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...
| Main Authors: | , , , |
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| Format: | Article |
| Language: | Russian |
| Published: |
Tomsk Polytechnic University
2009-06-01
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| Series: | Известия Томского политехнического университета: Инжиниринг георесурсов |
| Subjects: | |
| Online Access: | http://izvestiya-tpu.ru/archive/article/view/1140 |
| Summary: | 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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| ISSN: | 2500-1019 2413-1830 |