Temperature Control of a Batch Polymerization Reactor
In this work, DMC (Dynamic Matrix Control) of a batch solution polymerization reactor has been investigated experimentally and by simulation to achieve a specific constant number average chain length and conversion in a minimum time. The process variables are reaction temperature and initiator initi...
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| Published in: | Chemical engineering research & design Vol. 77; no. 5; pp. 413 - 420 |
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| Main Authors: | , , , |
| Format: | Journal Article |
| Language: | English |
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Elsevier B.V
01-07-1999
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| Abstract | In this work, DMC (Dynamic Matrix Control) of a batch solution polymerization reactor has been investigated experimentally and by simulation to achieve a specific constant number average chain length and conversion in a minimum time. The process variables are reaction temperature and initiator initiation concentration. The performance of the DMC controller was compared with that of the IMC (Internal Model Control) controller. It was seen that DMC and IMC controllers yielded a good performance in maintaining the reactor temperature at its set point at the isothermal conditions. |
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| AbstractList | In this work, DMC (Dynamic Matrix Control) of a batch solution polymerization reactor has been investigated experimentally and by simulation to achieve a specific constant number average chain length and conversion in a minimum time. The process variables are reaction temperature and initiator initiation concentration. The performance of the DMC controller was compared with that of the IMC (Internal Model Control) controller. It was seen that DMC and IMC controllers yielded a good performance in maintaining the reactor temperature at its set point at the isothermal conditions. Describes an investigation of the application of Dynamic Matrix Control (DMC) of a batch solution polymerization reactor, experimentally and by simulation, to achieve a specific constant average chain length and conversion in a minimum time. The process variables were reaction temperature and initiator initiation concentration. The performance of the DMC controller was compared with that of the Internal Model Control (IMC) controller. Concludes that DMC and IMC controllers yielded a good performance in maintaining the reactor temperature at its set point at the isothermal conditions. (Original abstract - amended) |
| Author | Erdoğan, S. Yüce, S. Hasaltun, A. Alpbaz, M. |
| Author_xml | – sequence: 1 givenname: S. surname: Yüce fullname: Yüce, S. email: scetinka@science.ankara.edn.tr organization: Department of Chemical Engineering, Cumhuriyet University, Sivas, Turkey – sequence: 2 givenname: A. surname: Hasaltun fullname: Hasaltun, A. organization: Department of Chemical Engineering, Gazi University, Ankara, Turkey – sequence: 3 givenname: S. surname: Erdoğan fullname: Erdoğan, S. organization: Department of Chemical Engineering, Gazi University, Ankara, Turkey – sequence: 4 givenname: M. surname: Alpbaz fullname: Alpbaz, M. organization: Department of Chemical Engineering, Ankara University, Ankara, Turkey |
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| CitedBy_id | crossref_primary_10_1016_S0098_1354_03_00073_5 crossref_primary_10_1155_2011_967198 crossref_primary_10_1016_j_cherd_2013_07_032 crossref_primary_10_1016_S0098_1354_01_00651_2 crossref_primary_10_1205_096030801753252315 crossref_primary_10_18038_estubtda_634183 crossref_primary_10_1205_cherd06027 crossref_primary_10_1016_j_cep_2004_04_010 crossref_primary_10_1016_j_jprocont_2019_05_014 |
| Cites_doi | 10.1016/0009-2509(73)85104-8 10.1016/0009-2509(78)80051-7 10.1016/0009-2509(92)80265-E 10.1016/0005-1098(89)90002-2 |
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| Copyright | 1999 The Institution of Chemical Engineers |
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| Keywords | temperature polymerization dynamic matrix control |
