A MATHEMATICAL MODEL FOR POLYMERIZATION OF ISOPRENE, STYRENE, OR BUTADIENE WITH ALKYL LITHIUMS IN BATCH REACTORS

被引：12

|

作者：

EDGAR, TD

HASAN, S

ANTHONY, RG

机构：

来源：

CHEMICAL ENGINEERING SCIENCE | 1970年 / 25卷 / 09期

关键词：

D O I：

10.1016/0009-2509(70)85068-0

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

收藏

页码：1463 / &

相关论文

共 50 条

[41] MATHEMATICAL MODELING OF THE GAS-PHASE POLYMERIZATION OF BUTADIENE BASED ON THE MODEL OF INTERPENETRATING CONTINUA
Manuiko, G. V.
Kharitonova, N. E.
Aminova, G. A.
D'yakonov, G. S.
JOURNAL OF ENGINEERING PHYSICS AND THERMOPHYSICS, 2006, 79 (05) : 893 - 898
[42] Model linear block co-, ter-, and quaterpolymers of 1,3-cyclohexadiene with styrene, isoprene, and butadiene
Tsoukatos, T
Avgeropoulos, A
Hadjichristidis, N
Hong, KL
Mays, JW
MACROMOLECULES, 2002, 35 (21) : 7928 - 7935
[43] Development of a mathematical model for the dynamic optimization of batch reactors, and MINLP synthesis of plug-flow reactors in complex networks
Ropotar, Marcel
Kravanja, Zdravko
ACTA CHIMICA SLOVENICA, 2007, 54 (04) : 700 - 712
[44] Controlling chain structure of diene polymers. Part 2. Role of polar modifiers in anionic polymerization of butadiene and isoprene and their copolymerization with styrene
Kozak, Radoslaw
Matlengiewicz, Marek
PRZEMYSL CHEMICZNY, 2015, 94 (08): : 1362 - 1368
[45] MATHEMATICAL-MODEL OF GROWTH OF LARGE PARTICLES FROM THE FINE FRACTION IN BATCH AND CONTINUOUS REACTORS
PENKOV, NV
FLISYUK, OM
JOURNAL OF APPLIED CHEMISTRY OF THE USSR, 1985, 58 (09): : 1990 - 1993
[46] Model-based On-Line Optimization Framework for Semi-batch Polymerization Reactors
Jung, Tae Y.
Nie, Yisu
Lee, J. H.
Biegler, L. T.
IFAC PAPERSONLINE, 2015, 48 (08): : 164 - 169
[47] On the kinetics of styrene emulsion polymerization above CMC.: I.: A mathematical model
Herrera-Ordóñez, J
Olayo, R
JOURNAL OF POLYMER SCIENCE PART A-POLYMER CHEMISTRY, 2000, 38 (12) : 2201 - 2218
[48] MATHEMATICAL MODEL OF GROWTH OF LARGE PARTICLES FROM THE FINE FRACTION IN BATCH AND CONTINUOUS REACTORS.
Pen'kov, N.V.
Flisyuk, O.M.
Journal of applied chemistry of the USSR, 1985, 58 (9 pt 3): : 1990 - 1993
[49] High pressure polymerization of ethylene. An improved mathematical model for industrial tubular reactors
Brandolin, A
Lacunza, MH
Ugrin, PE
Capiati, NJ
POLYMER REACTION ENGINEERING, 1996, 4 (04): : 193 - 241
[50] THE MODELING OF BATCH AND CONTINUOUS EMULSION POLYMERIZATION REACTORS .1. MODEL FORMULATION AND SENSITIVITY TO PARAMETERS
RAWLINGS, JB
RAY, WH
POLYMER ENGINEERING AND SCIENCE, 1988, 28 (05): : 237 - 256

← 1 2 3 4 5 →