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Development and Properties of New Mullite Based Refractory Grog

Zemánek, David; Lang, Karel; Tvrdík, Lukáš; Všianský, Dalibor; Nevřivová, Lenka; Štursa, Petr; Kovář, Pavel; Keršnerová, Lucie; Dvořák, Karel

Abstract

The presented study is focused on optimization and characterization of a high-alumina refractory aggregate based on natural raw materials—kaolins, claystone, and mullite dust by-product (used to increase the alumina and mullite contents, respectively). In total, four individual formulas with the Al2O3 contents between 45 and 50 wt.% were designed; the samples were subsequently fired, both in a laboratory oven and an industrial tunnel furnace. The effects of repeated firing were examined during industrial pilot tests. Mineral and chemical compositions and microstructures, of both the raw materials and designed aggregates, were thoroughly investigated by the means of X-ray fluorescence spectroscopy, powder X-ray diffraction, and optical and scanning electron microscopies. Porosity, mineral composition, and mullite crystal-size development during the firing process were also studied. Based on the acquired results, the formula with the perspective to be used as a new mullite grog, featuring similar properties as the available commercial products, however, with reduced production expenses, was selected. The quality of grog determines to a large extent the properties of the final product. Hence, optimization of aggregates for specific refractories is of a great importance. The production of engineered aggregates provides the opportunity to utilize industrial by-products.

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ma e ials A icle De elopmen and P ope ies o New Mulli e Based Re ac o y G og Da id Zemánek 1,2 , Ka el Lang 2, Lukáš T dík2, Dalibo Všianský3, Lenka Ne ˇ i o á1,2, Pe Š u sa 2,3, Pa el Ko ᡠ3, Lucie Ke šne o á3and Ka el D oˇ ák1,*   Ci a ion: Zemánek, D.; Lang, K.; T dík, L.; Všianský, D.; Ne ˇ i o á, L.; Š u sa, P.; Ko ᡠ, P.; Ke šne o á, L.; D oˇ ák, K. De elopmen and P ope ies o New Mulli e Based Re ac o y G og. Ma e ials 2021,14, 779. h ps://doi.o g/10.3390/ma14040779 Academic Edi o : Mangiala di Te esa Recei ed: 21 Decembe 2020 Accep ed: 26 Janua y 2021 Published: 7 Feb ua y 2021 Publishe ’s No e: MDPI s ays neu al wi h ega d o ju isdic ional claims in published maps and ins i u ional a il- ia ions. Copy igh : © 2021 by he au ho s. Licensee MDPI, Basel, Swi ze land. This a icle is an open access a icle dis ibu ed unde he e ms and condi ions o he C ea i e Commons A ibu ion (CC BY) license (h ps:// c ea i ecommons.o g/licenses/by/ 4.0/). 1Facul y o Ci il Enginee ing, B no Uni e si y o Technology, Ve eˇ í331/95, 602 00 B no, Czech Republic; [email p o ec ed].cz (D.Z.); [email p o ec ed].cz (L.N.) 2P-D Re ac o ies CZ JSC, Nád ažní218, 679 63 VelkéOpa o ice, Czech Republic; Ka el.Lang@pd-g oup.com (K.L.); Lukas.T [email p o ec ed] (L.T.); pe [email p o ec ed] (P.Š.) 3Depa men o Geological Sciences, Facul y o Science, Masa yk Uni e si y, Ko lᡠská267/2, 602 00 B no, Czech Republic; [email p o ec ed] (D.V.); Pa el.Ko a @pd-g oup.com (P.K.); Lucie.Ke sne o a@pd-g oup.com (L.K.) *Co espondence: [email p o ec ed].cz; Tel.: +420-54114-7511 (ex . 8067) Abs ac : The p esen ed s udy is ocused on op imiza ion and cha ac e iza ion o a high-alumina e ac o y agg ega e based on na u al aw ma e ials—kaolins, clays one, and mulli e dus by-p oduc (used o inc ease he alumina and mulli e con en s, espec i ely). In o al, ou indi idual o mulas wi h he Al 2 O 3 con en s be ween 45 and 50 w .% we e designed; he samples we e subsequen ly i ed, bo h in a labo a o y o en and an indus ial unnel u nace. The e ec s o epea ed i ing we e examined du ing indus ial pilo es s. Mine al and chemical composi ions and mic os uc u es, o bo h he aw ma e ials and designed agg ega es, we e ho oughly in es iga ed by he means o X- ay luo escence spec oscopy, powde X- ay di ac ion, and op ical and scanning elec on mic oscopies. Po osi y, mine al composi ion, and mulli e c ys al-size de elopmen du ing he i ing p ocess we e also s udied. Based on he acqui ed esul s, he o mula wi h he pe spec i e o be used as a new mulli e g og, ea u ing simila p ope ies as he a ailable comme cial p oduc s, howe