows the PV pan el voltage and current sign als, and the current and vo ltage signals obtained at the boost converter output. As can be seen in th e graphics, 380V constant vo ltage is obtained at the PV panel o utput, while 550V, 620V and 700V are obtained at the boost converter outp ut, respectively, depending on the amount of irradiation applied to the panel. Figure 4.4 . PV panel vol tage and current signals, boost conv erter voltage and current signals Figure 4.5, PV panel ideal po wer, PV panel po wer and boost con verter output power signals are given. PV ideal power varies between 3000W, 4000W and 5100W, respectively, depending on different irradiation intensity values. The power obtained from the PV panel and the boost converter power follow the ideal power of th e PV panel thanks to the FL MPPT algo rithm. Additionally, the 0 0.5 1 1.5 0 0.5 1 1.5 0 0.5 1 1.5 0 0.5 1 1.5 0 0.5 1 1.5 0 0.5 1 1.5 0 0.5 1 1.5 0 0.5 1 1.5 0 0.5 1 1.5 0 0.5 1 1.5 0 0.5 1 1.5 0 0.5 1 1.5 324 efficiency for the system was also calculated. Throughout the simulation, the circuit operates at an efficiency of ov er 94.5%. Havin g less fluctuatio n in the signals is a desired situation for the FL con troller, and the desired situation has been achieved. It has been observed that the boost converter works and follows the maximum power point of the FL MPPT method using the FL algorithm. Figure 4.5 . PV panel ideal po wer, PV panel power and boost con verter power signals for different irradiance and constant temperature values RESULTS In th is stud y, in order to operate the PV panel fed DC/DC boost converter at the maximum power point, the fuzzy logi c MPPT method was modeled under three different irradiation severity and simulation studies were carried ou t. Matlab/Simulink was used for modeling and simulating. The responses of the P V panel system under changing irradiance and constant temperature were ob served. The total power of the created panel system is 5115.6 W, current is 15.68 A, and voltage is 435. 6 V. While 38 0V constant voltage is obtained at the PV panel output, 550V, 620V and 700V are obtained respectively at the boost con verter output, depending on th e amount of irradiation app lied to the panel. PV ideal power varies between 3000W, 4000W and 5100W, respectively, depending on different irradiation intensity values. The po wer obtained from the PV panel and the boost converter power follow the ideal power of the PV panel thanks to the FL MPPT algorithm. The MPP detectio n efficiency of the FL MPP T method was obtained as 94.5% and above. It proves that in the presence of changes in solar irradiance, the FL MPPT method performs well and extracts the maximum power from the PV panels. 325 REFERENCES 1. Benner, J. P., and Kazmerski, L. (1999). Photovoltaics gaining greater vi sibility. IEEE Spectr., 29, 3 4- 42. 2. Hepzibah, A., and Premkumar, K. (2020). ANFIS curren t – voltage controlled MPPT algorithm for solar po wered brush less DC motor based water pump. Electrical En gineering , 102 (1), 421-435. 3. Jubaer, A., and Zain al, S. (2015). An improved perturb and observe (P&O) maximum power point tracking (MPPT) algorithm for higher efficiency. Appl. Energy. 150, 9 7 – 108. 4. 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Developme nt of generalized photovoltaic mod el usin g MATL AB/SIMULINK. In Proceedings of the world congress on En gineering and computer science, 1 -6. 23. Tutorial, PSIM. How to Use So lar Module Physical Mo del. Powersim Inc , Accessed on 25 November 2019. 327 Chapter 2 2 Results and Suggestions Regarding Cutting For ces, Surface Rough ness An d T ool W ear In T urning Inconel 718 With Differ ent Cutt ing T ools Abdulla h AL TIN 1 ABSTRACT In th is stud y , to ol life, cuttin g for ces and surface roughness , which are machinability parameters, were taken int o accou nt in evaluatin g the machinability of In con el 71 8 superallo y . In stock remov al experiment s, silicon nitrid e based ceramic (KY 20 00 RNGN, KY 21 00 S NGN), whisk er reinfo rced (Al2O3+SiC w) aluminum oxid e based cera mic ( KY 43 00 RNGN, KY 43 00 SNGN), CV D coated cement ite carbid e (KC 93 5 SCMT , KC 9225 ). SCMT , SECO 56 0 RCMT) and uncoated tungst en carbid e (SECO 88 3 RCMM) cutting tool s were us ed. Th e selec ted parameter s wer e con st ant feed (f=0.20mm/re v .), con stant dept h of cut (d=2 mm ), and dif f erent cutting speeds (V=15 , 30, 45, 60, 75 m/min . fo r carbid es, ceramics). fo r V=150, 20 0, 250, 30 0 m/min.). An evaluation was m ade by takin