Online inferential product attribute estimation for optimal operation of emulsion terpolymerisation: Application to styrene/MMA/MA
An advanced model for process design and control of emulsion terpolymerisation was developed. A test case of emulsion terpolymerisation of styrene (Sty), methyl methacrylate (MMA) and methyl acrylate (MA) was investigated on state of the art facilities for predicting, optimising and control end-use...
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Veröffentlicht in: | Chemical engineering science 2007-08, Vol.62 (16), p.4420-4438 |
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creator | Srour, M.H. Gomes, V.G. Romagnoli, J.A. |
description | An advanced model for process design and control of emulsion terpolymerisation was developed. A test case of emulsion terpolymerisation of styrene (Sty), methyl methacrylate (MMA) and methyl acrylate (MA) was investigated on state of the art facilities for predicting, optimising and control end-use product properties including global and individual conversions, terpolymer composition, the average particle diameter and concentration, glass transition temperature, molecular weight distribution, the number- and weight-average molecular weights and particle size distribution.
The model equations include diffusion-controlled kinetics at high monomer conversions, where transition from a ‘zero–one’ to a ‘pseudo-bulk’ regime occurs. Transport equations are used to describe the system transients for batch and semi-batch processes. The particle evolution is described by population balance equations which comprised a set of integro-partial differential and nonlinear algebraic equations. Backward finite difference approximation method is used to discretise the population equation and converts them from partial differential equations to ordinary differential equations. The model predictions were experimentally validated in the laboratory and were found to be in excellent agreement, thus paving the way for further application of the model. |
doi_str_mv | 10.1016/j.ces.2007.04.046 |
format | Article |
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The model equations include diffusion-controlled kinetics at high monomer conversions, where transition from a ‘zero–one’ to a ‘pseudo-bulk’ regime occurs. Transport equations are used to describe the system transients for batch and semi-batch processes. The particle evolution is described by population balance equations which comprised a set of integro-partial differential and nonlinear algebraic equations. Backward finite difference approximation method is used to discretise the population equation and converts them from partial differential equations to ordinary differential equations. The model predictions were experimentally validated in the laboratory and were found to be in excellent agreement, thus paving the way for further application of the model.</description><subject>Applied sciences</subject><subject>Chemical engineering</subject><subject>Diffusion-control</subject><subject>Emulsion terpolymerisation</subject><subject>Exact sciences and technology</subject><subject>Polymer molar mass</subject><subject>Polymer particle size</subject><subject>Pseudo-bulk kinetics</subject><subject>Zero–one kinetics</subject><issn>0009-2509</issn><issn>1873-4405</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2007</creationdate><recordtype>article</recordtype><recordid>eNp9UE1r3DAQFSWBbj5-QG-6tDfvjmzJttLTEvoFWXJpzkKWR6BFazmSXNhrf3m1daC3wsB8vXnDe4R8YLBlwNrdcWswbWuAbgu8RPuObFjfNRXnIK7IBgBkVQuQ78lNSsfSdh2DDfn9PHk3IXWTxYhTdtrTOYZxMZnqnKMblowUU3YnnV2YqA2RhvnS-pIxrtNgKZ4Wny51xjgHfz5hdOnv9oHu59k7s0JzoCmfyy_cHQ773WF_R66t9gnv3_Itefn65efj9-rp-duPx_1TZRopciUYWFO3wJnQTEtRj3qoG9Z20IDsRytHYbXh2PMe2TCIkTV27ASTth2GgfPmlnxaeYu-16VIUieXDHqvJwxLUk3xRNQcCpCtQBNDShGtmmPRG8-Kgbq4rY6quK0ubivgJdpy8_GNXCejvY16Mi79O-wll4W-4D6vOCxKfzmMKhmHk8HRRTRZjcH958sfQ4KX9A</recordid><startdate>20070801</startdate><enddate>20070801</enddate><creator>Srour, M.H.</creator><creator>Gomes, V.G.</creator><creator>Romagnoli, J.A.</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7U5</scope><scope>8FD</scope><scope>F28</scope><scope>FR3</scope><scope>L7M</scope></search><sort><creationdate>20070801</creationdate><title>Online inferential product attribute estimation for optimal operation of emulsion terpolymerisation: Application to styrene/MMA/MA</title><author>Srour, M.H. ; Gomes, V.G. ; Romagnoli, J.A.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c395t-510fc260415a1a952dab2316703098df9d5fac4e848e1bb5d13fd7519f6bbb443</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2007</creationdate><topic>Applied sciences</topic><topic>Chemical engineering</topic><topic>Diffusion-control</topic><topic>Emulsion terpolymerisation</topic><topic>Exact sciences and technology</topic><topic>Polymer molar mass</topic><topic>Polymer particle size</topic><topic>Pseudo-bulk kinetics</topic><topic>Zero–one kinetics</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Srour, M.H.</creatorcontrib><creatorcontrib>Gomes, V.G.</creatorcontrib><creatorcontrib>Romagnoli, J.A.</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>Technology Research Database</collection><collection>ANTE: Abstracts in New Technology & Engineering</collection><collection>Engineering Research Database</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>Chemical engineering science</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Srour, M.H.</au><au>Gomes, V.G.</au><au>Romagnoli, J.A.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Online inferential product attribute estimation for optimal operation of emulsion terpolymerisation: Application to styrene/MMA/MA</atitle><jtitle>Chemical engineering science</jtitle><date>2007-08-01</date><risdate>2007</risdate><volume>62</volume><issue>16</issue><spage>4420</spage><epage>4438</epage><pages>4420-4438</pages><issn>0009-2509</issn><eissn>1873-4405</eissn><coden>CESCAC</coden><abstract>An advanced model for process design and control of emulsion terpolymerisation was developed. A test case of emulsion terpolymerisation of styrene (Sty), methyl methacrylate (MMA) and methyl acrylate (MA) was investigated on state of the art facilities for predicting, optimising and control end-use product properties including global and individual conversions, terpolymer composition, the average particle diameter and concentration, glass transition temperature, molecular weight distribution, the number- and weight-average molecular weights and particle size distribution.
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source | ScienceDirect Journals (5 years ago - present) |
subjects | Applied sciences Chemical engineering Diffusion-control Emulsion terpolymerisation Exact sciences and technology Polymer molar mass Polymer particle size Pseudo-bulk kinetics Zero–one kinetics |
title | Online inferential product attribute estimation for optimal operation of emulsion terpolymerisation: Application to styrene/MMA/MA |
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