e , wi h educed p oduc ion expenses, was selec ed. The quali y o g og de e mines o a la ge ex en he p ope ies o he inal p oduc . Hence, op imiza ion o agg ega es o speci ic e ac o ies is o a g ea impo ance. The p oduc ion o enginee ed agg ega es p o ides he oppo uni y o u ilize indus ial by-p oduc s. Keywo ds: mulli e; e ac o y; high-alumina g og; kaolin; clays one 1. In oduc ion Al hough nume ous scien i ic pape s dealing wi h ce amics and e ac o ies ha e been published, ew au ho s ha e ocused on e ac o y g og so a . Mo eo e , in e ac o ies enginee ing, he esea ch has mos ly been ocused on he ma ix; he a en ion has shi ed o agg ega es only ecen ly [ 1 ]. Agg ega es a e an indispensable pa o e ac o ies, hey enhance he o e all p ope ies, such as olume s abili y du ing i ing and high empe a u e beha iou , and ep esen 50–100% o he aw mix o mos inal p oduc s. The p oduc ion o e ac o ies is, among o he ac o s, con olled by he a ailabili y o g og [ 2 , 3 ]. Enginee ing o agg ega es (i.e., he en i e p oduc ion sys em, including design, cus omiza ion, p ope ies es ing, e alua ion o pe o mance o e ac o y p oduc s, and hei applica ion o desi ed pu poses) is expec ed o b ing new b eak h oughs in e ac o ies echnologies. Design and cus omiza ion o agg ega es comp ise designing o shape, su ace p ope ies, chemical and phase composi ion, as well as op imizing mic os uc u e [ 1 ]. In he pas , e ac o y ma e ials a end-o -li e we e dumped in land ills and new b icks we e made o new aw ma e ials. Such was ing had a huge impac on he en i onmen , especially because o he con inuous mining o aw ma e ials [ 4 , 5 ]. This a i ude has changed no only o ecological, bu also o economic easons [6,7]. Ma e ials 2021,14, 779. h ps://doi.o g/10.3390/ma14040779 h ps://www.mdpi.com/jou nal/ma e ials Ma e ials 2021,14, 779 2 o 15 The gene al si ua ion in he e ac o y indus y has changed signi ican ly du ing he las decades (especially in ecen yea s), which also a ec ed he p oduc ion o i ed clay. Along wi h d op in demand o s anda d i ed clay caused by changes in he s eel manu ac- u ing echnology, he p oduc ion o i ed clays one has dec eased. The eno mous changes wo ldwide we e p ima ily gi en by he es ablishmen o new ecological egula ions in China, exhaus ion o clays one deposi s in Eu ope (e.g., F ance, Poland, Czech Republic), and lack o o he aw ma e ials used o g og p oduc ion, such as magnesi e, bauxi e, and all ypes o aluminium oxides. Limi ed clays one esou ces led o he heap u iliza ion and b ique ing echnology applica ion, bu he esul s o hese app oaches we e unsa is ac o y ega ding shaping and i ing. These we e he impulses beyond he de elopmen o high alumina e ac o y g og [8–10]. Mode n empe a u e-s able componen s ho -p oduced om me allic ma e ials based on elemen s such as i anium [ 11 ], a e-ea h me als [ 12 ], o ungs en [ 13 ] in oduce he necessi y o de elop du able empe a u e- esis an appliances o hei p oduc ion and p ocessing. To esis high empe a u es and main ain he shape and unc ionali y, he in e io o i ually any u nace is made o e ac o y ma e ials, which ha e become sophis- ica ed p oduc s wi h ca e ully designed composi ions. The ce amic indus y cons an ly de elops me hods o lowe he cos and inc ease he quali y and inal p ope ies o he ma e ials [14,15]. Classi ica ion o e ac o ies acco ding o he chemical composi ion is based on he anion: ca ion a io and consis s o h ee ypes o ma e ials: acidic, basic, and neu al. The anion: ca ion a io highe han 1.5:1.0 indica es acidic e ac o y ma e ials, o example SiO 2 con aining one ca ion and wo anions. The neu al a io is equal o 1.5:1.0, o example Al 2 O 3 , and 1.0:1.0 indica es basic e ac o ies, o example MgO. This classi ica ion is widely used in he me allu gic p oduc ion because he e ac o ies ha e o be compa ible wi h alloys p ocessing. Ano he classi ica ion can be, o example, by me hods o ins alla ion— shaped and unshaped, by me hods o manu ac u e— used and sin e ed, and by po osi y con en —po ous and dense [14,16]. Each ype o e ac o y ma e ial, including g og, is applied in di e en indus ial sec- o s gi en by hei cha ac e is ic p ope ies. Aluminosilica e e ac o ies, mulli e ma e ials, and i eclay belong among acidic up o neu al e ac o ies. They a e usually applied in elec ic u naces, coke o ens, annealing u naces, e c. They con ain silica and be ween 40 o 90 w .