g int o account th e wea r pattern s on cutting tools and th eir causes , th e cutti ng forces acting when cutting th e ma terial, t he resulting surface roughness values and chip shap es. As a result, op timum machining condi tions fo r both cerami c and carbid e tool s were t ried to be determined for Incon el 71 8 mat erial. In th is stud y , th ree criteria were taken as ba sis in determining th e effect of cutting variables on to ol life . These; 1-T ool wear and tool life 2- Cutting forces and cutting power 3- It is the surface roughn ess or the quality of the processed surface. While evaluating the machinability , the surface quality of the processed material was taken as the main criterion to reveal the perfo rmance of the cutting tool used . For example, if processing is to be done based on surface quality , a better quality surface was formed in the whisker-reinforced alumin um oxide (Al2O3+SiCw) ceramic tool (KYON 4300 SNGN), although the to ol life was shorter , at a cutting speed of 15 0 m/min. On the contrary , in cases where surface quality is con sidered secondary , V=25 0 m/ min. wi th whisker reinforced 1 Prof. Dr . Abdullah AL TIN; Y uzuncu Yıl University , V an V ocational of Higher Schoo l, Mechanical and Metal T echnology Department. V an/Turkey , [email protected] .tr ORCID No:0000 - 0003 -4 372-8272 328 7. Refer ences Richards, N., Aspin wall, D., “Use of ceramic to ols for machining ni ckel -based alloys”, Int. J. Mach. t ools Manuf. , 294, 575-588 (1989). Ezugwu, E. O., W ang, Z. M., “Performance of PVD and CVD coated tools when nickel-based machining Inconel 718 all oy”. IN: N.Narutaki et al. Progress of Cutting and Grinding 1 1 1 , 102 -107 (1996). W ang, Z. M., Ph.D Thesis, South Ba nk University , L ondon, pp78,79(1997). Khamsehzadeh, H., “Behaviour of ceramic cutting tools when machining superalloys”, PhD Thesis, pp125 (1991). Bhattacharya, S. K., Pashby , I. R., Ezugwu, E. O., “Machining of INCO 718 and INCO 901 superalloys with Sic -whisker reinforced Al 2 O 3 composite ceramic tools”, Prod. En g , Osaka, 176-18 1 (1987). Moltreacht, K. H., “T ool failure when turning nickel base high temperatur e alloys”, ASME T echnical Paper series no. 637 , Presented at Ann ual Meeting, Detroit, 1 -31 (April 1964). Ezugwu, E. O., Pashb y , I. R., “High speed milling of nickel -based superalloys”. J.Mater Proc.technol. 3 , 429- 437 (1992). Lee, M., Horne, J. G., T abor , D., “The mechanism of no tch formation at dept of cut line of cer amic tools machining nickel -base superalloys”, Pr oc. 2nd Int Conf , W ear Material s Dearborn, MI, 460 -464 (1979). Shaw , M. C., Thurman, A. L., Ahlgren, H. J., “A plasticity problem impro ving plain strain and plain stress simultaneously: Groove formation in the machining of high temperature alloy s”, T rans. ASME (series B), J. Eng. Ind. , 88-2, 142-146 (1966). Choudhury , I. A., El-Baradie, M. A., “Ma chinability of nickel base super alloys: a general review”, Proc. Advances in Materials and Processing T echnologies AMPT '95 , Du blin, Ireland, vol. III, 1 405-1413 (1 995). Suh, N. P ., “New theories of wear and their implications for tools materials”, W ear , vol. 62, 1-20, Abstract INSPEC/ Abstract -FLUIDEX (198 0). Anon, “Cutting T ool Innovations from Carboloy Systems”, Metal Powder Report No. 39 , 41 1-412 (July 1984). Niemi, R.M., “Integrity prediction”, SME T echnical Paper , Dea rbon, Michigan, pp46 (1971). Bhattacharya, S. K., Jawaid, A., Lewis, M. H., W allbank, J., “W ear me chanism of sialon ceramic tools when machining nickel based materials”, Metals T echno. 10 , 71-74 (Dec. 1983) . Chow , C. B., Liu, Y . H., Miao, H. C., Lo, Z. P ., “Investigation on the cutti ng performance of silicon nitride ceramic too ls” , Int. Conf. on Manu. Eng , Melbourne, Australia, 71-74 (Aug. 1980). 335 Reckling, K. S., “New cutting tool tames tough metals”, T ooling Prod. , 47, 74- 79 (1981). Baker , R. D., “High-velocity cutting tools: Application guid elines”, Proc . Biennial Int. Mach. T ool T ech. Con , McLean, V A, 487-52 9 (Sept 1982). Ezugwu, E. O., Machado, A. R., Pashby , I. R., W allbank , J., “The e f fect of high - pressure coolant supply”. Lub. Eng. , 47 9, 751-757 (1990). Kramer , B. M. , Hartun g, P . D., Proc. Int. Con f. Of Cutting T ool Mat , Fort Mitchell, K,Y , 57-74 (1980). Focke, A. E., W estermann, F . E., Eemi, A., Y avelak, J., Hoch, M. , “Failure mechanism of sup erhard materials wh en cutting superalloys”, Proc. 4th Int.