Nonlinear Model Algorithmic Control of a pH Neutralization Process
Control of pH neutralization processes is challenging in the chemical process industry because of their inherent strong nonlinearity. In this paper, the model algorithmic control (MAC) strategy is extended to nonlinear processes using Hammerstein model that consists of a static nonlinear polynomial...
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Published in | Chinese journal of chemical engineering Vol. 21; no. 4; pp. 395 - 400 |
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Main Author | |
Format | Journal Article |
Language | English |
Published |
Elsevier B.V
01.04.2013
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Online Access | Get full text |
ISSN | 1004-9541 2210-321X |
DOI | 10.1016/S1004-9541(13)60479-6 |
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Abstract | Control of pH neutralization processes is challenging in the chemical process industry because of their inherent strong nonlinearity. In this paper, the model algorithmic control (MAC) strategy is extended to nonlinear processes using Hammerstein model that consists of a static nonlinear polynomial function followed in series by a linear impulse response dynamic element. A new nonlinear Hammerstein MAC algorithm (named NLH-MAC) is presented in detail. The simulation control results of a pH neutralization process show that NLH-MAC gives better control performance than linear MAC and the commonly used industrial nonlinear propotional plus integral plus derivative (PID) controller. Further simulation experiment demonstrates that NLH-MAC not only gives good control response, but also possesses good stability and robustness even with large modeling errors. |
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AbstractList | Control of pH neutralization processes is challenging in the chemical process industry because of their inherent strong nonlinearity. In this paper, the model algorithmic control (MAC) strategy is extended to nonlinear processes using Hammerstein model that consists of a static nonlinear polynomial function followed in series by a linear impulse response dynamic element. A new nonlinear Hammerstein MAC algorithm (named NLH-MAC) is presented in detail. The simulation control results of a pH neutralization process show that NLH-MAC gives better control performance than linear MAC and the commonly used industrial nonlinear propotional plus integral plus derivative (PID) controller. Further simulation experiment demonstrates that NLH-MAC not only gives good control response, but also possesses good stability and robustness even with large modeling errors. Control of pH neutralization processes is challenging in the chemical process industry because of their inherent strong nonlinearity. In this paper, the model algorithmic control (MAC) strategy is extended to nonlinear processes using Hammerstein model that consists of a static nonlinear polynomial function followed in series by a linear impulse response dynamic element. A new nonlinear Hammerstein MAC algorithm (named NLH-MAC) is presented in detail. The simulation control results of a pH neutralization process show that NLH-MAC gives better control performance than linear MAC and the commonly used industrial nonlinear propotional plus integral plus derivative (PID) controller. Further simulation experiment demonstrates that NLH-MAC not only gives good control response, but also possesses good stability and robustness even with large modeling errors. |
Author | 邹志云 于蒙 王志甄 刘兴红 郭宇晴 张风波 郭宁 |
AuthorAffiliation | Research Institute of Pharmaceutical Chemistry, Beijing 102205, China |