% o alumina. The dominan aw ma e ials o hese ypes o e ac o ies a e clays [4,14,17]. The inal in e media e phase o he sin e ing p ocess is mulli e. The ea lies syn hesis o mulli e was done by i ing kaolini e. Du ing hea ing o kaolini e, X- ay amo phous me akaolini e is p oduced a i s . Subsequen ly, so called spinel phase and γ -alumina a e o med, and inally, abo e 1000 ◦ C, mulli e and amo phous silica a e p oduced. To a oid he o ma ion o amo phous silica, addi ional alumina has o be added o he ini ial aw ma e ial [ 18 ]. The chemical composi ion o mulli e in e ac o ies is usually close o 3Al 2 O 3· 2SiO 2 , which co esponds o he Al 2 O 3 con en o nea ly 72 w .%. The idealized o mula o he mos commonly p oduced mulli e is 3Al 2 O 3· 2SiO 2 , howe e , he a io o alumina and silica may a y om 2:1 o 3:2. Among he speci ic p ope ies o mulli e a e high he mal esis ance up o 1700 ◦ C in ai a mosphe e, low he mal expansion coe icien 6 × 10 −6 K −1 and conduc ibili y 4–6 W/(m K) a 100–1400 ◦ C, high c eep and co osion esis ance, and, las bu no leas , a ou able physical and mechanical beha iou [ 18 , 19 ]. The i ing p ocess is ealized in sha , unnel, o o a ing kilns a he maximum empe a u e usually no exceeding 1350 ◦ C. In p inciple, a i icial mulli e can be ob ained in wo ways. The majo i y o mulli e in indus ial condi ions is p oduced ia solid-s a e syn hesis by i ing clay, Al 2 SiO 5 mine als (andalusi e, sillimani e, and kyani e), bauxi e, and o he solid aw ma e ials. Ano he way is he sol-gel syn hesis. Solu ion-sol-gel-de i ed mulli es a e cha ac e ized as chemical-mulli es. They a e syn hesized by chemical eac ion, py olysis, and mulli iza ion [ 18 , 20 ]. Each o hese ways o mulli e o ma ion p o ides mulli e wi h di e en p ope ies [16]. Ma e ials 2021,14, 779 3 o 15 The e a e wo ways o indus ial p oduc ion o ma e ials wi h high mulli e con en (abo e ~50% o mulli e): sin e ing (>1500 ◦ C), and using (>1830 ◦ C, in some cases e en >2000 ◦ C). The e m sin e -mulli e e e s o mulli es syn hesized by hea ing o empe a- u es below he mel ing poin ( o c ys allize and densi y he mulli e). Fused-mulli es a e p epa ed by hea ing alumina and silica mix u es o empe a u es abo e he mel ing poin , ollowed by cooling, du ing which mulli es c ys allize. Mulli es p oduced by using ha e highe Al 2 O 3 :SiO 2 a ios han hose p oduced by sin e ing om iden ical ini ial ma e ials. The amoun o alumina in sin e -mulli es usually does no exceed 77 w .% [ 3 , 21 ]. Mulli e con en s in i ed clays o clays ones a e usually below 65 w .% o he whole ma e ial, including he amo phous phase. Ex eme mulli e con en s occu in so called used mul- li es, which may be used as componen s o high alumina g ogs o enhance hei posi i e p ope ies. F om he chemical poin o iew, posi i e pe o mance o mulli e based g og is de e mined by high con en o alumina and low con en s o CaO, MgO, Fe 2 O 3 , and alkalis. The p esence o de imen al elemen s, mainly alkalis, may signi ican ly dec ease he o e all hea a igue esis ance [18,22]. The pape p esen s he enginee ing, cha ac e iza ion, and manu ac u ing possibili ies o new mulli e based agg ega es wi h Al 2 O 3 con en be ween 45 and 50 w .%. The main objec i e o he esea ch is o p esen new agg ega es ea u ing p ope ies simila o hose o comme cially a ailable agg ega es, howe e , his solu ion is much cheape since we use clays one and kaolins mixed wi h used mulli e by-p oduc . 2. Ma e ials and Me hods 2.1. Raw Ma e ials and Mixes Raw mixes wi h he con en s o Al 2 O 3 be ween 45 and 50 w .% we e designed and p e- pa ed in indus ial condi ions (P-D Re ac o ies CZ JSC, VelkéOpa o ice, Czech Republic). To each such high alumina con en s, suppo ing aw ma e ials we e necessa y o be added o he na u al clays one and loa ed kaolins (Tables 1and 2). Fo economic easons, MOTIM Whi e Fused Mulli e p oduced by Elec oco undum L d., Mosonmagya ó á , Hunga y, was chosen (0–1 mm ac ion; see Table 3 o he pa icle size dis ibu ion). MOTIM mulli e is a by-p oduc om mechanical p ocessing o used mulli e blocks designed o glass indus y applica ions. The e o e, i can be conside ed as a seconda y aw ma e ial. The a io o 85% clays one–kaolin and 15% MOTIM mulli e was used o each he Al 2 O 3 con en o a leas 45%. Fo he chemical and phase composi ions o he aw ma e ial see Table 4in he Resul s sec ion. Table 1. Lis o aw ma e ials. Raw Ma e ial Clays one Kaolin Mulli e G og W Supe KN-83 GP3 DS1 MOTIM Si e/ Kaznˇejo si e, Czech Republic/ Kosya in, Uk aine/ Kosya in, Uk aine/ Chlumˇcany si e, Czech Republic/ Elec oco undum L d. P oduce Ke amos company SOKA company SOKA company Sedleckýkaolin, a.s. company Mosonmagya ó á , Hunga y Ma e ials 2021,14, 779 4 o 15 Table 2. Calcula ed chemical composi ions o aw mixes (85% clay, 15% MOTIM mulli e) based on WDXRF analysis in w .