-Am.Conf. , China, A 268-296 (April 1991). Al -T or nachi, M. J. K., Dugdale, D. S., Proc. 18th MTD R Con f , 523- 528 (1977). Itakura, M., Kuro da, H., Omokawa, H ., Itani, K., Y amamoto,Y ., Ariura, “W e ar mechanism of coated cemented carpide tool in coated in cutting of Inconel 718 super heat resisting alloy ”, International Jo urnal of Japanese Society for Precision Engineering 334, 326-333 (December 1999). Prengel, H. G., Jindal., P . C., W endt, K. H., Santhanam, A. T ., Hedge, P . L., Penich, R.M., “A new class of high performance PVD c oatings for carbide cutting tools”. Surface and Co atings T echnolog y 139, 25-34 (2001). 336 Chapter 2 3 Contact Mechanics of Functionall y Graded Orthotropic Materials : Semi-Analytical Solution for Rigid Punch Loading E rdal ÖNE R 1 Ahme d Wasfi Hasan A L-QADO 2 ABSTRACT Contact mechani cs has consistently been a significant field of study in the realm of elasticity theory, since it has been utilized to address a diverse range of engineering problems. Due to the fact that changing the gradient of material characteristi cs permits to alte r contact stresses and , consequently, to minimize surface-related damages, contact mechanics analysis of functionally graded materials (FGMs) is of major relevance. This study focused on handling t he continuous contact problem of a fu nctionall y graded (FG) orthot ropic layer th at is in contact with a rigid found ation. The analy sis was conducted using the principles of linear elasticity th eory. The solution incorporates the considerat ion of the body force acting on the layer. In order to apply normal concentr ated load to the FG orthotro pic layer, a rig id cylindrical punch was used. Over the course of the thickn ess of the FG orthotropic layer, it was presumed that the elastic stiffnes s constants exhibited an expon ential variation. Th e Gauss – Chebysh ev integratio n formulas are employ ed to achieve the numerical solutio n for the singular integral equation. Th e main goal of this stud y is to examine the in fluence of several factors, such as punch radius, indentation load, and the inhomogeneity parameter of the FG orthot ropic layer, on both contact stress and contact length. Keywords – Contact mechanics, functio nally graded materials, orthotropic layer, rigid founda tion, theory of elasticity INTRODUCTION 1 Assoc. Prof. ; Bayb urt University Faculty of Engin eering, Departmen t of Civil Eng ineering . eoner@baybu rt.edu.tr ORCID No: 0000 -0001-7492-3754 2 Graduate student ; Bayburt University Faculty of Engineering, Department of Civil Eng ineering . [email protected] ORCID No: 0000 - 0002 - 4609 -5047 337 Contact problems have remained a pivotal area in engineering f or ov er 150 years. In 1882, Hertz initiated a new era in the realm of contact mechanics. Engineering disciplines deriv e advantages from un derstanding the contact leng ths and stress distributions of materials, since it facilitates the production of materials with more ease and reliability. Contact mechanics found use in many technical con texts, in cluding highways, braking disks, airport superstructures, trains, foundations, grain silos, fuel tanks , and clutches. Functionally graded materials (FGMs) are compo site materials consisting of two or more con stituent ph ases, characterized by continuous and smooth spatial gradients in both composition and microstructure. Because of their exceptio nal thermal, mechanical, optical, and electric al capabilities, FGMs are now extensively utilized in a variety of technical applications. These include tribology, nanotechnolo gy, thermal barrier coatings, and biomechanics. In the existing body of literature, numerous studies have been conducted to explore the behavio r of FGMs in contact mechanics scenario s. These investigations have employed diverse solu tion method s, geometric conditions, variations in loading, and material distributions. Singh et al. (2007:155) examined the dynamic response of FG piezoelectric materials subjected to both anti -plane mechanical loading and in -plane electrical loadin g. Barik et al. (200 8:775) explored the static plane contact between FG heat-con ducting punch and a ri gid insulated half -space. Choi (2009:27 03 ) investigated the contact mechanic s invo lving a FG layer that experiences loading from a fl at punch with frictional sliding. Shahzamanian et al. (2010:1591) conducted an analysis of the thermoelastic contact prob lem associated with a rotating brake disk made of FG material. The study considered the presence of a heat source in duced by contact friction. Trubchik et