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One approach to adaptive control of a tubular chemical reactor

Dostál, Petr,Bobál, Vladimír,Vojtěšek, Jiří,Babík, Zdeněk

Abstract

The paper deals with continuous-time adaptive control of a tubular chemical reactor with the countercurrent cooling as a nonlinear single input - single output process. The mean reactant temperature and the output reactant temperature are chosen as the controlled outputs, and, the coolant flow rate as the control input. The nonlinear model of the reactor is approximated by an external linear model with a structure chosen on the basis of controlled outputs step responses. Its parameters are estimated via corresponding delta model. The control system structure with two feedback controllers is considered. The resulting controllers are derived using polynomial approach. The method is tested on a mathematical model of the tubular chemical reactor.

Full text

One App oach o Adap i e Con ol o a Tubula Chemical Reac o PETR DOSTÁL, VLADIMÍR BOBÁL, JIŘÍ VOJTĚŠEK, and ZDENĚK BABÍK Tomas Ba a Uni e si y in Zlin Depa men o P ocess Con ol, Cen e o Polyme Sys ems nam. T.G. Masa yka 5555, 760 01 Zlin CZECH REPUBLIC {dos alp, bobal, oj esek, babik}@ ai.u b.cz h p://www. ai.u b.cz/ Abs ac : – The pape deals wi h con inuous- ime adap i e con ol o a ubula chemical eac o wi h he coun e cu en cooling as a nonlinea single inpu – single ou pu p ocess. The mean eac an empe a u e and he ou pu eac an empe a u e a e chosen as he con olled ou pu s, and, he coolan low a e as he con ol inpu . The nonlinea model o he eac o is app oxima ed by an ex e nal linea model wi h a s uc u e chosen on he basis o con olled ou pu s s ep esponses. I s pa ame e s a e es ima ed ia co esponding del a model. The con ol sys em s uc u e wi h wo eedback con olle s is conside ed. The esul ing con olle s a e de i ed using polynomial app oach. The me hod is es ed on a ma hema ical model o he ubula chemical eac o . Key-Wo ds: – Nonlinea sys em, ubula chemical eac o , app oxima e linea model, pa ame e iden i ica ion, polynomial app oach, pole assignmen . 1 In oduc ion Tubula chemical eac o a e uni s equen ly used in chemical indus y. F om he sys em heo y poin o iew, ubula chemical eac o s belong o a class o nonlinea dis ibu ed pa ame e sys ems wi h ma hema ical models desc ibed by se s o nonlinea pa ial di e en ial equa ions (NPDRs). The me hods o modelling and simula ion o such p ocesses a e desc ibed e.g. in [1] – [5]. I is well known ha he con ol o chemical eac o s, and, ubula eac o s especially, o en ep esen s e y complex p oblem. The con ol p oblems a e due o he p ocess nonlinea i y, i s dis ibu ed na u e, and high sensi i i y o he s a e and ou pu a iables o inpu changes. E iden ly, he p ocess wi h such p ope ies is ha dly con ollable by con en ional con ol me hods, and, i s e ec i e con ol equi es applica ion some o ad anced me hods. He e, a ious e icien me hods may be used as he p edic i e con ol, e.g. [6], [7], [8], he obus con ol, e.g. [9], he uzzy nonlinea con ol, e.g. [10], he model e e ence con ol, e.g. [11], o nonlinea con ol, e.g. [12], [13] and [14]. Some o he s me hods a e desc ibed in [15]. One possible me hod o cope wi h his p oblem is using adap i e s a egies based on an app op ia e choice o a con inuous- ime ex e nal linea model (CT ELM) wi h ecu si ely es ima ed pa ame e s. These pa ame e s a e consequen ly used o pa allel upda ing o con olle ‘s pa ame e s. Some esul s ob ained in his