%, ounded o wo decimal places. Fo mula Designa ion Raw Ma e ials Al2O3SiO2Fe2O3TiO2CaO MgO K2O Na2O WW supe clays one + MOTIM 48.62 47.51 0.88 1.37 0.37 0.15 0.49 0.25 K KN83 kaolin + MOTIM 49.74 47.82 0.40 1.23 0.30 0.07 0.31 0.14 G GP3 kaolin + MOTIM 48.53 48.86 0.76 0.67 0.26 0.20 2.89 0.10 D DS1 kaolin + MOTIM 45.20 50.19 0.54 0.56 0.32 0.20 0.71 0.38 Table 3. Pa icle size dis ibu ion o MOTIM mulli e, 0–1 ac ion. Sie e Opening [mm] >1 0.5–1.0 0.2–0.5 0.2–0.09 <0.09 w .% 0 44 34.6 15 6.4 Table 4. Chemical and phase composi ion o aw ma e ials in w .%, ounded o wo and one decimal places espec i ely. Raw Ma e ial/Composi ion Clays one Kaolin Mulli e G og W Supe KN-83 GP3 DS1 MOTIM Loss o Igni ion (1000 ◦C) −14.24 −13.47 −13.15 −12.46 Chemical Composi ion Al2O342.15 43.53 42.04 37.93 76.38 SiO253.19 53.57 54.86 56.49 23.40 Al2O3:SiO2 a io 0.79 0.81 0.77 0.67 3.26 Fe2O31.03 0.43 0.87 0.61 0.01 TiO21.68 1.50 0.81 0.68 0.01 CaO 0.38 0.29 0.24 0.12 0.01 MgO 0.17 0.07 0.23 0.24 – K2O 0.85 0.36 0.57 3.53 0.08 Na2O 0.45 0.15 0.28 0.1 0.1 Phase Composi ion and Gene al Fo mula Kaolini e (Al2Si2O5(OH)4) 80.2 93.3 89.7 69.9 – Illi e (K0.65Al2(AlSi3O10)(OH)2) 11.7 4.1 4.7 6.2 – Smec i e (no gene al o mula a ailable) 2.8 – – Ana ase (TiO2) 2.5 0.8 0.7 0.6 – Qua z (SiO2) 2.8 1.8 4.3 10.8 0.1 Feldspa s (K x Na y Ca 1−(x+y) Al 2−(x+y) Si 2+(x+y) O 8 ) - - 0.6 12.5 – Mulli e (Al(4 + 2x)Si(2 −2x)O(10 −x) whe e x = 0.17 o 0.59) – – – – 80.5 Co undum (Al2O3) – – – – 0.2 C is obali e (SiO2) – – – – Amo phous phase NA NA NA NA 19.2 Fo he pilo indus ial expe imen s, p essed b ique es om he aw mixes wi h he app oxima e dimensions o 7 cm × 5 cm × 3 cm we e p epa ed. The b ique ing echnology enables p epa a ion o bodies o op imized sizes and posi i ely impac s educ ion in was ing o aw ma e ials ( he ese es o kaolins and clays ones a e limi ed). Fo labo a o y expe imen s, he mixes we e addi ionally homogenized wi h a wheel mixe o 10 min. Ma e ials 2021,14, 779 5 o 15 Be o e p essing wi h he p essu e o 10 MPa in o cylinde bodies wi h 5 cm in diame e , 10% o wa e was added o he d y mixes. Th ee i ing expe imen s we e used: 1. Fi ing in labo a o y o en—hea ing 10 ◦ C/min o he maximum empe a u es o 1250, 1450, and 1550 ◦C, ollowed by 5 h soaking a he maximum empe a u e 2. One cycle o i ing in indus ial unnel kiln: 1480 ◦C wi h 5 h soaking 3. Two cycles o i ing in an indus ial kiln wi h he egime iden ical as lis ed abo e (ad 2) 2.2. Analy ical Me hods Chemical composi ion analysis o he aw ma e ials was pe o med by wa eleng h- dispe si e X- ay spec oscopy (WDXRF) using SPECTROSCAN MAKC-GV ins umen (Spec on Company, S . Pe e sbu g, Russia) equipped wi h QUANTITATIVE ANALYSIS 4.0 so wa e. Samples we e analysed in o ms o used beads. Powde X- ay di ac ion analysis o he aw ma e ials and enginee ed agg ega es was conduc ed on Panaly ical Empy ean di ac ome e (Mal e n Panaly ical Company, Almelo, The Ne he lands) equipped wi h Cu-anode, 1-D posi ion sensi i e de ec o a con en ion B agg–B en ano e lec ion geome y. The se ing we e s ep size–0.013 2 θ , ime pe s ep— 188 s, and angula ange 5–80 2 θ . Con en s o he amo phous phase we e quan i ied using he addi ion o 10 w .% luo i e (CaF 2 ) as an in e nal s anda d. Quan i a i e phase analysis was done ia he Rie eld me hod using Panaly ical High Sco e 3.0 plus so wa e. Pola izing ligh mic oscopy (PLM) examina ion was pe o med on 30 µ m hick pol- ished hin sec ions using an Olympus BX 51 mic oscope (Olympus Company, Tokyo, Japan). Scanning elec on mic oscopy wi h X- ay mic oanalysis (SEM/EDS) was conduc ed on gold-coa ed mechanically b oken specimens ( o mo phological analyses) and on polished ca bon-coa ed hin sec ions ( o chemical mic oanalyses) using TESCAN MIRA 3 (Tescan Company, B no, Czech Republic) ins umen wi h he accele a ing ol age o 30 kV. De e mina ions o bulk densi y, appa en densi y, appa en po osi y, and wa e ab- so p ion we e done by he well-known hyd os a ic g a i y me hod (e.g., ˇ CSN EN 993-1 s anda d [ 23 ]). Appa en po osi y and po e size dis ibu ion was de e mined by me cu y po osime y using The mo Finnigan POROTEC Pascal 140–240 ins umen (The moFishe Scien i ic, Wal ham, MA, USA). 