al. (201 1:1754) studied the contact problem associated with th e layer, examining instances where the elastic prop erties of the medium vary as arbitra ry continuously differentiab le funct ions of its thickness. Volkov et al. (2013:1 96 ) investigated a contact problem within the theory of elasticity, specifically addressing the penetration of a circular indenter with a flat base into a compliant FG elastic layer. Nikb akht et al. (2014:92) conducted a study on the elastic contact i nvolving a FG plate of finite dimensions, characterized by a continuous variation of material properties, and subjected to the indentation of a rigid spherical indenter. Çömez (201 5:339) examined a contact problem inv olving the motion of a rigid cylindrical pu nch and a FG la yer. Adıyaman et al. (201 6:1753) explored the scenario of a frictionless receding contact in the plane problem, 338 focusing on an elastic FG layer pressed against two ho mogeneou s qu arter planes. Güler et al. (20 17:12 ) studied the frictional contact problem in the plane, focusing on a cylindrical punch interacting with a FG orthotropic medium. Polat et al. (2018:3565) solved the con tinuous contact pr oblem of a FG layer po sitioned on an semi-infinite plane, subjected to loadin g from two distinct blocks. Balci and Dag (2019:267) introduced an analytical method designed fo r exploring the dynamic frictional contact mechanics between a FG coating and a moving cylin drical punch. Öner and Birinci (2020:2799) explored the discontin uous contact problem involvi ng a FG layer lo aded by a rigid block. Çömez and Omurtag (2021:3937 ) focused on the frictionless plane contact pr oblem between a rig id punch and a FG orthotropic layer situated on a Pasternak foundation within the bounds of linear elasticity theory. Karabulut and Çömez (2023:e202200427) investigated the scenario s of continuous and discontinuous contact in a FG orthotropic laye r, positioned over a homogeneou s and isotropic layer. In this study, the continuous co nt act problem of a FG orthotropic layer resting on a rigid foundation was examined using elasticity theory , while considering the body force exerted by th e functionally gr aded orthotropi c layer. ANALYTICAL FORMU LATION OF THE CONTACT P ROBLEM Figure 1 depicts the schematics addressing the considered problem. The orthotropic layer has a thickness denoted by h . The orthotropic layer is considered to have functional gradin g as part of the assumptio n. The layer is subjected to a no rmal force, represented as P , applied th rough a rig id cylindrical-profile pu nch. Contact between the punch and th e layer occurs within the interval (-a, +a) . Figure 1: The problem's geometric conf iguration and loading condition 339 In Fig. 1, the elastic stiffness constants C ij (z) exhibit exponential variation through the layer's thickness, characterized as fo llo ws: ( 1) where the inho mogeneity parameter, den oted as β , is featured in the context. The stiffness con stants at the bottom surfac e of the FG layer ar e denoted by C ij0 . The boundary conditions governing the con tinuous contact problem presented in Fig. 1 can be expressed in the follo wing manner: ( 2) ( 3) ( 4) ( 5) where the contact length is indicated by a and the function P(x) represents the contact stress und er the punch. The boundary conditions (2-5) lead to the derivation of unknown functions in integral form, expressed in terms of the contact stres s function P(x) . By utilizing the displacement deriv ative condition associated with the punch profile, the problem is transformed into a singul ar integral equation, expressed as follows: ( 6) where R denot es the punch radiu s. By applying the aforemention ed Eq . (6) and conducting the necessary asymptotic analyses, the singular integral equation (SIE) is expressed in the following form: ( 7) In the singular integral equation (7), the contact length a remains unknown a prio ri. A complete solu tion requires the function p(  ) to satisfy the following equilibriu m condition. ( 8) Following the essential n ormalizations and con sidering that the contact stresses at the ends of th e con tact area are zero, the in dex of th e integral is 340 set to - 1 (Erdog an et al., 1973 :368). Subsequent in termediate operations lead to the reduction of the integral equation and the equilib rium conditi on into the following system of algebraic equati ons: ( 9) ( 10) where (1 1a) (1 1b) (1 1c) The N/2+1 th equation in Eq. (9) is sati sfied aut omatically and it is extracted from