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CitedBy_id | crossref_primary_10_1007_s13369_017_2740_7 crossref_primary_10_1016_j_cjche_2024_09_005 crossref_primary_10_1007_s11071_014_1771_9 crossref_primary_10_3390_agriculture12091395 crossref_primary_10_25046_aj020607 crossref_primary_10_3390_agriculture13122176 crossref_primary_10_1016_j_conengprac_2024_106159 crossref_primary_10_1016_j_cjche_2015_10_009 crossref_primary_10_1016_S1004_9541_14_60057_4 crossref_primary_10_1016_j_rineng_2024_103357 crossref_primary_10_1007_s13369_020_04463_0 crossref_primary_10_1016_j_cjche_2014_09_053 crossref_primary_10_1016_j_ijcce_2024_09_004 crossref_primary_10_3390_pr9091506 crossref_primary_10_1016_j_isatra_2022_08_022 crossref_primary_10_3390_agronomy13051423 crossref_primary_10_1016_j_cjche_2015_01_009 crossref_primary_10_1016_j_matcom_2020_11_006 crossref_primary_10_1093_imamat_hxx029 crossref_primary_10_3390_pr10071311 crossref_primary_10_1016_j_cjche_2014_05_013 crossref_primary_10_1109_TSMC_2023_3341031 crossref_primary_10_1016_j_conengprac_2015_09_005 crossref_primary_10_1016_j_eswa_2023_120012 |
Cites_doi | 10.1016/0005-1098(89)90002-2 10.1016/S0098-1354(98)00260-9 10.1016/j.conengprac.2011.09.003 10.1016/j.conengprac.2006.10.016 10.1016/j.compchemeng.2011.04.009 10.1016/j.cej.2010.07.065 10.1016/j.automatica.2008.05.013 10.1016/S0005-1098(01)00292-8 10.1016/j.sysconle.2007.09.009 10.1016/S0098-1354(98)00301-9 10.1016/j.jprocont.2011.08.001 10.1016/S1004-9541(08)60200-1 10.1021/ie000309r 10.1016/S1004-9541(07)60147-5 10.1016/0005-1098(78)90001-8 10.1016/j.compchemeng.2006.10.005 10.1016/S0967-0661(02)00186-7 10.1016/S0959-1524(02)00022-7 10.1016/j.dsp.2010.06.006 10.1007/978-3-0348-8407-5_21 10.1016/S0959-1524(97)80001-B 10.1016/S1004-9541(08)60325-0 10.1016/S1004-9541(08)60305-5 10.1016/j.isatra.2007.12.002 10.1016/j.jpowsour.2008.06.064 |
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Notes | Control of pH neutralization processes is challenging in the chemical process industry because of their inherent strong nonlinearity. In this paper, the model algorithmic control (MAC) strategy is extended to nonlinear processes using Hammerstein model that consists of a static nonlinear polynomial function followed in series by a linear impulse response dynamic element. A new nonlinear Hammerstein MAC algorithm (named NLH-MAC) is presented in detail. The simulation control results of a pH neutralization process show that NLH-MAC gives better control performance than linear MAC and the commonly used industrial nonlinear propotional plus integral plus derivative (PID) controller. Further simulation experiment demonstrates that NLH-MAC not only gives good control response, but also possesses good stability and robustness even with large modeling errors. ZOU Zhiyun , YU Meng, WANG Zhizhen , LIU Xinghong , GUO Yuqing , ZHANG Fengbo , GUO Ning ( Research Institute of Pharmaceutical Chemistry, Beijing 102205, China) 11-3270/TQ model algorithmic control, nonlinear model predictive control, Hammerstein model, pH neutralization process, control simulation ObjectType-Article-2 SourceType-Scholarly Journals-1 ObjectType-Feature-1 content type line 23 ObjectType-Article-1 ObjectType-Feature-2 |
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References | Mehra, R., Rouhai, R., “Model algorithm control: Review and recent developments”, In: Proceedings of Engineering Foundation Conference on Chemical Process Control II, Sea Island, GA, 287–310 (1982). Nejati, Shahrokhi, Mehrabani (bib2) 2012; 22 Vanbeylen, Pintelon, Schoukens (bib27) 2008; 44 Harnischmacher, Marquardt (bib20) 2007; 15 Alvarez, Londono (bib1) 2001; 40 Henson (bib13) 1998; 23 Morari, Lee (bib15) 1999; 23 Huo, Zhu, Hu, Tu, Li, Yang (bib19) 2008; 185 Zou, Z.Y., Liu, G.P., Guo, N., “Predictive control of nonlinear Hammerstein systems and application to pH process”, In: Proceedings of European Control Conference 2003, Cambridge, UK, 166 (2003). Lu, Zhu, Huang, Jiang, Jin (bib7) 2010; 18 Lei, X., Datta, A., “Adaptive model algorithm control”, In: