SEMICONTINUOUS SEEDED EMULSION COPOLYMERIZATION OF VINYL-ACETATE AND METHYL ACRYLATE

被引:27
作者
URQUIOLA, B
ARZAMENDI, G
LEIZA, JR
ZAMORA, A
ASUA, JM
DELGADO, J
ELAASSER, MS
VANDERHOFF, JW
机构
[1] UNIV BASQUE COUNTRY, FAC QUIM,DEPT QUIM APLICADA,INGN QUIM GRP, APDO 1072, E-20080 SAN SEBASTIAN, SPAIN
[2] LEHIGH UNIV, INST EMULS POLYMERS, CTR POLYMER SCI & ENGN, BETHLEHEM, PA 18015 USA
[3] LEHIGH UNIV, INST EMULS POLYMERS, DEPT CHEM ENGN, BETHLEHEM, PA 18015 USA
关键词
D O I
10.1002/pola.1991.080290204
中图分类号
O63 [高分子化学(高聚物)];
学科分类号
070305 ; 080501 ; 081704 ;
摘要
The semicontinuous seeded emulsion copolymerization of vinyl acetate and methyl acrylate was investigated. The effect of type of process (starved process versus semi-starved process), type of feed (neat monomer addition versus monomer emulsion addition), amount of seed initially charged in the reactor, and feed rate on the time evolution of the overall conversion, copolymer composition, and polymer particle size was analyzed. It was found that, in the case of the starved process, both monomers, but mainly vinyl acetate, accumulated in the reactor. The preferential accumulation of vinyl acetate resulted in a drift of the copolymer composition. Both monomers accumulation and copolymer composition drift were reduced by increasing the amount of seed initially charged in the reactor and by decreasing the feed rate. For the semi-starved process, it was found that a vinyl acetate rich copolymer was formed when a low methyl acrylate feed was used, whereas a methyl acrylate rich copolymer was obtained at high methyl acrylate feed rates. For both starved process and semi-starved process, the total number of polymer particles, after an initial increase, reached a plateau value which was the same in all of the experiments carried out. These results were analyzed by means of a mathematical model developed for this system.
引用
收藏
页码:169 / 186
页数:18
相关论文
共 66 条
[51]   THE MODELING OF BATCH AND CONTINUOUS EMULSION POLYMERIZATION REACTORS .1. MODEL FORMULATION AND SENSITIVITY TO PARAMETERS [J].
RAWLINGS, JB ;
RAY, WH .
POLYMER ENGINEERING AND SCIENCE, 1988, 28 (05) :237-256
[52]   MATHEMATICAL-MODELING OF EMULSION COPOLYMERIZATION REACTORS [J].
RICHARDS, JR ;
CONGALIDIS, JP ;
GILBERT, RG .
JOURNAL OF APPLIED POLYMER SCIENCE, 1989, 37 (09) :2727-2756
[53]  
RODRIGUEZ VS, IN PRESS J POLYM SCI
[54]   SEMICONTINUOUS EMULSION COPOLYMERIZATION OF STYRENE AND BUTYL ACRYLATE [J].
SNUPAREK, J ;
KRSKA, F .
JOURNAL OF APPLIED POLYMER SCIENCE, 1976, 20 (07) :1753-1764
[55]   SEMICONTINUOUS EMULSION COPOLYMERIZATION OF ACRYLONITRILE, BUTYL ACRYLATE, AND STYRENE [J].
SNUPAREK, J ;
KRSKA, F .
JOURNAL OF APPLIED POLYMER SCIENCE, 1977, 21 (08) :2253-2260
[56]   CONTRIBUTION TO SEMICONTINUOUS EMULSION POLYMERIZATION .3. PARTICLE FORMATION AND PARTICLE-SIZE [J].
SNUPAREK, J .
ANGEWANDTE MAKROMOLEKULARE CHEMIE, 1974, 37 (JUL5) :1-9
[57]  
SNUPAREK J, 1981, ACTA POLYM, V32, P368
[58]   DIFFUSION-CONTROLLED VINYL POLYMERIZATION .3. FREE-VOLUME PARAMETERS AND DIFFUSION-CONTROLLED PROPAGATION [J].
SOH, SK ;
SUNDBERG, DC .
JOURNAL OF POLYMER SCIENCE PART A-POLYMER CHEMISTRY, 1982, 20 (05) :1331-1344
[59]   DIFFUSION-CONTROLLED VINYL POLYMERIZATION .1. THE GEL EFFECT [J].
SOH, SK ;
SUNDBERG, DC .
JOURNAL OF POLYMER SCIENCE PART A-POLYMER CHEMISTRY, 1982, 20 (05) :1299-1313
[60]   DIFFUSION-CONTROLLED VINYL POLYMERIZATION .4. COMPARISON OF THEORY AND EXPERIMENT [J].
SOH, SK ;
SUNDBERG, DC .
JOURNAL OF POLYMER SCIENCE PART A-POLYMER CHEMISTRY, 1982, 20 (05) :1345-1371