ield we e p esen ed by au ho s o his pape e.g. in [16] and [17]. Fo he CT ELM pa ame e es ima ion, ei he he di ec me hod [18] and [19] o applica ion o an ex e nal del a model wi h he same s uc u e as he CT model can be used. The basics o del a models ha e been desc ibed in e.g. [20] and [21]. Al hough del a models belong in o disc e e models, hey do no ha e such disad an ageous p ope ies connec ed wi h sho ening o a sampling pe iod as disc e e z- models. In addi ion, pa ame e s o del a models can di ec ly be es ima ed om sampled signals. Mo eo e , i can be easily p o ed ha hese pa ame e s con e ge o pa ame e s o CT models o a su icien ly small sampling pe iod (compa ed o he dynamics o he con olled p ocess), as shown in [22]. This pape deals wi h con inuous- ime adap i e con ol o a ubula chemical eac o wi h a coun e cu en cooling as a nonlinea single inpu – single ou pu p ocess. Wi h espec o p ac ical possibili ies o a measu emen and con ol, he mean eac an empe a u e and he ou pu eac an empe a u e a e chosen as he con olled ou pu s, and, he coolan low a e as he con ol inpu . The nonlinea model o he eac o is app oxima ed by a CT ex e nal linea model wi h a s uc u e chosen on he basis o compu ed con olled ou pu s s ep esponses. The pa ame e s o he CT ELM hen a e es ima ed ia co esponding del a model. The con ol s uc u e wi h wo eedback con olle s is conside ed, e.g. [23]. The esul ing con olle s a e de i ed using he polynomial app oach [24] and he pole assignmen me hod (see, e.g. [25]). The me hod WSEAS TRANSACTIONS on FLUID MECHANICS Pe Dos ál, Vladimí Bobál, Jiří Voj ěšek, Zdeněk Babík E-ISSN: 2224-347X 13 Issue 1, Volume 7, Janua y 2012 is es ed on a ma hema ical model o a ubula chemical eac o . 2 Model o he Reac o An ideal plug- low ubula chemical eac o wi h a simple exo he mic consecu i e eac ion 12 kk ABC→→ in he liquid phase and wi h he coun e cu en cooling is conside ed. Hea losses and hea conduc ion along he me al walls o ubes a e assumed o be negligible, bu dynamics o he me al walls o ubes a e signi ican . All densi ies, hea capaci ies, and hea ans e coe icien s a e assumed o be cons an . Unde abo e assump ions, he eac o model can be desc ibed by i e PDRs in he o m 1 AA A cc kc z ∂∂ +=− ∂∂ (1) 12 BB AB cc kckc z ∂∂ +=− ∂∂ (2) 1 1 4() () () w p p TTQ U TT zcdc ρρ ∂∂ += − − ∂∂ (3) [ ] 11 22 21 22 4() ()() ( w w pw cw TdU T T dd c dU T T ρ ∂=−+ ∂− +− (4) 12 2 22 312 4() ()() cc cwc pc TT ndU TT z dnd c ρ ∂∂ −= − ∂∂ − (5) wi h ini ial condi ions (,0) () s AA cz cz=, ( ,0) ( ) s BB cz cz=, ( ,0) ( ) s Tz T z=, (,0) () s ww Tz Tz=, ( ,0) ( ) s cc Tz T z= and bounda y condi ions 0 (0, ) ( ) AA c c =(kmol/m3), 0 (0, ) ( ) BB c c =(kmol/m3), 0 (0, ) ( ) T T =(K), (,) () ccL TL T =(K). He e, is he ime, z is he axial space a iable, c a e concen a ions, T a e empe a u es, a e luid eloci ies, d a e diame e s, ρ a e densi ies, cp a e speci ic hea capaci ies, U a e hea ans e coe icien s, n1 is he numbe o ubes and L is he leng h o ubes. The subsc ip (⋅) s ands o he eac an mix u e, (⋅)w o he me al walls o ubes, (⋅)c o he coolan , and he supe sc ip (⋅)s o s eady-s a e alues. The eac ion a es and hea o eac ions a e nonlinea unc ions exp essed as 0exp j jj E kk R T − ⎛⎞ =⎜⎟ ⎝⎠ , j = 1, 2 (6) 11 2 2 ()() A B QHkcHkc=−Δ +−Δ (7) whe e k0 a e p e-exponen ial ac o s, E a e ac i a ion ene gies, () H −Δ a e in he nega i e conside ed eac ion en alpies, and R is he gas cons an . The luid eloci ies a e calcula ed ia he eac an and coolan low a es as 2 