dc.contributor.author |
Kotoulas, C |
en |
dc.contributor.author |
Pladis, P |
en |
dc.contributor.author |
Papadopoulos, E |
en |
dc.contributor.author |
Kiparissides, C |
en |
dc.date.accessioned |
2014-03-01T01:52:34Z |
|
dc.date.available |
2014-03-01T01:52:34Z |
|
dc.date.issued |
2003 |
en |
dc.identifier.uri |
https://dspace.lib.ntua.gr/xmlui/handle/123456789/26657 |
|
dc.subject |
Dynamic Behavior |
en |
dc.subject |
Energy Balance |
en |
dc.subject |
Equation of State |
en |
dc.subject |
Free Radical |
en |
dc.subject |
Free Volume |
en |
dc.subject |
Kinetic Model |
en |
dc.subject |
Molecular Weight Distribution |
en |
dc.subject |
Programming Language |
en |
dc.title |
Computer aided design of styrene batch suspension polymerization reactors |
en |
heal.type |
journalArticle |
en |
heal.identifier.primary |
10.1016/S1570-7946(03)80110-4 |
en |
heal.identifier.secondary |
http://dx.doi.org/10.1016/S1570-7946(03)80110-4 |
en |
heal.publicationDate |
2003 |
en |
heal.abstract |
The present paper deals with the development of a comprehensive, CAD tool for a styrene free-radical batch suspension polymerization reactor. The gPROMS© simulation platform is employed for describing the dynamic behavior of the batch polymerization system. The kinetic model accounts for both thermal and chemical initiation mechanisms, thus, the model can be employed over an extended range of polymerization temperatures. |
en |
dc.identifier.doi |
10.1016/S1570-7946(03)80110-4 |
en |