Proceedings of the American Control Conference, Arlington, VA, 4155–4160 (2001). Dolanc, Strmčnik (bib21) 2008; 57 Ding, Liu, Liu (bib28) 2011; 21 Patikirikorala, Wang, Colman, Han (bib18) 2012; 20 Ławryczuk (bib24) 2011; 166 Zhou, Wang, Jin, Zhang (bib11) 2009; 17 Bai (bib26) 2002; 38 Altinten (bib3) 2007; 31 Garcia, Prett, Morari (bib5) 1989; 25 Qin, S., Badgwell, T.A., “An overview of nonlinear model predictive control applications”, In Nonlinear Predictive Control, Allgower, F., Zheng, A., eds, Birkhauser, 369–393 (2000). Manenti (bib16) 2011; 35 Qin, Badgwell (bib6) 2003; 11 Gu, Gupta (bib12) 2008; 47 Fruzzetti, Palazoğlu, McDonald (bib22) 1997; 7 Bao, Pi, Sun (bib4) 2007; 15 Zhao, Su, Gu, Chu (bib8) 2009; 17 Man, Shao (bib23) 2011; 62 Pearson (bib25) 2003; 13 Rault, Richalet, Testud, Papon (bib9) 1978; 14 10.1016/S1004-9541(13)60479-6_bib14 Pearson (10.1016/S1004-9541(13)60479-6_bib25) 2003; 13 10.1016/S1004-9541(13)60479-6_bib17 Lu (10.1016/S1004-9541(13)60479-6_bib7) 2010; 18 Vanbeylen (10.1016/S1004-9541(13)60479-6_bib27) 2008; 44 10.1016/S1004-9541(13)60479-6_bib10 Patikirikorala (10.1016/S1004-9541(13)60479-6_bib18) 2012; 20 Huo (10.1016/S1004-9541(13)60479-6_bib19) 2008; 185 Zhao (10.1016/S1004-9541(13)60479-6_bib8) 2009; 17 Harnischmacher (10.1016/S1004-9541(13)60479-6_bib20) 2007; 15 Manenti (10.1016/S1004-9541(13)60479-6_bib16) 2011; 35 Man (10.1016/S1004-9541(13)60479-6_bib23) 2011; 62 Morari (10.1016/S1004-9541(13)60479-6_bib15) 1999; 23 Fruzzetti (10.1016/S1004-9541(13)60479-6_bib22) 1997; 7 Henson (10.1016/S1004-9541(13)60479-6_bib13) 1998; 23 10.1016/S1004-9541(13)60479-6_bib29 Qin (10.1016/S1004-9541(13)60479-6_bib6) 2003; 11 Ławryczuk (10.1016/S1004-9541(13)60479-6_bib24) 2011; 166 Dolanc (10.1016/S1004-9541(13)60479-6_bib21) 2008; 57 Bao (10.1016/S1004-9541(13)60479-6_bib4) 2007; 15 Ding (10.1016/S1004-9541(13)60479-6_bib28) 2011; 21 Altinten (10.1016/S1004-9541(13)60479-6_bib3) 2007; 31 Gu (10.1016/S1004-9541(13)60479-6_bib12) 2008; 47 Bai (10.1016/S1004-9541(13)60479-6_bib26) 2002; 38 Nejati (10.1016/S1004-9541(13)60479-6_bib2) 2012; 22 Alvarez (10.1016/S1004-9541(13)60479-6_bib1) 2001; 40 Zhou (10.1016/S1004-9541(13)60479-6_bib11) 2009; 17 Garcia (10.1016/S1004-9541(13)60479-6_bib5) 1989; 25 Rault (10.1016/S1004-9541(13)60479-6_bib9) 1978; 14 |
References_xml | – volume: 166 start-page: 269 year: 2011 end-page: 287 ident: bib24 article-title: “On-line set-point optimisation and predictive control using neural Hammerstein models” publication-title: Chemical Engineering Journal – volume: 62 start-page: 2275 year: 2011 end-page: 2280 ident: bib23 article-title: “Neural network predictive control of continuous stirred-tank reactor based on Hammerstein-Wiener model” publication-title: CIESC Journal – volume: 15 start-page: 1238 year: 2007 end-page: 1256 ident: bib20 article-title: “Nonlinear model predictive control of multivariable processes using block-structured models” publication-title: Control Eng. Practice – volume: 38 start-page: 967 year: 2002 end-page: 979 ident: bib26 article-title: “A blind approach to the Hammerstein-Wiener model identification” publication-title: Automatica – volume: 31 start-page: 1199 year: 2007 end-page: 1204 ident: bib3 article-title: “Generalized predictive control applied to a pH neutralization process” publication-title: Comput. Chem. Eng. – volume: 14 start-page: 413 year: 1978 end-page: 428 ident: bib9 article-title: “Model predictive heuristic control: application to industrial processes” publication-title: Automatica – volume: 25 start-page: 335 year: 1989 end-page: 348 ident: bib5 article-title: “Model predictive control: Theory and practice—a survey” publication-title: Automatica – volume: 23 start-page: 187 year: 1998 end-page: 202 ident: bib13 article-title: “Nonlinear model predictive control: current status and future directions” publication-title: Comput. Chem. Eng. – volume: 13 start-page: 1 year: 2003 end-page: 26 ident: bib25 article-title: “Selecting nonlinear model structures for computer control” publication-title: J. Process Control – volume: 17 start-page: 976 year: 2009 end-page: 982 ident: bib11 article-title: “Iterative learning model predictive control for a class of continuous/batch processes” publication-title: Chin. J. Chem. Eng. – reference: Zou, Z.Y., Liu, G.P., Guo, N., “Predictive control of nonlinear Hammerstein systems and application to pH process”, In: Proceedings of European Control Conference 2003, Cambridge, UK, 166 (2003). – volume: 15 start-page: 691 year: 2007 end-page: 697 ident: bib4 article-title: “Nonlinear model predictive control based on support vector machine with multi-kernel” publication-title: Chin. J. Chem. Eng. – volume: 22 start-page: 263 year: 2012 end-page: 271 ident: bib2 article-title: “Comparison between backstepping and input–output linearization techniques for pH process control” publication-title: J. Process Control – volume: 44 start-page: 3139 year: 2008 end-page: 3146 ident: bib27 article-title: “Blind maximum likelihood identification of Hammerstein systems” publication-title: Automatica – volume: 47 start-page: 211 year: 2008 end-page: 216 ident: bib12 article-title: “Control of nonlinear processes by using linear model predictive control algorithms” publication-title: ISA Transactions – volume: 40 start-page: 2467 year: 2001 end-page: 2473 ident: bib1 article-title: “pH neutralization process as a benchmark for testing nonlinear controllers” publication-title: Ind. Eng. Chem. Res. – volume: 11 start-page: 733 year: 2003 end-page: 764 ident: bib6 article-title: “A survey of industrial model predictive control technology” publication-title: Control Eng. Practice – reference: Qin, S., Badgwell, T.A., “An overview of nonlinear model predictive control applications”, In Nonlinear Predictive Control, Allgower, F., Zheng, A., eds, Birkhauser, 369–393 (2000). – volume: 35 start-page: 2491 year: 2011 end-page: 2509 ident: bib16 article-title: “Considerations on nonlinear model predictive control techniques” publication-title: Comput. Chem. Eng. – volume: 20 start-page: 49 year: 2012 end-page: 61 ident: bib18 article-title: “Hammerstein-Wiener nonlinear model based predictive control for relative QoS performance and resource management of software systems” publication-title: Control Eng. Practice – volume: 17 start-page: 241 year: 2009 end-page: 250 ident: bib8 article-title: “A pragmatic approach for assessing the economic performance of model predictive control systems and its industrial application” publication-title: Chin. J. Chem. Eng. – reference: Lei, X., Datta, A., “Adaptive model algorithm control”, In: Proceedings of the American Control Conference, Arlington, VA, 4155–4160 (2001). – volume: 23 start-page: 667 year: 1999 end-page: 682 ident: bib15 article-title: “Model predictive control: Past, present and future” publication-title: Comput. Chem. Eng. – volume: 18 start-page: 66 year: 2010 end-page: 79 ident: bib7 article-title: “A new strategy of integrated control and on-line optimization on high-purity distillation process” publication-title: Chin. J. Chem. Eng. – volume: 185 start-page: 338 year: 2008 end-page: 344 ident: bib19 article-title: “Nonlinear model predictive control of SOFC based on a Hammerstein model” publication-title: Journal of Power Sources – volume: 21 start-page: 215 year: 2011 end-page: 238 ident: bib28 article-title: “Identification methods for Hammerstein nonlinear systems” publication-title: Digital Signal Processing – reference: Mehra, R., Rouhai, R., “Model algorithm control: Review and recent developments”, In: Proceedings of Engineering Foundation Conference on Chemical Process Control II, Sea Island, GA, 287–310 (1982). – volume: 57 start-page: 