3. Resul s and Discussion 3.1. Cha ac e iza ion o Raw Ma e ials The alumina con en (be ween 42–44 w .%) and alumina:silica a io (0.77–0.81) was simila o he clays one (W-supe ) and wo o he kaolin samples (KN-83 and GP3). In DS1 kaolin, bo h he pa ame e s we e signi ican ly lowe (37.93 and 0.67%). The Al 2 O 3 :SiO 2 a io in MOTIM mulli e g og (3.26) was much close o he mulli e alue o 2:1 (3.39), han 3:2 (2.54), which co esponds o he p oduc ion by using. The Fe 2 O 3 con en was be ween 1.03 (clays one) and 0.43 (KN-83), while in he MOTIM mulli e i eached only 0.01%. The CaO con en s we e below 0.4% in all he clay and kaolin samples. The con en s o alkalis in all he aw ma e ials we e ela i ely low wi h he excep ion o DS1 kaolin, whe e he con en o K2O eached 3.53%. The con en s o mine als p esen in he aw ma e ials e lec ed hei chemical com- posi ions: he highes kaolini e con en (o e 93%) was iden i ied in he KN-83 sample, and he lowes one (below 70%) in he DS1 kaolin. The mos di e se associa ion o clay mine als was ound he W-supe clays one, whe e, besides kaolini e and illi e, smec i e was also p esen . The highes con en s o “impu i ies”, qua z and eldspa s, we e ound in he DS1 kaolin. The high pe cen age o eldspa s co esponds o he high con en s o po assium in his sample. Chemical and phase composi ions o he used aw ma e ials a e gi en in Table 4. Mo phology o he aw ma e ials was obse ed using SEM. The size o kaolini e pseudohexagonal pla ele s no mal o (0 0 1) was appa en ly he la ges (up o 5 µ m) in Ma e ials 2021,14, 779 6 o 15 he DS1 kaolin, whe e also he c ys al size was he mos uni o m. The smalles kaolini e c ys als (<1 µ m) we e obse ed in W-supe clays one, and GP3 kaolin samples. I can be assumed ha kaolini e c ys al size, i s dis ibu ion and, hence, speci ic su ace may a ec eac i i y. Fo compa ison o mic os uc u es see Appendix A. The SEM obse a ion o MOTIM mulli e (Figu e A5) co esponds o he sie e analysis esul s. The pa icle size o he MOTIM suppo ing aw ma e ial was below 1 mm wi h he mean alue o 0.28 µm (Table 3). 3.2. Tailo ed Agg ega es 3.2.1. Phase Composi ion The bulk phase composi ion, including amo phous (“glassy“) phase, o all he ag- g ega es p epa ed in bo h he labo a o y and indus ial condi ions was analysed by XRD (Table 5, Appendix B). The c is obali e and amo phous phase con en s o well homogenized samples i ed in a labo a o y o en di e ed signi ican ly (Figu e 1). In agg ega e samples K and D, c is obali e did no appea a any o he i ing empe a u es (1250, 1450, and 1550 ◦ C). The con en o he amo phous phase was ela i ely high al eady a 1250 ◦ C and inc eased negligibly wi h inc easing empe a u e. Fo sample D, such a se e e mel ing al eady a lowe empe a u es can be explained by he abundance o po assium in he o mula (2.89%, Table 2). Howe e , o sample K, he chemical composi ion did no p o ide any clea explana ion o he cou se o he mel ing p ocess. In samples W and G, he con en s o he amo phous phase and c is obali e co ela ed nega i ely wi h each o he . C is obali e mel ed below 1450 ◦ C in sample W, and abo e his empe a u e in sample G. Residual qua z in he amoun s abo e 1% emained in samples W and G a 1450 ◦ C. On he o he hand, qua z did no ans o m o c is obali e bu mel ed di ec ly in samples K and D. Ma e ials 2021, 14, x FOR PEER REVIEW 7 o 15 Figu e 1. C is obali e and amo phous phase con en s in labo a o y- i ed samples; no c is obali e was de ec ed in K-L and D-L samples. Figu e 2. Con en s o mulli e in syn he ised samples and e e ence ma e ial; L =l abo a o y i ing, T,TT = one and wo cycles o i ing in indus ial unnel kiln. Table 5. Phase composi ion o p epa ed g og samples (L = labo a o y o en, T = indus ial unnel kiln one i ing cycle, TT = indus- ial unnel kiln wo i ing cycles) and e e ence ma e ial – Re e ence ma e ial. The o mulas wi h simila composi ion as he e e - ence ma e ial a e highligh ed by ed colou . Sample Fi ing Mulli e Co undum C is obali eQua z Amo phous Phase Designa ion Tempe a u e[°C] WL 1250 74.5 0.0 16.1 4.0 5.5 1450 75.6 0.0 7.4 3.8 13.1 1550 71.2 0.0 0.5 0 29.7 W−T 1550 58.5 0.5 20.3 0.9 19.8 W−TT 1550 54.9 0.7 14.6 0.4 29.4 G−L 1250 69.5 0.0 19.6 3.0 7.9 1450 70.7 0.0 24.8 1.0 3.5 1550 71.7 0.0 0.6 0.0 27.7 G−T 1550 56.9 0.1 21.8 0.1 21.1 G−TT 1550 55.9 0.1 23.2 0.0 20.8 K−L 1250 59.1 0.0 0.0 3.9 36.8 1450 57.2 0.0 0.0 0.0 42.8 1550 54.9 0.0 0.0 0.0 45.1 Figu e 1. C is obali e and amo phous phase con en s in labo a o y- i ed samples; no c is obali e was de ec ed in K-L and D-L samples. Ma e ials 2021,14, 779 7 o 15 Table 5. Phase composi ion o p epa ed g og samples (L = labo a o y o en, T = indus ial unnel kiln one i ing cycle, TT = indus ial unnel kiln wo i ing cycles) and e e ence ma e ial–Re e ence ma e ial. The o mulas wi h simila composi ion as he e e ence ma e ial a e highligh ed by ed colou . Sample Fi ing Mulli e Co undum C is obali e Qua z Amo phous Phase Designa ion Tempe a u e [◦C] WL 1250 74.5 0.0 16.1 4.0 5.5 1450 75.6 0.0 7.4 3.8 13.1 1550 71.2 0.0 0.5 0 29.7 W-T 1550 58.5 0.5 20.3 0.9 19.8 W-TT 1550 54.9 0.7 14.6 0.4 29.4 G-L 1250 69.5 0.0 19.6 3.0 7.9 1450 70.7 0.0 24.8 1.0 3.5 1550 71.7 0.0 0.6 0.0 27.7 G-T 1550 56.9 0.1 21.8 0.1 21.1 G-TT 1550 55.9 0.1 23.2 0.0 20.8 K-L 1250 59.1 0.0 0.0 3.9 36.8 1450 57.2 0.0 0.0 0.0 42.8 1550 54.9 0.0 0.0 0.0 45.1 K-T 1550 67.2 0.0 31.1 0.1 1.6 K-TT 1550 66.5 0.0 24.4 0.0 9.1 D-L 1250 56.6 0.0 0.0 4.0 39.4 1450 55.3 0.0 0.0 0.7 44.2 1550 54.9 0.0 0.0 0.6 44.5 D-T 1550 51.2 0.0 1.6 0.0 47.2 D-TT 1550 49.5 0.0 1.8 0.1 48.6 Re e ence Ma e ial 70.1 2.4 21.1 0.3 6.0 Mulli e con en s did no signi ican ly change be ween 1250 and 1550 ◦ C in he labo a o y-p epa ed samples (Figu e 2). In he samples i ed a 1250 ◦ C, bo h he s uc u es o mulli e—close o 3:2 and 2:1—we e p esen . A highe empe a u es, he 3:2 s uc u e became dominan . Based on he mulli e peak p o iles, i is appa en ha he c ys allini y o mulli e inc eased be ween 1250 and 1450 ◦ C. The mulli e peaks’ alues o ull wid h a hal maximum (FWHM) we e signi ican ly highe in he samples i ed a 1250 ◦ C compa ed o hose exposed o highe empe a u es. A e i ing a an indus ial unnel kiln, mulli e con en was simila as in analogous labo a o y-p epa ed sample o sample G. In samples W and D, he acqui ed mulli e con en s we e lowe , and in sample K i was highe (Figu e 2). Mulli e con en s in he indus ial samples can be a ec ed by inhomogenei y o he aw mix. The highe mulli e con en in sample K co ela ed wi h he low amo phous phase con en (below 10%), in compa ison o he same o mula i ed in labo a o y condi ions (o e 36–44%). I may be assumed ha seconda y mulli e o med by c ys alliza ion o he mel du ing slow cooling in he unnel kiln. In all he o mulas, mulli e con en sligh ly dec eased a e he second cycle o indus ial i ing, which may be a ibu ed o co osion by mel . Fi eclay e ac o ies a e usually no exposed o such high empe a u es (1550 ◦ C) du ing hei li ecycle. The common maximum exposi ion empe a u e does no exceed 1400 ◦ C. The e o e, he isk o he occu ence o co osion by mel du ing hei wo king li e ime is limi ed. Ma e ials 2021,14, 779 8 o 15 Ma e ials 2021, 14, x FOR PEER REVIEW 7 o 15 Figu e 1. C is obali e and amo phous phase con en s in labo a o y- i ed samples; no c is obali e was de ec ed in K-L and D-L samples. Figu e 2. Con en s o mulli e in syn he ised samples and e e ence ma e ial; L =l abo a o y i ing, T,TT = one and wo cycles o i ing in indus ial unnel kiln. Table 5. Phase composi ion o p epa ed g og samples (L = labo a o y o en, T = indus ial unnel kiln one i ing cycle, TT = indus- ial unnel kiln wo i ing cycles) and e e ence ma e ial – Re e ence ma e ial. The o mulas wi h simila composi ion as he e e - ence ma e ial a e highligh ed by ed colou . Sample Fi ing Mulli e Co undum C is obali eQua z Amo phous Phase Designa ion Tempe a u e[°C] WL 1250 74.5 0.0 16.1 4.0 5.5 1450 75.6 0.0 7.4 3.8 13.1 1550 71.2 0.0 0.5 0 29.7 W−T 1550 58.5 0.5 20.3 0.9 19.8 W−TT 1550 54.9 0.7 14.6 0.4 29.4 G−L 1250 69.5 0.0 19.6 3.0 7.9 1450 70.7 0.0 24.8 1.0 3.5 1550 71.7 0.0 0.6 0.0 27.7 G−T 1550 56.9 0.1 21.8 0.1 21.1 G−TT 1550 55.9 0.1 23.2 0.0 20.8 K−L 1250 59.1 0.0 0.0 3.9 36.8 1450 57.2 