11 4 q nd π = , 22 312 4 () c c q dnd π =− (8) The pa ame e alues wi h co esponden uni s used o simula ions a e gi en in Table 1. Table 1. Used pa ame e alues L = 8 m n1 = 1200 d1 = 0.02 m d2 = 0.024 m d3 = 1 m ρ = 985 kg/m3 cp = 4.05 kJ/kg K ρw = 7800 kg/m3 cpw = 0.71 kJ/kg K ρc = 998 kg/m3 cpc = 4.18 kJ/kg K U1 = 2.8 kJ/m2s K U2 = 2.56 kJ/m2s K k10 = 5.61⋅1016 1/s k20 = 1.128⋅1018 1/s E1/R = 13477 K E2/R = 15290 K (-ΔH 1) = 5.8⋅104 kJ/kmol (-ΔH 2) = 1.8⋅104 kJ/kmol F om he sys em enginee ing poin o iew, ou (,) AA cL c=, ou (,) BB cL c=, ou (,) TL T= and ou (0, ) cc T T= a e he ou pu a iables, and, () q , ( ) c q , 0() A c , 0() T and ( ) cL T a e he inpu a iables. Among hem, o he con ol pu poses, mos ly he coolan low a e can be aken in o accoun as he con ol a iable, whe eas o he inpu s en e ing in o he p ocess can be accep ed as dis u bances. In his pape , he mean eac an empe a u e gi en by 0 1 () (,) L m T Tz dz L =∫ (9) and he eac an ou pu empe a u e ou () T a e conside ed as he con olled ou pu s. 3 Compu a ion Models Fo compu a ion o bo h s eady-s a e and dynamic cha ac e is ics, he ini e di e ences me hod is employed. The p ocedu e is based on subs i u ion o he space in e al 0,zL∈< > by a se o disc e e WSEAS TRANSACTIONS on FLUID MECHANICS Pe Dos ál, Vladimí Bobál, Jiří Voj ěšek, Zdeněk Babík E-ISSN: 2224-347X 14 Issue 1, Volume 7, Janua y 2012 node poin s { } i z o i = 1, … , n , and, subsequen ly, by app oxima ion o de i a i es wi h espec o he space a iable in each node poin by ini e di e ences. Two ypes o ini e di e ences a e applied, ei he he backwa d ini e di e ence 1 (,) ( ,) (,) (,) ( 1,) i ii zz yz yz yz zh yi yi h − = − ∂≈= ∂ −− = (10) o he o wa d ini e di e ence 1 (,)(,) (,) (1,) (,) i ii zz yz yz yz zh yi yi h + = − ∂≈= ∂ +− = . (11) He e, a unc ion ( , )yz is con inuously di e en iable in he in e al 0,L<> , and, hLn= is he disk e iza ion s ep. 3.1 Dynamic model Applying he subs i u ions (10), (11) in (1) – (5) and, omi ing he a gumen in pa en hesis, PDRs (1) – (5) a e app oxima ed by a se o ODRs in he o m [] 01 0 () () () ( 1) AAA dc i bkicibci d =− + + − (12) [] 102 0 () () () () () (1) BAB B dc i kic i b kic i d bc i =−+ + +− (13) 1020 2 () () ( ) () ( 1) () w dT i bQ i b b T i b T i d bT i =−+ +−+ + (14) [][] 34 () () () () () w w cw dT i bTi Ti bTi T i d =−+− (15) 56 5 6 () ()()(1) () ccc w dT m bbTmbTm d bT m =− + + + + + (16) o 1,...,in= and 1mni=−+, and, wi h ini ial condi ions (,0) () s AA ci ci=, (,0) () s BB ci ci=, (,0) () s Ti T i=, (,0) () s ww Ti Ti= and ( ,0) ( ) s cc Ti T i= o 1,...,in=. The bounda y condi ions en e in o Eqs. (12) – (14) and (16) o i = 1 . Now, nonlinea unc ions in Eqs. (12) – (16) ake he disc e e o m 0 () exp () j jj E ki k R Ti − ⎛⎞ =⎜⎟ ⎝⎠ , j = 1, 2 (17) 11 22 () ( ) () () ( ) () () A B Qi H kic i Hkici =−Δ + +−Δ (18) o i = 1, … , n. The pa ame e s b in Eqs. (12) – (16) a e calcula ed om o mulas 0 bh =, 1 1 () p bc ρ =, 1 21 4 () p U bdc ρ =, 11 322 21 4 ()() p w dU bdd c ρ =−, 22 422 21 4 ()() p w dU bdd c ρ =− (19) 5c bh =, 12 2 622 312 4 ()() p c ndU bdnd c ρ =−. He e, he o mulas o compu a ion o Tm and ou T ake he disc e e o m 1 1 () ( ,) n m i i T Tz n= =∑, ou () ( ,) n T Tz = (20) 3.2 S eady-s a e model Compu a ion o he s eady-s a e cha ac e is ics is necessa y no only o a s eady-s a e analysis bu he s eady s a e alues ( ) s yi also cons i u e ini ial condi ions in ODRs (12) – (16) (he e, y p esen s some o he a iable in he se (12) – (16)). The s eady-s a e model can simply