反应详情
EQUATION
反应方程式
REACTANTS
反应物
PRODUCTS
生成物
AUXILIARIES
试剂、催化剂与溶剂
PROCEDURE
实验过程
A rubber-reinforced styrene-based resin (C8-6) was produced by the following method. That is, 80 parts of ion-exchanged water, 0.5 part of potassium rosinate, 0.1 part of tert-dodecyl mercaptan, 30 parts (solid content) of a polybutadiene latex (average particle diameter: 2000 Å; gel content: 90%), 10 parts (solid content) of a styrene-butadiene copolymer latex (styrene content: 25%; average particle diameter: 6000 Å), 15 parts of styrene and 5 parts of acrylonitrile were charged into a glass flask equipped with a stirrer under a nitrogen flow, and heated while stirring. When an inside temperature of the flask reached 45° C., a solution prepared by dissolving 0.2 part of sodium pyrophosphate, 0.01 part of ferrous sulfate heptahydrate and 0.2 part of glucose in 20 parts of ion-exchanged water were added thereto. Thereafter, 0.07 part of cumene hydroperoxide was added to the flask to initiate polymerization of the contents in the flask. After conducting the polymerization for 1 hr, 50 parts of ion-exchanged water, 0.7 part of potassium rosinate, 30 parts of styrene, 10 parts of acrylonitrile, 0.05 part of tert-dodecyl mercaptan and 0.01 part of cumene hydroperoxide were continuously added to the flask over 3 hr, and the polymerization of the contents in the flask was further continued for 1 hr, and then 0.2 part of 2,2′-methylene-bis(4-ethyl-6-tert-butyl phenol) was added to the flask to complete the polymerization. The obtained reaction product in the form of a latex was coagulated with an aqueous sulfuric acid solution, washed with water and then washed and neutralized with a potassium hydroxide aqueous solution. Further, the resulting product was washed with water and then dried to obtain a rubber-reinforced styrene-acrylonitrile graft copolymer. It was confirmed that the thus obtained copolymer had a graft percentage of 68%, and the intrinsic viscosity [η] of an acetone-soluble component therein was 0.45 dL/g.
WORKUP
后处理
- customwas produced by the following method
- customequipped with a stirrer under a nitrogen flow
- temperatureheated
- customreached 45° C.
- customa solution prepared
- additionwere added
- custompolymerization of the contents in the flask
- customthe polymerization for 1 hr
- customthe polymerization of the contents in the flask
- customthe polymerization
- customThe obtained reaction product in the form of
- washwashed with water
- washwashed
- washFurther, the resulting product was washed with water
- customdried