Bulk polymerization of styrene using multifunctional initiators in a batch reactor: A comprehensive mathematical model
"A detailed, comprehensive mathematical model for bulk polymerization of styrene using multifunctional initiators - both linear and cyclic - in a batch reactor was developed. The model is based on a kinetic mechanism that considers thermal initiation and chemical initiation by sequential decomp...
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| Acceso en línea: | http://ri.itba.edu.ar/handle/123456789/3790 |
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I32-R138-123456789-37902022-12-07T13:05:56Z Bulk polymerization of styrene using multifunctional initiators in a batch reactor: A comprehensive mathematical model Berkenwald, Emilio Laganá, María Laura Acuña, Pablo Morales Balado, Graciela Elizabeth Estenoz, Diana MODELOS MATEMATICOS POLIMERIZACION POLIESTIRENOS INICIADORES MULTIFUNCIONALES "A detailed, comprehensive mathematical model for bulk polymerization of styrene using multifunctional initiators - both linear and cyclic - in a batch reactor was developed. The model is based on a kinetic mechanism that considers thermal initiation and chemical initiation by sequential decomposition of labile groups, propagation, transfer to monomer, termination by combination and re-initiation reactions due to undecomposed labile groups. The model predicts the evolution of global reaction variables (e.g, concentration of reagents, products, radical species and labile groups) as well as the evolution of the detailed complete polymer molecular weight distributions, with polymer species characterized by chain length and number of undecomposed labile groups. The mathematical model was adjusted and validated using experimental data for various peroxide-type multifunctional initiators: diethyl ketone triperoxide (DEKTP, cyclic trifunctional), pinacolone diperoxide (PDP, cyclic bifunctional) and 1,1-bis(tert-butylperoxy)cyclohexane (L331, linear bifunctional). The model very adequately predicts polymerization rates and complete molecular weight distributions. The model is used to theoretically evaluate the influence of initiator structure and functionality as well as reaction conditions." info:eu-repo/date/embargoEnd/2017-02-28 2022-04-18T19:36:13Z 2022-04-18T19:36:13Z 2016-02 Artículos de Publicaciones Periódicas info:eu-repo/semantics/acceptedVersion 1542-6580 http://ri.itba.edu.ar/handle/123456789/3790 en info:eu-repo/semantics/reference/doi/10.1515/ijcre-2015-0102 info:eu-repo/grantAgreement/ANPCyT/PICT/2011-1254/AR. Ciudad Autónoma de Buenos Aires info:eu-repo/semantics/embargoedAccess application/pdf |
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Instituto Tecnológico de Buenos Aires (ITBA) |
| institution_str |
I-32 |
| repository_str |
R-138 |
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Repositorio Institucional Instituto Tecnológico de Buenos Aires (ITBA) |
| language |
Inglés |
| topic |
MODELOS MATEMATICOS POLIMERIZACION POLIESTIRENOS INICIADORES MULTIFUNCIONALES |
| spellingShingle |
MODELOS MATEMATICOS POLIMERIZACION POLIESTIRENOS INICIADORES MULTIFUNCIONALES Berkenwald, Emilio Laganá, María Laura Acuña, Pablo Morales Balado, Graciela Elizabeth Estenoz, Diana Bulk polymerization of styrene using multifunctional initiators in a batch reactor: A comprehensive mathematical model |
| topic_facet |
MODELOS MATEMATICOS POLIMERIZACION POLIESTIRENOS INICIADORES MULTIFUNCIONALES |
| description |
"A detailed, comprehensive mathematical model for bulk polymerization of styrene using multifunctional initiators - both linear and cyclic - in a batch reactor was developed. The model is based on a kinetic mechanism that considers thermal initiation and chemical initiation by sequential decomposition of labile groups, propagation, transfer to monomer, termination by combination and re-initiation reactions due to undecomposed labile groups. The model predicts the evolution of global reaction variables (e.g, concentration of reagents, products, radical species and labile groups) as well as the evolution of the detailed complete polymer molecular weight distributions, with polymer species characterized by chain length and number of undecomposed labile groups. The mathematical model was adjusted and validated using experimental data for various peroxide-type multifunctional initiators: diethyl ketone triperoxide (DEKTP, cyclic trifunctional), pinacolone diperoxide (PDP, cyclic bifunctional) and 1,1-bis(tert-butylperoxy)cyclohexane (L331, linear bifunctional). The model very adequately predicts polymerization rates and complete molecular weight distributions. The model is used to theoretically evaluate the influence of initiator structure and functionality as well as reaction conditions." |
| format |
Artículos de Publicaciones Periódicas acceptedVersion |
| author |
Berkenwald, Emilio Laganá, María Laura Acuña, Pablo Morales Balado, Graciela Elizabeth Estenoz, Diana |
| author_facet |
Berkenwald, Emilio Laganá, María Laura Acuña, Pablo Morales Balado, Graciela Elizabeth Estenoz, Diana |
| author_sort |
Berkenwald, Emilio |
| title |
Bulk polymerization of styrene using multifunctional initiators in a batch reactor: A comprehensive mathematical model |
| title_short |
Bulk polymerization of styrene using multifunctional initiators in a batch reactor: A comprehensive mathematical model |
| title_full |
Bulk polymerization of styrene using multifunctional initiators in a batch reactor: A comprehensive mathematical model |
| title_fullStr |
Bulk polymerization of styrene using multifunctional initiators in a batch reactor: A comprehensive mathematical model |
| title_full_unstemmed |
Bulk polymerization of styrene using multifunctional initiators in a batch reactor: A comprehensive mathematical model |
| title_sort |
bulk polymerization of styrene using multifunctional initiators in a batch reactor: a comprehensive mathematical model |
| publishDate |
info |
| url |
http://ri.itba.edu.ar/handle/123456789/3790 |
| work_keys_str_mv |
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| _version_ |
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