be de i ed equa ing he ime de i a i es in (12) – (16) o ze o. Then, a e some algeb aic manipula ions, he s eady-s a e model akes he o m o di e ence equa ions 0 01 () ( 1) () ss AA s b ci ci bki =− + (21) 10 02 1 () () () ( 1) () ssss BAB s ci kici bci bki ⎡ ⎤ =+− ⎣ ⎦ + (22) 10 2 02 1 () () ( 1) () ssss w Ti bQi bTi bTi bb ⎡ ⎤ =+−+ ⎣ ⎦ + (23) 34 34 1 () () () sss w c Ti bTi bTi bb ⎡ ⎤ =+ ⎣ ⎦ + (24) WSEAS TRANSACTIONS on FLUID MECHANICS Pe Dos ál, Vladimí Bobál, Jiří Voj ěšek, Zdeněk Babík E-ISSN: 2224-347X 15 Issue 1, Volume 7, Janua y 2012 56 56 1 () ( 1) () sss ccw Tm bTm bTm bb ⎡⎤ =++ ⎣⎦ + (25) o 1,...,in= and 1mni=−+. Nonlinea unc ions acco dan wi h a s eady-s a e a e 0 () exp () j s jj s E ki k R Ti ⎛⎞ − =⎜⎟ ⎜⎟ ⎝⎠ , j = 1, 2 (26) 11 22 () ( ) () () ( ) () () sss A ss B Qi H kici Hkici =−Δ + +−Δ (27) Now, he o mulas o compu a ion T m and ou T ha e he o m 1 1() n ss m i i TTz n= =∑, ou () ss n TTz= (28) 3.3 S eady-s a e and dynamic cha ac e is ics Typical eac an empe a u e p o iles along he eac o ubes compu ed o 02.85 s A c=, 00 s B c=, 0323 s T=, 0293 s c T= and 0.15 s q= o a ious coolan low a es a e shown in Fig. 1. A p esence o a maximum on he eac an empe a u e p o iles is a common p ope y o many ubula eac o s wi h exo he mic eac ions. 012345678 320 330 340 350 360 Reac an empe a u e (K) z (m) 1 - qs c = 0.2 2 - qs c = 0.25 3 - qs c = 0.3 1 2 3 Fig. 1 Reac an empe a u e p o iles o a ious coolan low a es. A dependences o he eac an mean empe a u e and he eac an ou pu empe a u e on he coolan low a e is shown in Fig. 2. The o m o bo h cu es documen s a nonlinea ela ion be ween supposed con olled ou pu s and he coolan low a e which is conside ed as he con ol inpu . Dynamic cha ak e is ics we e compu ed in he neighbou hood o he chosen ope a ing poin 3 0.27 m /s s c q=, 334.44K s m T=, ou 326.10K s T= Fo he dynamic analysis and subsequen con ol pu poses, he con olled ou pu s a e de ined as 0.20 0.25 0.30 0.35 0.40 310 315 320 325 330 335 340 345 Ts m Ts ou Ts ou = 326.10 Tempe a u es (K) qs c (m3/s) qs c = 0.27 Ts m = 334.44 Fig. 2 Dependence o he eac an mean empe a u e on he coolan low a es. de ia ions om s eady alues 1 2 ou ou ou () () () () () () s mmm s y T T T y T T T =Δ = − =Δ = − . (29) Such o m is equen ly used in he con ol. The de ia ion o he coolan low a e is deno ed as () s cc c qq qΔ= −. (30) The esponses o bo h ou pu s o he coolan low a e s ep changes a e shown in Figs. 3, 4. 0 50 100 150 200 -12 -10 -8 -6 -4 -2 0 2 4 6 8 y1 (K) (s) 1 - Δqc = - 0.05 2 - Δqc = - 0.025 3 - Δqc = 0.025 4 - Δqc = 0.05 1 2 3 4 Fig. 3 Reac an mean empe a u e s ep esponses. 0 50 100 150 200 -10 -8 -6 -4 -2 0 2 4 y2 (K) (s) 1 - Δqc = - 0.05 2 - Δqc = - 0.025 3 - Δqc = 0.025 4 - Δqc = 0.05 1 2 3 4 Fig. 4 Reac an ou pu empe a u e s ep esponses. The abo e shown esponses demons a e mo e exp essi e nonlinea beha iou o he eac an ou pu empe a u e o inpu changes han he eac an mean empe a u e. This ac is e iden also om he gain alues compu ed as WSEAS TRANSACTIONS on FLUID MECHANICS Pe Dos ál, Vladimí Bobál, Jiří Voj ěšek, Zdeněk Babík E-ISSN: 2224-347X 16 Issue 1, Volume 7, Janua y 2012 () lim s c y gq →∞ =Δ (31) and p esen ed in Tab. 2. Tab. 2 Gains o a ious inpu hanges. Δqc - 0.025 - 0.05 0.025 0.05 Main eac an empe a u e gs -155.4 -166.2 -263.5 -205.1 Ou pu eac an empe a u e gs -69.6 -72.0 -194.3 -193.5 This ac p edica es be e p ope ies o he eac an mean empe a u e as he con olled ou pu han he eac an ou pu empe a u e. Mo eo e , he dynamics o he eac