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| References | Cutler, C. R. and Ramaker, B. L., 1980, Dynamic matrix control—a computer control algorithm Chen, Jeng (bib5) 1978; 33 Ray (bib6) 1972; 08 Sacks, Lee, Biesenberger (bib4) 1973; 28 Garcia, Prett, Morari (bib2) 1989; 25 Luyben (bib8) 1990 paper WP5. Karagöz, Özkan, Erdoğan, Alpbaz (bib7) 1997; 25 Marlin (bib9) 1995 Seborg, Edgar, Mellichamp (bib10) 1989 Peterson, Hernandez, Arkun, Schork (bib3) 1992; 47 10.1205/026387699526395_bib1 Karagöz (10.1205/026387699526395_bib7) 1997; 25 Chen (10.1205/026387699526395_bib5) 1978; 33 Marlin (10.1205/026387699526395_bib9) 1995 Peterson (10.1205/026387699526395_bib3) 1992; 47 Sacks (10.1205/026387699526395_bib4) 1973; 28 Garcia (10.1205/026387699526395_bib2) 1989; 25 Ray (10.1205/026387699526395_bib6) 1972; 08 Seborg (10.1205/026387699526395_bib10) 1989 Luyben (10.1205/026387699526395_bib8) 1990 |
| References_xml | – year: 1989 ident: bib10 article-title: Process Dynamics and Control contributor: fullname: Mellichamp – volume: 47 start-page: 737 year: 1992 end-page: 753 ident: bib3 article-title: A nonlinear DMC algorithm and its application to a semibatch polymerization reactor publication-title: Chem Eng Sci contributor: fullname: Schork – volume: 25 start-page: 21 year: 1997 ident: bib7 article-title: Modelling, optimization and control of batch polymerization reactor of styrene publication-title: Control and Computer, IASTED contributor: fullname: Alpbaz – year: 1995 ident: bib9 article-title: Process Control: Design Processes and Control System for Dynamic Performance contributor: fullname: Marlin – volume: 33 start-page: 735 year: 1978 end-page: 743 ident: bib5 article-title: Minimum end time policies for batch radical chain polymerization publication-title: Chem Eng Sci contributor: fullname: Jeng – volume: 08 year: 1972 ident: bib6 article-title: On the mathematical modeling of polymerization reactors publication-title: J-Macromolec Sci Revs Macromol Chem contributor: fullname: Ray – year: 1990 ident: bib8 article-title: Process Modeling, Simulation and Control for Chemical Engineers contributor: fullname: Luyben – volume: 25 start-page: 335 year: 1989 end-page: 348 ident: bib2 article-title: Model predictive control theory and practice—a survey publication-title: Automatica contributor: fullname: Morari – volume: 28 start-page: 241 year: 1973 end-page: 257 ident: bib4 article-title: Effect of temperature variation on molecular weight distribution: batch, chain addition polymerization publication-title: Chem Eng Sci contributor: fullname: Biesenberger – volume: 25 start-page: 21 issue: 1 year: 1997 ident: 10.1205/026387699526395_bib7 article-title: Modelling, optimization and control of batch polymerization reactor of styrene publication-title: Control and Computer, IASTED contributor: fullname: Karagöz – year: 1990 ident: 10.1205/026387699526395_bib8 contributor: fullname: Luyben – volume: 28 start-page: 241 year: 1973 ident: 10.1205/026387699526395_bib4 article-title: Effect of temperature variation on molecular weight distribution: batch, chain addition polymerization publication-title: Chem Eng Sci doi: 10.1016/0009-2509(73)85104-8 contributor: fullname: Sacks – volume: 33 start-page: 735 year: 1978 ident: 10.1205/026387699526395_bib5 article-title: Minimum end time policies for batch radical chain polymerization publication-title: Chem Eng Sci doi: 10.1016/0009-2509(78)80051-7 contributor: fullname: Chen – year: 1995 ident: 10.1205/026387699526395_bib9 contributor: fullname: Marlin – volume: 47 start-page: 737 year: 1992 ident: 10.1205/026387699526395_bib3 article-title: A nonlinear DMC algorithm and its application to a semibatch polymerization reactor publication-title: Chem Eng Sci doi: 10.1016/0009-2509(92)80265-E contributor: fullname: Peterson – volume: 25 start-page: 335 year: 1989 ident: 10.1205/026387699526395_bib2 article-title: Model predictive control theory and practice—a survey publication-title: Automatica doi: 10.1016/0005-1098(89)90002-2 contributor: fullname: Garcia – volume: 08 issue: 1 year: 1972 ident: 10.1205/026387699526395_bib6 article-title: On the mathematical modeling of polymerization reactors publication-title: J-Macromolec Sci Revs Macromol Chem contributor: fullname: Ray – ident: 10.1205/026387699526395_bib1 – year: 1989 ident: 10.1205/026387699526395_bib10 contributor: fullname: Seborg |
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| Snippet | In this work, DMC (Dynamic Matrix Control) of a batch solution polymerization reactor has been investigated experimentally and by simulation to achieve a... Describes an investigation of the application of Dynamic Matrix Control (DMC) of a batch solution polymerization reactor, experimentally and by simulation, to... |
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| SubjectTerms | dynamic matrix control polymerization temperature |
| Title | Temperature Control of a Batch Polymerization Reactor |
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