Mathematical modeling of the reaction system of dicyclopentadiene polymerization

Based on the mathematical model of dicyclopentadiene polymerization the authors have proposed the mathematical model of the polymerization reactor. The reactor for producing polydicyclopentadiene was designed. It is operated in adiabatic and isothermal temperature conditions. The maximum permissible...

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Main Authors: Vladimir Grigoryevich Bondaletov, Aleksey Alekseevich Lyapkov, Elena Ivanovna Melnik, Georgy Vitalievich Borisov
Format: Article
Language:Russian
Published: Tomsk Polytechnic University 2009-06-01
Series:Известия Томского политехнического университета: Инжиниринг георесурсов
Subjects:
Online Access:http://izvestiya-tpu.ru/archive/article/view/1140
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author Vladimir Grigoryevich Bondaletov
Aleksey Alekseevich Lyapkov
Elena Ivanovna Melnik
Georgy Vitalievich Borisov
author_facet Vladimir Grigoryevich Bondaletov
Aleksey Alekseevich Lyapkov
Elena Ivanovna Melnik
Georgy Vitalievich Borisov
author_sort Vladimir Grigoryevich Bondaletov
collection DOAJ
description Based on the mathematical model of dicyclopentadiene polymerization the authors have proposed the mathematical model of the polymerization reactor. The reactor for producing polydicyclopentadiene was designed. It is operated in adiabatic and isothermal temperature conditions. The maximum permissible monomer concentration in toluene solution was determined. It was shown that the polymerization products in different reactors have the same molecular mass and different molecular weight distribution.
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spelling doaj.art-52a321e355724bca93b7501df98812dc2023-06-03T21:13:21ZrusTomsk Polytechnic UniversityИзвестия Томского политехнического университета: Инжиниринг георесурсов2500-10192413-18302009-06-013233Mathematical modeling of the reaction system of dicyclopentadiene polymerizationVladimir Grigoryevich BondaletovAleksey Alekseevich LyapkovElena Ivanovna MelnikGeorgy Vitalievich BorisovBased on the mathematical model of dicyclopentadiene polymerization the authors have proposed the mathematical model of the polymerization reactor. The reactor for producing polydicyclopentadiene was designed. It is operated in adiabatic and isothermal temperature conditions. The maximum permissible monomer concentration in toluene solution was determined. It was shown that the polymerization products in different reactors have the same molecular mass and different molecular weight distribution.http://izvestiya-tpu.ru/archive/article/view/1140polydicyclopentadieneisotermic reactormathematic modelingmolecular massmolecular weight distribution
spellingShingle Vladimir Grigoryevich Bondaletov
Aleksey Alekseevich Lyapkov
Elena Ivanovna Melnik
Georgy Vitalievich Borisov
Mathematical modeling of the reaction system of dicyclopentadiene polymerization
Известия Томского политехнического университета: Инжиниринг георесурсов
polydicyclopentadiene
isotermic reactor
mathematic modeling
molecular mass
molecular weight distribution
title Mathematical modeling of the reaction system of dicyclopentadiene polymerization
title_full Mathematical modeling of the reaction system of dicyclopentadiene polymerization
title_fullStr Mathematical modeling of the reaction system of dicyclopentadiene polymerization
title_full_unstemmed Mathematical modeling of the reaction system of dicyclopentadiene polymerization
title_short Mathematical modeling of the reaction system of dicyclopentadiene polymerization
title_sort mathematical modeling of the reaction system of dicyclopentadiene polymerization
topic polydicyclopentadiene
isotermic reactor
mathematic modeling
molecular mass
molecular weight distribution
url http://izvestiya-tpu.ru/archive/article/view/1140
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AT alekseyalekseevichlyapkov mathematicalmodelingofthereactionsystemofdicyclopentadienepolymerization
AT elenaivanovnamelnik mathematicalmodelingofthereactionsystemofdicyclopentadienepolymerization
AT georgyvitalievichborisov mathematicalmodelingofthereactionsystemofdicyclopentadienepolymerization