an ou pu empe a u e is slowe in compa ison wi h he dynamics o he eac an mean empe a u e. 4 CT and Del a ELM Fo he con ol pu poses, he con ol inpu a iable a e conside ed in he o m () () 10 s cc s c q q u q − = (32) This exp ession enables o ob ain con ol inpu and con olled ou pu a iables o app oxima ely he same magni ude. A choice o he CT ELM s uc u e does no s em om known s uc u e o he model (1) – (5) bu om a cha ac e o simula ed s ep esponses. I is well known ha in adap i e con ol a con olled p ocess o a highe o de can be app oxima ed by a linea model o a lowe o de wi h a iable pa ame e s. Taking in o accoun p o iles o cu es in Figs. 3 and 4 wi h ze o de i a i es in = 0, he second o de CT ELM has been chosen o bo h con olled ou pu s in he o m o he second o de linea di e en ial equa ion 100 () () () ()y ay a y bu ++ =   (33) whe e y = y1 o y = y2 , and, in he complex domain, as he ans e unc ion 0 210 () b Gs s as a =++ . (34) Es ablishing he δ ope a o 0 1q T δ − = (35) whe e q is he o wa d shi ope a o and T0 is he sampling pe iod, he del a ELM co esponding o (33) akes he o m 2100 () () () ()y a y a y bu δδ ′′ ′′′′′ ++= (36) whe e ′is he disc e e ime. When he sampling pe iod is sho ened, he del a ope a o app oaches he de i a i e ope a o , and, he es ima ed pa ame e s ,ab ′′ each he pa ame e s a, b o he CT model (33). 5 Del a Model Pa ame e Es ima ion Subs i u ing 2 k ′=−, equa ion (36) can be ew i en o he o m 210 0 (2) (2) (2) (2) yk a yk a yk buk δδ ′′ −+ −+ −= ′ =− (37) In he pape , he ecu si e iden i ica ion me hod wi h exponen ial and di ec ional o ge ing was used. Es ablishing he eg ession ec o () (1) (2) (2)(2) Tkykykuk δ δ −=− − − − −Φ(38) whe e 0 (1)(2) (2) yk yk yk T δ −− − −= (39) he ec o o del a model pa ame e s () 100 () Tkaab δ ′′′ =Θ (40) is ecu si ely es ima ed om he ARX model 2(2) ()(1)() T yk k k k δδ δε −= −+ΘΦ (41) whe e 2 2 0 () 2( 1) ( 2) (2) yk yk yk yk T δ −−+− −= (42) 6 Con olle Design The con ol sys em wi h wo eedback con olle s is depic ed in Fig. 5. - - e wu u 0 y R CT ELM Q Fig. 5. Con ol sys em wi h wo eedback con olle s In he scheme, w is he e e ence signal, deno es he load dis u bance, e he acking e o , u0 ou pu o con olle s, u he con ol inpu and y he WSEAS TRANSACTIONS on FLUID MECHANICS Pe Dos ál, Vladimí Bobál, Jiří Voj ěšek, Zdeněk Babík E-ISSN: 2224-347X 17 Issue 1, Volume 7, Janua y 2012 con olled ou pu . The ans e unc ion G(s) o he CT ELM is gi en by (34). The e e ence w and he dis u bance a e conside ed as s ep unc ions wi h ans o ms 0 () w Ws s =, 0 () Vs s = (43) The ans e unc ions o bo h con olle s a e in o ms () () () , () () () s qs Rs Qs p sps ==   (44) whe e q , and p  a e cop ime polynomials in s ul illing he condi ion o p ope ness deg deg p≤ and deg deg qp≤ . The con olle design desc ibed in his sec ion appea s om he polynomial app oach. The gene al equi emen s on he con ol sys em a e o mula ed as i s in e nal p ope ness and s ong s abili y (in addi ion o he con ol sys em s abili y, also he con olle s abili y is equi ed), asymp o ic acking o he e e ence and load dis u bance a enua ion. The p ocedu e o de i e admissible con olle s can be pe o med as ollows: T ans o ms o he basic signals in he closed-loop sys em ake ollowing o ms ( o simpli ica ion, he a gumen s is in some equa ions omi ed) [] () () () b Ys Ws pVs d =+  (45) [] 1 () ( ) () () E sapbqWsbpVs d =+ −   (46) [] () () () a Us Ws pVs d =+  (47) He e, [ ] () () () () () ()ds as ps bs s qs=++  (48) is he cha ac e is ic polynomial