dc.contributor.author |
Baltsas, A |
en |
dc.contributor.author |
Papadopoulos, E |
en |
dc.contributor.author |
Kiparissides, C |
en |
dc.date.accessioned |
2014-03-01T01:46:40Z |
|
dc.date.available |
2014-03-01T01:46:40Z |
|
dc.date.issued |
1998 |
en |
dc.identifier.uri |
https://dspace.lib.ntua.gr/xmlui/handle/123456789/24985 |
|
dc.subject |
Free Radical |
en |
dc.subject |
Free Radical Polymerization |
en |
dc.subject |
High Pressure |
en |
dc.subject |
Kinetics |
en |
dc.subject |
Manufacturing Industry |
en |
dc.subject |
Polyethylene |
en |
dc.subject |
Rate Constant |
en |
dc.subject |
Method of Moment |
en |
dc.title |
Application and validation of the pseudo-kinetic rate constant method to high pressure LDPE tubular reactors |
en |
heal.type |
journalArticle |
en |
heal.identifier.primary |
10.1016/S0098-1354(98)00042-8 |
en |
heal.identifier.secondary |
http://dx.doi.org/10.1016/S0098-1354(98)00042-8 |
en |
heal.publicationDate |
1998 |
en |
heal.abstract |
The present study is concerned with the application of the pseudo-kinetic rate constant method to high pressure LDPE tubular reactors. The utilization of multiple monomers is of profound importance to the polymer manufacturing industry since it leads to the production of an unlimited number of polymer types with a wide range of properties. However, by increasing the number of comonomers |
en |
heal.journalName |
Computers & Chemical Engineering |
en |
dc.identifier.doi |
10.1016/S0098-1354(98)00042-8 |
en |