Transport of free radicals out of latex particles into the aqueous phase plays an important role in the emulsion polymerization of vinyl acetate. This so-called "desorption" process involves chain transfer to monomer which generates a mobile an8 rather stable monomer-unit free radical followed by th
Kinetics of vinyl chloride and vinyl acetate emulsion polymerization
β Scribed by N. Friis; A. E. Hamielec
- Publisher
- John Wiley and Sons
- Year
- 1975
- Tongue
- English
- Weight
- 707 KB
- Volume
- 19
- Category
- Article
- ISSN
- 0021-8995
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β¦ Synopsis
Abstract
The kinetics of vinyl chloride and vinyl acetate emulsion polymerization are reexamined. The validity of Ugelstad's model for systems with high desorption rate is confirmed by simulating conversion histories for both systems at different initiator concentrations and particle numbers. On the basis of the model, it is shown that at ordinary initiation rates, termination reactions are unimportant with respect to molecular weight development in both systems, and as a consequence, molecular weight development is independent of number and size distribution of polymer particles and of initiator and emulsifier level. Based on this conclusion, it is shown that in accordance with experimental facts, the molecular weight distribution obtained in vinyl chloride emulsion polymerization is the most probable distribution, and it is concluded that the number of longβchain branch points per repetition unit is less than 2 Γ 10^β4^ at high conversions. In vinyl acetate emulsion polymerization, an almost logarithmic normal distribution is obtained. The distribution is strongly broadened by branching reactions with the number of longβchain branch points increasing rapidly with monomer conversion. The increase of M~n~ with increasing conversion is due to terminal doubleβbond polymerization, while the increase in M~w~ is due mainly to transfer to polymer.
π SIMILAR VOLUMES
The emulsion polymerization of vinyl acetate was studied a t 50Β°C. It was found that the rate of polymerization was proportional to the 0.5 power of the initiator concentration and the 0.25 power of the number of particles. The number of particles was proportional to the power 0.5 f 0.05 of the emul
Kinetics and mechanism of the emulsion polymerization of vinyl acetate by redox initiation ## 2. L.cperittwnlrt1 'l'lie experimental riiethods crnployt:tl wen: itlentical with ttiosc described previously [17, IS]. The image analyzer (Biltlanalyse IBAS 1 arid 3) was used to measure t h e average d
Studies have been made of the 7-induced emulsion polymerization of styrene and comparisons made with chemically initiated emulsion polymerization. The polymerization proceeded smoothly to high conversions at 0 and 60Β°C, the reaction showing a high G (monomer) value. Complete conversions were obtaine