wi h oo s as poles o he closed-loop. Es ablishing he polynomial as () () () s s qs=+  (49) and subs i u ing (49) in o (48), he condi ion o he con ol sys em s abili y is ensu ed when polynomials p  and a e gi en by a solu ion o he polynomial Diophan ine equa ion () () ()() () asps bs s ds+=  (50) wi h a s able polynomial d on he igh side. Wi h ega d o he ans o ms (43), he asymp o ic acking and load dis u bance a enua ion a e p o ided by di isibili y o bo h e ms ap bq+  and p  in (46) by s. This condi ion is ul illed when polynomials p and q ha e o ms () () p ssps= , ( ) ( ) qs sqs= . (51) Subsequen ly, he ans e unc ions (44) ake o ms () () () qs Qs p s =, () () () s Rs s ps = (52) and, a s able polynomial p(s) in hei denomina o s ensu es he s abili y o con olle s. The con ol sys em sa is ies he condi ion o in e nal p ope ness when he ans e unc ions o all i s componen s a e p ope . Consequen ly, he deg ees o polynomials q and mus ul il hese inequali ies deg deg qp≤, deg deg 1 p≤+. (53) Now, he polynomial can be ew i en o he o m () () () s s sqs=+ . (54) Taking in o accoun he sol abili y o (50) and condi ions (53), he deg ees o polynomials in (50) and (52) can be easily de i ed as deg deg deg a==, deg deg 1qa=−, deg deg 1 p a≥−, deg 2degda≥. (55) Deno ing deg a = n, polynomials , and q ha e o ms 0 () n i i i s s = = ∑ , 0 () n i i i s s = = ∑ , 1 1 () n i i i qs qs− = =∑ (56) and, ela ions among hei coe icien s a e 00 =, iii q += o 1,...,in=. (57) Since by a solu ion o he polynomial equa ion (50) p o ides calcula ion o coe icien s i, unknown coe icien s i and qi can be ob ained by a choice o selec able coe icien s 0,1 i β ∈ such ha iii β =, (1 ) iii q β =− o 1,...,in=. (58) The coe icien s i β dis ibu e a weigh be ween nume a o s o ans e unc ions Q and R. Rema k: I 1 i β = o all i, he con ol sys em in Fig. 5 educes o he 1DOF con ol con igu a ion (Q = 0). I 0 i β = o all i, and, bo h e e ence and load dis u bance a e s ep unc ions, he con ol sys em co esponds o he 2DOF con ol con igu a ion. Fo he second o de model (34) wi h deg 2 a=, he con olle 's ans e unc ions ake speci ic o ms 21 0 2 210 0 () () () () () () ( ) qs qs q Qs ps s p s s s Rs sps s s p + == + ++ == + . (59) whe e 00 =, 111 β =, 222 β =, WSEAS TRANSACTIONS on FLUID MECHANICS Pe Dos ál, Vladimí Bobál, Jiří Voj ěšek, Zdeněk Babík E-ISSN: 2224-347X 18 Issue 1, Volume 7, Janua y 2012 111 (1 )q β =− , 222 (1 )q β =− . (60) The con olle pa ame e s hen esul om a solu ion o he polynomial equa ion (50) and depend upon coe icien s o he polynomial d. The nex p oblem he e is o ind a s able polynomial d ha enables o ob ain accep able s abilizing con olle s. In his pape , he polynomial d wi h oo s de e mining he closed-loop poles is chosen as 2 () ()( )ds ns s α =+ (61) whe e n is a s able polynomial ob ained by spec al ac o iza ion () () () ()asas nsns ∗∗ = (62) and α is he selec able pa ame e . No e ha a choice o d in he o m (61) p o ides he con ol o a good quali y o ape iodic con olled p ocesses. The coe icien s o n hen a e exp essed as 2 00 na=, 2 1100 22nana=+− (63) and, he con olle pa ame e s p0 and can be ob ained om solu ion o he ma ix equa ion 10 00 0 1000 00 00 000 ab ab b ⎛⎞ ⎜⎟ ⎜⎟ ⎜⎟ ⎜⎟ ⎝⎠ × 0 2 1 0 p ⎛⎞ ⎜⎟ ⎜⎟ ⎜⎟ ⎜⎟ ⎝⎠ = 31 20 1 0 da da d d − ⎛⎞ ⎜⎟ − ⎜⎟ ⎜⎟ ⎜⎟ ⎝⎠ (64) whe e 2 31 2 10 22 10100 2, 2 2, dn d nn dnndn αα α αα α =+ = ++ =+ = (65) Now, i ollows om he abo e in oduced p ocedu e ha uning o con olle s can be pe o med by a sui able choice o selec able pa ame e s β and α. The con olle pa ame e s and q can hen be ob ained om (60). The adap i e con ol sys em is shown in Fig. 6. Con olle Pa ame e es ima ion Con olled p ocess Compu a ion o con olle pa ame e s T 0 T 0 w u q, p y b, a - Fig. 6 Adap i e con ol scheme. 