332 year: 2008 end-page: 339 ident: bib21 article-title: “Design of a nonlinear controller based on a piecewise-linear Hammerstein model” publication-title: Systems & Control Letters – volume: 7 start-page: 31 year: 1997 end-page: 41 ident: bib22 article-title: “Nolinear model predictive control using Hammerstein models” publication-title: J. Process Control – volume: 25 start-page: 335 issue: 3 year: 1989 ident: 10.1016/S1004-9541(13)60479-6_bib5 article-title: “Model predictive control: Theory and practice—a survey” publication-title: Automatica doi: 10.1016/0005-1098(89)90002-2 – volume: 23 start-page: 187 issue: 2 year: 1998 ident: 10.1016/S1004-9541(13)60479-6_bib13 article-title: “Nonlinear model predictive control: current status and future directions” publication-title: Comput. Chem. Eng. doi: 10.1016/S0098-1354(98)00260-9 – volume: 20 start-page: 49 issue: 1 year: 2012 ident: 10.1016/S1004-9541(13)60479-6_bib18 article-title: “Hammerstein-Wiener nonlinear model based predictive control for relative QoS performance and resource management of software systems” publication-title: Control Eng. Practice doi: 10.1016/j.conengprac.2011.09.003 – volume: 15 start-page: 1238 issue: 10 year: 2007 ident: 10.1016/S1004-9541(13)60479-6_bib20 article-title: “Nonlinear model predictive control of multivariable processes using block-structured models” publication-title: Control Eng. Practice doi: 10.1016/j.conengprac.2006.10.016 – volume: 35 start-page: 2491 issue: 11 year: 2011 ident: 10.1016/S1004-9541(13)60479-6_bib16 article-title: “Considerations on nonlinear model predictive control techniques” publication-title: Comput. Chem. Eng. doi: 10.1016/j.compchemeng.2011.04.009 – volume: 166 start-page: 269 issue: 1 year: 2011 ident: 10.1016/S1004-9541(13)60479-6_bib24 article-title: “On-line set-point optimisation and predictive control using neural Hammerstein models” publication-title: Chemical Engineering Journal doi: 10.1016/j.cej.2010.07.065 – volume: 44 start-page: 3139 issue: 12 year: 2008 ident: 10.1016/S1004-9541(13)60479-6_bib27 article-title: “Blind maximum likelihood identification of Hammerstein systems” publication-title: Automatica doi: 10.1016/j.automatica.2008.05.013 – volume: 38 start-page: 967 issue: 6 year: 2002 ident: 10.1016/S1004-9541(13)60479-6_bib26 article-title: “A blind approach to the Hammerstein-Wiener model identification” publication-title: Automatica doi: 10.1016/S0005-1098(01)00292-8 – ident: 10.1016/S1004-9541(13)60479-6_bib29 – volume: 57 start-page: 332 issue: 4 year: 2008 ident: 10.1016/S1004-9541(13)60479-6_bib21 article-title: “Design of a nonlinear controller based on a piecewise-linear Hammerstein model” publication-title: Systems & Control Letters doi: 10.1016/j.sysconle.2007.09.009 – volume: 23 start-page: 667 issue: 4–5 year: 1999 ident: 10.1016/S1004-9541(13)60479-6_bib15 article-title: “Model predictive control: Past, present and future” publication-title: Comput. Chem. Eng. doi: 10.1016/S0098-1354(98)00301-9 – volume: 22 start-page: 263 issue: 1 year: 2012 ident: 10.1016/S1004-9541(13)60479-6_bib2 article-title: “Comparison between backstepping and input–output linearization techniques for pH process control” publication-title: J. Process Control doi: 10.1016/j.jprocont.2011.08.001 – volume: 17 start-page: 241 issue: 2 year: 2009 ident: 10.1016/S1004-9541(13)60479-6_bib8 article-title: “A pragmatic approach for assessing the economic performance of model predictive control systems and its industrial application” publication-title: Chin. J. Chem. Eng. doi: 10.1016/S1004-9541(08)60200-1 – volume: 40 start-page: 2467 year: 2001 ident: 10.1016/S1004-9541(13)60479-6_bib1 article-title: “pH neutralization process as a benchmark for testing nonlinear controllers” publication-title: Ind. Eng. Chem. Res. doi: 10.1021/ie000309r – volume: 62 start-page: 2275 issue: 8 year: 2011 