Free-radical polymerization engineering—III. Modelling homogeneous polymerization of ethylene: mathematical model and new method for obtaining molecular-weight distribution-Reference-Cited by-同舟云学术

Free-radical polymerization engineering—III. Modelling homogeneous polymerization of ethylene: mathematical model and new method for obtaining molecular-weight distribution

Published:1992-10 Issue:15-16 Volume:47 Page:3969-3980
ISSN:0009-2509
Container-title:Chemical Engineering Science
language:en
Short-container-title:Chemical Engineering Science

Author:

Lorenzini Pascal,Pons Michel,Villermaux Jacques

Publisher

Elsevier BV

Subject

Applied Mathematics,Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Reference18 articles.

1. Analysis of the high pressure polyethylene tubular reactor with axial mixing;Agrawal;A.I.Ch.E.J.,1975

2. Mathematical model for high-pressure tubular reactor for ethylene polymerization;Brandolin;Ind.Engng Chem. Res.,1988

3. Computer model for tubular high-pressure polyethylene reactors;Chen;A.I.Ch.E.J.,1976

4. Prediction of molar mass distribution, number and weight average degree of polymerization and branching of low density polyethylene;Feucht;Chem. Engng. Sci,1985

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