7 Con ol Simula ion Also he con ol simula ions we e pe o med in a neighbou hood o he ope a ing poin 3 0.27 m /s s c q=, 334.44K s m T=, ou 326.10K s T=. Fo he s a ( he adap a ion phase), he P con olle wi h a small gain was used in all simula ions. Wi h espec o mo e exp essi e nonlinea i y and slowe dynamics o he eac an ou pu empe a u e in compa ison wi h he eac an mean empe a u e, he changes o e e ences as well as he con ol unning ime in e als we e chosen di e en o bo h ou pu s. The e ec o he pole α on he con olled esponses is anspa en om Figs. 7 and 8. Fo bo h ou pu s, wo alues o α we e selec ed. The con ol simula ions show sensi i i y o con olled ou pu s o α. The highe alues o his pa ame e speed he con ol, howe e , hey p o ide g ea e o e shoo s (unde shoo s). O he he e no men io ed simula ions showed ha a ca eless selec ion o he pa ame e α can lead o con olled ou pu esponses o a poo quali y, o oscilla ions o e en o he con ol ins abili y. 0 100 200 300 400 500 600 700 800 -8 -6 -4 -2 0 2 4 6 y1 (K) (s) 1 - α = 0.075 2 - α = 0.2 1 2 1 2 w Fig. 7 Con olled ou pu y1 esponses: e ec o α (β1 = 1, β2 = 0.5). 0 200 400 600 800 1000 1200 -2 -1 0 1 2 y2 (K) (s) 1 - α = 0.05 2 - α = 0.025 w 1 2 1 21 2 Fig. 8 Con olled ou pu y2 esponses: e ec o α (β1 = 1, β2 = 0). Mo eo e , an inc easing α leads o highe alues and changes o he con ol inpu as shown in Fig. 9 and 10. This ac can be impo an in con ol o eal echnological p ocesses. The con olled ou pu y1 esponse o wo alues β2 is shown in Fig. 11. I can be seen ha an e ec o his pa ame e e is insigni ican . WSEAS TRANSACTIONS on FLUID MECHANICS Pe Dos ál, Vladimí Bobál, Jiří Voj ěšek, Zdeněk Babík E-ISSN: 2224-347X 19 Issue 1, Volume 7, Janua y 2012 0 100 200 300 400 500 600 700 800 0.21 0.22 0.23 0.24 0.25 0.26 0.27 0.28 0.29 0.30 0.31 0.32 0.33 qc (m3/ s) (s) 1 - α = 0.075 2 - α = 0.2 1 1 1 2 2 2 Fig. 9 Coolan low a e esponses in con ol o eac an mean empe a u e – e ec o α (β1 = 1, β2 = 0.5). 0 200 400 600 800 1000 1200 0.22 0.24 0.26 0.28 0.30 qc (m3/ s) (s) 1 - α = 0.05 2 - α = 0.025 1 2 1 2 1 2 Fig. 10 Coolan low a e esponses in con ol o eac an ou pu empe a u e – e ec o α (β1 = 1, β2 = 0). 0 100 200 300 400 500 600 700 800 -6 -4 -2 0 2 4 y1 (K) (s) 1 - β2 = 0 2 - β2 = 1 w 1 2 Fig. 11 Con olled ou pu esponses: e ec o β2 (α = 0.1, β1 = 1). The con olled ou pu esponses documen ing an e ec o he pa ame e β1 a e in Figs. 12 and 13. In bo h cases, a highe alue o β1 esul s in g ea e o e shoo s (unde shoo s) whe eas i s in luence on he speed o con ol is inexp essi e. Co esponding con ol inpu esponses can be seen in Figs. 14 and 15. The e, an inc easing β1 leads o g ea e alues o inpu s, howe e , i can educe occu ed oscila ions, as shown in Fig. 15. O in e es , he e olu ion o es ima ed CT ELM pa ame e s in con ol o he eac an mean empe a u e is shown in Fig. 16. 0 100 200 300 400 500 600 700 800 -8 -6 -4 -2 0 2 4 6 y1 (K) (s) 1 - β1 = 0.2 2 - β1 = 1 w 1 2 1 2 Fig. 12 Con olled ou pu esponses: e ec o β1 (α = 0.15, β2 = 0). 0 200 400 600 800 1000 1200 1400 -2 -1 0 1 2 y2 (K) (s) 1 - β1 = 0 2 - β1 = 1 w 1 1 1 2 2 2 Fig. 13 Con olled ou pu esponses: e ec o β1 (α = 0.04, β2 = 0). 