0.0 0.0 0.0 42.8 1550 54.9 0.0 0.0 0.0 45.1 Figu e 2. Con en s o mulli e in syn he ised samples and e e ence ma e ial; L = l abo a o y i ing, T,TT = one and wo cycles o i ing in indus ial unnel kiln. Table 5shows he e ec o he i ing empe a u e on he phase composi ion o labo a o y-p epa ed samples, he compa ison wi h indus ial samples p oduced by one and wo i ing cycles, and he e e ence ma e ial. The phase composi ion o sample K i ed in he indus ial unnel kiln was he closes o he comme cial e ac o y mulli e agg ega e used as he e e ence ma e ial. In labo a o y condi ions, simila composi ion was acqui ed o he sample wi h o mula G (Table 5). The he e ogeneous mic os uc u e o he indus ially p epa ed samples was obse ed by pola izing ligh mic oscopy (PLM). Physical-mechanical p ope ies o he composi e p oduc s a e usually s ongly a ec ed by he in e aces o di e en used ma e ials. Fi ed clay nodules, locally o he size o e 1 cm, we e su ounded by mix u es o well-dispe sed clay binde and MOTIM mulli e pa icles in all he examined samples ( o examples see Figu e 3). The in e aces o hese egions we e ela i ely sha p (Figu e 4) wi h no subs an ial po osi y possibly dec easing he physical-mechanical p ope ies o he samples. G ey colou ing o he nodules nea he in e aces was caused by mig a ion o i on oxides owa ds hei cen al pa s. In some cases, i on oxides o med isola ed ci cula spo s in he i ed clay nodules. The ims o MOTIM mulli e did no exhibi any se e e co osion (Figu e 3). Ma e ials 2021, 14, x FOR PEER REVIEW 8 o 15 K−T 1550 67.2 0.0 31.1 0.1 1.6 K−TT 1550 66.5 0.0 24.4 0.0 9.1 D−L 1250 56.6 0.0 0.0 4.0 39.4 1450 55.3 0.0 0.0 0.7 44.2 1550 54.9 0.0 0.0 0.6 44.5 D−T 1550 51.2 0.0 1.6 0.0 47.2 D−TT 1550 49.5 0.0 1.8 0.1 48.6 Re e ence Ma e ial 70.1 2.4 21.1 0.3 6.0 The he e ogeneous mic os uc u e o he indus ially p epa ed samples was ob- se ed by pola izing ligh mic oscopy (PLM). Physical-mechanical p ope ies o he com- posi e p oduc s a e usually s ongly a ec ed by he in e aces o di e en used ma e ials. Fi ed clay nodules, locally o he size o e 1 cm, we e su ounded by mix u es o well- dispe sed clay binde and MOTIM mulli e pa icles in all he examined samples ( o ex- amples see Figu e 3). The in e aces o hese egions we e ela i ely sha p (Figu e 4) wi h no subs an ial po osi y possibly dec easing he physical-mechanical p ope ies o he samples. G ey colou ing o he nodules nea he in e aces was caused by mig a ion o i on oxides owa ds hei cen al pa s. In some cases, i on oxides o med isola ed ci cula spo s in he i ed clay nodules. The ims o MOTIM mulli e did no exhibi any se e e co osion (Figu e 3). Figu e 3. Sample K-T– i ed clay nodules su ounded by mix u e o i ed clay and mulli e; PPL = plane pola ized ligh , XPL = c ossed pola ized ligh . Figu e 4. Sample G-T–in e ace o la ge, i ed clay nodule and mix u e o i ed clay and agmen s o used mulli e. 3.2.2. Mulli e C ys al Size De elopmen The de elopmen o mulli e c ys als‘ mean size along c c ys allog aphic axis wi h i ing empe a u e (5 h soaking) in he clay pa o he g og was obse ed and calcula ed using SEM (Figu e 5; mulli e was iden i ied by EDS analysis). Simila end was obse ed in all he samples (Table 6). The slowes g owing o mulli e c ys als was obse ed in DS1 kaolin, which was he mos alkali- ich one. Howe e , he alues we e simila o each o he Figu e 3. Sample K-T– i ed clay nodules su ounded by mix u e o i ed clay and mulli e; PPL = plane pola ized ligh , XPL = c ossed pola ized ligh . Ma e ials 2021,14, 779 9 o 15 Ma e ials 2021, 14, x FOR PEER REVIEW 8 o 15 K−T 1550 67.2 0.0 31.1 0.1 1.6 K−TT 1550 66.5 0.0 24.4 0.0 9.1 D−L 1250 56.6 0.0 0.0 4.0 39.4 1450 55.3 0.0 0.0 0.7 44.2 1550 54.9 0.0 0.0 0.6 44.5 D−T 1550 51.2 0.0 1.6 0.0 47.2 D−TT 1550 49.5 0.0 1.8 0.1 48.6 Re e ence Ma e ial 70.1 2.4 21.1 0.3 6.0 The he e ogeneous mic os uc u e o he indus ially p epa ed samples was ob- se ed by pola izing ligh mic oscopy (PLM). Physical-mechanical p ope ies o he com- posi e p oduc s a e usually s ongly a ec ed by he in e aces o di e en used ma e ials. Fi ed clay nodules, locally o he size o e 1 cm, we e su ounded by mix u es o well- dispe sed clay binde and MOTIM mulli e pa icles in all he examined samples ( o ex- amples see Figu e 3). The in e aces o hese egions we e ela i ely sha p (Figu e 4) wi h