ident: 10.1016/S1004-9541(13)60479-6_bib23 article-title: “Neural network predictive control of continuous stirred-tank reactor based on Hammerstein-Wiener model” publication-title: CIESC Journal – ident: 10.1016/S1004-9541(13)60479-6_bib17 – volume: 15 start-page: 691 issue: 5 year: 2007 ident: 10.1016/S1004-9541(13)60479-6_bib4 article-title: “Nonlinear model predictive control based on support vector machine with multi-kernel” publication-title: Chin. J. Chem. Eng. doi: 10.1016/S1004-9541(07)60147-5 – volume: 14 start-page: 413 issue: 5 year: 1978 ident: 10.1016/S1004-9541(13)60479-6_bib9 article-title: “Model predictive heuristic control: application to industrial processes” publication-title: Automatica doi: 10.1016/0005-1098(78)90001-8 – volume: 31 start-page: 1199 issue: 10 year: 2007 ident: 10.1016/S1004-9541(13)60479-6_bib3 article-title: “Generalized predictive control applied to a pH neutralization process” publication-title: Comput. Chem. Eng. doi: 10.1016/j.compchemeng.2006.10.005 – volume: 11 start-page: 733 issue: 7 year: 2003 ident: 10.1016/S1004-9541(13)60479-6_bib6 article-title: “A survey of industrial model predictive control technology” publication-title: Control Eng. Practice doi: 10.1016/S0967-0661(02)00186-7 – volume: 13 start-page: 1 issue: 1 year: 2003 ident: 10.1016/S1004-9541(13)60479-6_bib25 article-title: “Selecting nonlinear model structures for computer control” publication-title: J. Process Control doi: 10.1016/S0959-1524(02)00022-7 – volume: 21 start-page: 215 issue: 2 year: 2011 ident: 10.1016/S1004-9541(13)60479-6_bib28 article-title: “Identification methods for Hammerstein nonlinear systems” publication-title: Digital Signal Processing doi: 10.1016/j.dsp.2010.06.006 – ident: 10.1016/S1004-9541(13)60479-6_bib14 doi: 10.1007/978-3-0348-8407-5_21 – volume: 7 start-page: 31 issue: 1 year: 1997 ident: 10.1016/S1004-9541(13)60479-6_bib22 article-title: “Nolinear model predictive control using Hammerstein models” publication-title: J. Process Control doi: 10.1016/S0959-1524(97)80001-B – volume: 18 start-page: 66 issue: 1 year: 2010 ident: 10.1016/S1004-9541(13)60479-6_bib7 article-title: “A new strategy of integrated control and on-line optimization on high-purity distillation process” publication-title: Chin. J. Chem. Eng. doi: 10.1016/S1004-9541(08)60325-0 – volume: 17 start-page: 976 issue: 6 year: 2009 ident: 10.1016/S1004-9541(13)60479-6_bib11 article-title: “Iterative learning model predictive control for a class of continuous/batch processes” publication-title: Chin. J. Chem. Eng. doi: 10.1016/S1004-9541(08)60305-5 – volume: 47 start-page: 211 issue: 2 year: 2008 ident: 10.1016/S1004-9541(13)60479-6_bib12 article-title: “Control of nonlinear processes by using linear model predictive control algorithms” publication-title: ISA Transactions doi: 10.1016/j.isatra.2007.12.002 – volume: 185 start-page: 338 issue: 1 year: 2008 ident: 10.1016/S1004-9541(13)60479-6_bib19 article-title: “Nonlinear model predictive control of SOFC based on a Hammerstein model” publication-title: Journal of Power Sources doi: 10.1016/j.jpowsour.2008.06.064 – ident: 10.1016/S1004-9541(13)60479-6_bib10 |
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Snippet | Control of pH neutralization processes is challenging in the chemical process industry because of their inherent strong nonlinearity. In this paper, the model... |
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SubjectTerms | Algorithms Chemical engineering Computer simulation control simulation Derivatives Hammerstein model Hammerstein模型 MAC算法 model algorithmic control nonlinear model predictive control Nonlinearity pH neutralization process pH中和过程 pH值 Robustness Strategy 强非线性 模型算法控制 线性多项式 非线性过程 |
Title | Nonlinear Model Algorithmic Control of a pH Neutralization Process |
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