Open AccessUnseeded semibatch emulsion polymerization of butyl acrylate: Bimodal particle size distribution
Author(s) -
Sajjadi S.,
Brooks B. W.
Publication year - 2000
Publication title -
journal of polymer science part a: polymer chemistry
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.768
H-Index - 152
eISSN - 1099-0518
pISSN - 0887-624X
DOI - 10.1002/(sici)1099-0518(20000201)38:3<528::aid-pola19>3.0.co;2-h
Subject(s) - emulsion polymerization , dispersity , monomer , chemistry , nucleation , polymerization , emulsion , polymer chemistry , potassium persulfate , particle size , butyl acrylate , chemical engineering , acrylate , particle size distribution , particle (ecology) , organic chemistry , polymer , oceanography , engineering , geology
Unseeded semibatch emulsion polymerization of butyl acrylate (BA) using sodium lauryl sulfate as emulsifier and potassium persulfate as initiator was carried out at the conditions where secondary nucleation was probable. This was achieved by using no emulsifier in the initial reactor charge. The effects of changes in monomer emulsion feed rate, initiator concentration and distribution, emulsifier concentration in the feed, and temperature on the evolution of particle size averages and distribution were investigated. Bimodal particle size distributions (PSD) were obtained for most of the latexes. Inhibition effects were found to be important in the development of PSD. Primary particle formation occurred through micellar nucleation, whereas secondary nucleation probably occurred through homogenous nucleation. The polydispersity index (PDI) of the latexes increased with the decreasing monomer emulsion feed rate. The application of a larger amount of initiator to the reactor charge or using a higher temperature, reduced the formation of secondary particles and resulted in a formation of an unimodal PSD. The overall steady‐state rate of polymerization was found to approach the rate of monomer addition ( R p ≈ R a ), if the emulsifier concentration in the aqueous phase was appreciable. This is different from the correlation 1/ R p = 1/K + 1/ R a obtained for the BA semibatch process with neat monomer feed. This suggests that different rate expressions can be used for BA semibatch emulsion polymerization at different conditions. © 2000 John Wiley & Sons, Inc. J Polym Sci A: Polym Chem 38: 528–545, 2000