0 100 200 300 400 500 600 700 800 0.22 0.23 0.24 0.25 0.26 0.27 0.28 0.29 0.30 0.31 0.32 qc (m3/ s) (s) 1 - β1 = 0.2 2 - β1 = 1 1 1 1 2 2 2 Fig. 14 Coolan low a e esponses in con ol o eac an mean empe a u e – e ec o β1 (α = 0.15, β2 = 0). 0 200 400 600 800 1000 1200 1400 0.23 0.24 0.25 0.26 0.27 0.28 0.29 0.30 qc (m3/ s) (s) 1 - β1 = 0 2 - β1 = 1 1 11 2 2 2 Fig. 15 Coolan low a e esponses in con ol o eac an ou pu empe a u e – e ec o β1 (α = 0.15, β2 = 0). WSEAS TRANSACTIONS on FLUID MECHANICS Pe Dos ál, Vladimí Bobál, Jiří Voj ěšek, Zdeněk Babík E-ISSN: 2224-347X 20 Issue 1, Volume 7, Janua y 2012 0 100 200 300 400 500 600 700 800 -0.02 0.00 0.02 0.04 0.06 0.08 0.10 0.12 0.14 CT ELM pa ame e s (s) 1 - b0 2 - 10 x a0 3 - 10-1x a1 1 2 3 Fig. 16 CT ELM pa ame e e olu ion (α = 0.15, β1 = 1, β2 = 0). A p esence o an in eg a ing pa in he con olle enables ejec ion o a ious s ep dis u bances en e ing in o he p ocess. As an example, s ep dis u bances a enua ion o he ou pu y1 is p esen ed. S ep dis u bances 3 00.15 kmol/ m A cΔ= , 3 0.03 m /s qΔ=− and 02K TΔ= we e injec ed in o he nonlinea model o he eac o in imes 220s =, 440s = and 640s =. The con olle pa ame e s we e es ima ed only in he i s ( acking) in e al < 200 s. The au ho s' expe iences p o ed ha an u iliza ion o ecu si e iden i ica ion using he del a model a e eaching o a cons an e e ence and in p esence o s ep dis u bances dec eases he con ol quali y. F om his eason, du ing in e al ≥ 200 s, ixed pa ame e s we e used. The con olled ou pu esponses y1 a e shown in Fig. 17. 0 100 200 300 400 500 600 700 800 900 0 1 2 3 4 5 6 7 y1 (K) (s) w Fig. 17 Con olled ou pu in p esence o s ep dis u bances (α = 0.15, β1 = 0.5, β2 = 0). To illus a e an e ec o an addi i e andom dis u bance, he esul o he con olled ou pu y1 simula ion in a p esence o he andom signal 0 () () s A A c c=− is shown in Fig. 18. 8 Conclusions In his pape , one app oach o con inuous- ime adap i e con ol o he mean and ou pu eac an -0.04 -0.02 0.00 0.02 0.04 (kmol/ m3) 0 100 200 300 400 500 600 700 800 -2 -1 0 1 2 3 4 y1 (K) (s) w Fig. 18. Con olled ou pu in he p esence o andom dis u bance in 0 A c (α = 0.15). empe a u es in a ubula chemical eac o was p oposed. The con ol s a egy is based on he p elimina y s eady-s a e and dynamic analysis o he p ocess and on he assump ion o he empe a u e measu emen along he eac o . The p oposed algo i hm employs an al e na i e con inuous- ime ex e nal linea model wi h pa ame e s ob ained h ough ecu si e pa ame e es ima ion o a co esponding del a model. The con ol sys em s uc u e wi h wo eedback con olle s is conside ed. Resul ing con inuous- ime con olle s a e de i ed using he polynomial app oach and gi en by a solu ion o he polynomial Diophan ine equa ion. Tuning o hei pa ame e s is possible ia closed-loop pole assignmen . The p esen ed me hod has been es ed by compu e simula ion on he nonlinea model o he ubula chemical eac o wi h a consecu i e exo he mic eac ion. The simula ion esul s demons a e an applicabili y o he p esen ed con ol s a egy. Acknowledgmen s The au ho s wish o hank o he Minis y o Educa ion o he Czech Republic (MSM7088352101) o inancial suppo . This a icle was c ea ed wi h suppo o Ope a ional P og amme Resea ch and De elopmen o Inno a ions co- unded by he Eu opean Regional De elopmen Fund (ERDF) and na ional budge o Czech Republic wi hin he amewo k o he Cen e o Polyme Sys ems p ojec ( eg.numbe : CZ.1.05/2.1.00/03.0111). WSEAS TRANSACTIONS on FLUID MECHANICS Pe Dos ál, Vladimí Bobál, Jiří Voj ěšek, Zdeněk Babík E-ISSN: 2224-347X 21 Issue 1, Volume 7, Janua y 2012