Eq. (9). Therefore, Eq s. (9) and (10) togeth er provide N + 1 equations for determining the N +1 unknown s. Due to the nonlinearity in the system of equations regarding contact length, it is necessary to employ an it erative procedure for determining the unknown contact lengt h. In the iterative algo rithm, an initial value for contact len gth is chosen, and N unknowns are obtained from Eq. (9). Subsequently, the equat ion extracted in (9) and the equilibrium condition (10) are validated. If the targeted level of accuracy is not achieved, new values for the contact length are selected. The loop continues until the contact length meets the desired accuracy. RESULTS AND DIS CUSSION In this section, we present t he nu merical finding s pertaining to the scenario illustrated in Fig . 1, where a rigid cylindrical punch interacts with an orth otropic layer composed of functionally gr aded (FG) materials. The mechanical characteristi cs of the orthotropic materials e mployed in this study are detailed in (Binienda and Pindera, 1994 :119) . Fig. 2 illustrates variations in contact length resulting from changes in both punch radius and indentatio n load. Upo n closer inspection of the figure, 341 it becomes evident that a larger punch radius results in the formation of a correspondingly larger contact surface with the FG orthotropic layer. Consequently, this leads to an augmentation in the contact length in this particular scenario. Another in sight gl eaned from the figure is that an es calation in the inden tation load facilitates deeper penetratio n of the punch into the FG orthotropic layer, consequently leading to an increase in contact length. Fig. 3 shows the effect of variation in th e inhomogeneity parameter on contact length. As the inhomogeneity parameter for the functionally graded layer increases, indicating a gradual increase in rigidity from the bottom to the top surface of the ort hotropic layer, the con sequence is a redu ction in contact l ength. Physically, the reduced penetrati on of the pu nch on a stiffer surface aligns with the ob served outcome. Figure 2: Effect of p unch radius and indentation lo ad on contact length (graphite/epoxy (T300/934) , =2, h=1, β=0.5 ) 342 Figure 3: Effect of in homogeneity parameter on contact leng th (boron/aluminum (B/Al), =2, h=1, (P/h)/C 550 =0.005) Figs. 4 -6 depict alterations in the distribution of contact str ess under the punch across vario us dimensio nless paramet ers. Upon examination of these figures, it becomes evident that th e highest stress is concentrated along th e axis of symmetry, reaching zero at th e end of the contact region. Fig. 4 illustrates the variations in contact stress distribution under the punch resulting from changes in punch radiu s. Clearly discernible fro m the figure is the direct relationship between an increase in punch radiu s and the corresponding increase in con tact length. This exp anded contact area leads to a dispersio n of the load over a wider region, consequently causing a reduction in the peak values o f contact stresses. In Fig. 5, the effect of variations in indentation load on contact stress distribution under the punch is demonstrated. As antic ipated, the peak values of stresses exhib it an increase with increase in pun ch indentation load. 343 Figure 4: Effect of pun ch radius on contact stress dist ribution (graphite/epoxy (T300/934) , =2, h=1, β=0.5, (P/h )/C 550 =9x10 -3 ) In Fig. 6, the effect of variations in the inhomogeneity parameter of the FG orthot ropic layer on contact stress distrib ution under the punch is illustrated. The figure demonstrates th at an increase in the inhomogeneity parameter, signifying enhanced stiffness from th e bottom to the top surface, results in a corresponding increase in th e peak values of contact stresses. Figure 5: Effect of in dentation load on contact stress distrib ution (graphite/epoxy (T300/934) , =2 , h=1, β=0.5, R/h=80 ) 344 compared to other algorithms. The flowchart of the PoW consensus algorithm is provided in Fig. 1. Fig. 1 PoW Consensus Algor ithm flowchart PoS is a consensus algorithm that add resses the energy consumptio n and computational requirements of PoW. Instead of solv ing NONCE pu zzles, PoS assigns block validation rights based on the number of tokens held by validators. Validators with a higher stake ha ve a gr eater chance of being selected to verify transactions and create new block s. The flowchart of the PoS consensus algorithm is presented in Fig. 2 . 351 [Document text truncated for crawler view.]