no subs an ial po osi y possibly dec easing he physical-mechanical p ope ies o he samples. G ey colou ing o he nodules nea he in e aces was caused by mig a ion o i on oxides owa ds hei cen al pa s. In some cases, i on oxides o med isola ed ci cula spo s in he i ed clay nodules. The ims o MOTIM mulli e did no exhibi any se e e co osion (Figu e 3). Figu e 3. Sample K-T– i ed clay nodules su ounded by mix u e o i ed clay and mulli e; PPL = plane pola ized ligh , XPL = c ossed pola ized ligh . Figu e 4. Sample G-T–in e ace o la ge, i ed clay nodule and mix u e o i ed clay and agmen s o used mulli e. 3.2.2. Mulli e C ys al Size De elopmen The de elopmen o mulli e c ys als‘ mean size along c c ys allog aphic axis wi h i ing empe a u e (5 h soaking) in he clay pa o he g og was obse ed and calcula ed using SEM (Figu e 5; mulli e was iden i ied by EDS analysis). Simila end was obse ed in all he samples (Table 6). The slowes g owing o mulli e c ys als was obse ed in DS1 kaolin, which was he mos alkali- ich one. Howe e , he alues we e simila o each o he Figu e 4. Sample G-T–in e ace o la ge, i ed clay nodule and mix u e o i ed clay and agmen s o used mulli e. 3.2.2. Mulli e C ys al Size De elopmen The de elopmen o mulli e c ys als‘ mean size along c c ys allog aphic axis wi h i ing empe a u e (5 h soaking) in he clay pa o he g og was obse ed and calcula ed using SEM (Figu e 5; mulli e was iden i ied by EDS analysis). Simila end was obse ed in all he samples (Table 6). The slowes g owing o mulli e c ys als was obse ed in DS1 kaolin, which was he mos alkali- ich one. Howe e , he alues we e simila o each o he (in compa ison o comme cial samples, o which hey a e app oxima ely by one o de o magni ude la ge ). Ma e ials 2021, 14, x FOR PEER REVIEW 9 o 15 (in compa ison o comme cial samples, o which hey a e app oxima ely by one o de o magni ude la ge ). Figu e 5. Compa ison o mulli e c ys als size in ma ices o K and G samples a e wo cycles o indus ial i ing wi h he e e ence ma e ial ( i ing empe a u e 1480 °C/5h soaking). Table 6. Mean size o mulli e c ys als [μm] on ma ix o labo a o y-p oduced samples, MOTIM mulli e and e e ence ma e ial based on SEM obse a ion. Fi ing Tempe a u e [°C] / Sample 1250 1450 1550 W-L 0.2 0.6 4.0 G-L 0.2 1.0 6.0 K-L 0.5 2.0 10.0 D-L 0.1 0.4 2.0 Comme cial Mulli e Based P oduc s Re e ence Ma e ial 3.0 MOTIM 283.0 3.2.3. Po e Size Analysis The e ec o i ing empe a u e on po e-size dis ibu ion de elopmen in labo a o y- p epa ed samples is shown in Figu es 6 and 7. The o al olume o open po es wi h he diame e s below 1 μm was signi ican ly lowe in all he samples i ed a 1450 °C (in com- pa ison o hose i ed a 1250 °C). The o al olume o small po es also dec eased be ween 1450 and 1550 °C in he G-L and W-L samples. In he K-L and D-L samples, sligh inc ease in open po osi y be ween 1450 and 1550 °C can be obse ed. The labo a o y-p epa ed g og samples based on kaolins ea u ed lowe o al olumes o po es wi h he diame e s be ween 1 and 40 μm han he sample based on clays one (W-L), his po e size o which was dominan . A e i ing a 1250 °C, all he kaolin-based samples displayed simila po e- size dis ibu ions wi h app oxima ely 85 ol.% o po es below 1 μm in diame e . The low- es o al po osi y a e all he i ing egimes was obse ed in D-L sample. The inc ease in he i ing empe a u e om 1250 o 1450 °C led o signi ican clinke ing o K-L and D-L samples, which mani es ed by he dominance o small po es (below 1 μm). Figu e 5. Compa ison o mulli e c ys als size in ma ices o K and G samples a e wo cycles o indus ial i ing wi h he e e ence ma e ial ( i ing empe a u e 1480 ◦C/5h soaking). Table 6. Mean size o mulli e c ys als [ µ m] on ma ix o labo a o y-p oduced samples, MOTIM mulli e and e e ence ma e ial based on SEM obse a ion. Fi ing Tempe a u e [◦C]/Sample 1250 1450 1550 W-L 0.2 0.6 4.0 G-L 0.2 1.0 6.0 K-L 0.5 2.0 10.0 D-L 0.1 0.4 2.0 Comme cial Mulli e Based P oduc s Re e ence Ma e ial 3.0 MOTIM 283.0 3.2.3. Po e Size Analysis The e ec o i ing empe a u e on po e-size dis ibu ion de elopmen in labo a o y- p epa ed samples is shown in Figu es 6and 7. The o al olume o open po es wi h he diame e s below 1 µ m was signi ican ly lowe in all he samples i ed a 1450 ◦ C (in compa ison o hose i ed a 1250 ◦ C). The o al olume o small po es also dec eased