Kinetics and Mechanism of Emulsion Polymerization

1976 ◽  
Vol 49 (3) ◽  
pp. 536-609 ◽  
Author(s):  
J. Ugelstad ◽  
F. K. Hansen

Abstract The course of emulsion polymerization may be considered as involving three intervals: Interval I, where particle formation takes place. The end of this interval is not dependent upon the degree of conversion, but on the total amount of polymer formed. With usual recipes, it ends at about 1-5% conversion. Interval II lasts from the end of Interval I until monomer disappears as a separate phase. In this interval, the particle number is usually found to be constant, the particle volume increases proportional to conversion, the monomer concentration in the particles is approximately constant, and therefore the termination is also constant within the particles. Interval III starts when the monomer disappears as a separate phase. The transition from Intervals II to III is determined by the degree of conversion and differs for different monomers. In cases where the solubility of monomer in the water phase is low, the monomer present in the aqueous phase may usually be neglected compared to the monomer present in the polymer particles. This will usually hold with most monomers at ordinary conditions, where the amount of polymer per unit of water is relatively high, and when the concentration of monomer in the particles is much higher than in the aqueous phase. In this case, the particle volume during Interval III will decrease slightly due to the contraction by polymerization. The concentration of monomer in the particles generally decreases during Interval III, which leads to an increased viscosity within the particles and thereby also to a decrease in the value of the termination constant. The present paper deals chiefly with the kinetics of emulsion polymerization in the three intervals and the application of kinetics to the study of the mechanism. Several review articles on emulsion polymerization have recently appeared in the literature. The reason for presenting a new review article is that a vast number of papers on emulsion polymerization have recently been published, which have broadened the theoretical and experimental knowledge of the process. Several experimental and theoretical studies on the mechanisms of particle formation have appeared. New theories for particle formation outside the micelles have appeared. Also the relative effectiveness of micelles and particles in capturing radicals from the aqueous phase has been discussed in several papers.

1956 ◽  
Vol 29 (1) ◽  
pp. 121-125 ◽  
Author(s):  
A. P. Sheinker ◽  
S. S. Medvedev

Abstract It has been established earlier that polymerization in aqueous solutions of emulsifiers takes place in the water or in the micellae of the emulsifier, depending on the solubility of the monomer and the initiator. The question of the topochemical properties of polymerization in emulsions has not yet been definitively explained. In a number of studies, the hypothesis was advanced that the process of emulsion polymerization takes place in the micellae of the emulsifier, according to the degree of conversion of the micellae into polymer-monomer particles, with the monomer dissolved in the polymer. In order to explain further the mechanism of emulsion polymerization, the kinetics of polymerization of isoprene in water, in solutions of emulsifier and N-cetylpyridinium bromide, and in emulsions in the presence of a water-soluble initiator (hydrogen peroxide) were studied. The dilatometric method was chosen for the kinetic measurements of solutions of emulsifier not saturated with isoprene, and for emulsions. Experiments with solutions of emulsifier saturated with monomer were made during continuous saturation of the emulsifierinitiator solution with isoprene in the gaseous phase. All the experiments were made at 50° C in the absence of oxygen.


1992 ◽  
Vol 45 (12) ◽  
pp. 2057 ◽  
Author(s):  
GL Leslie ◽  
DH Napper ◽  
RG Gilbert

Data on the rate of approach to steady state in a series of studies of the seeded emulsion polymerization of styrene yield the dependence of the rate coefficient for entry of free radicals into latex particles as a function of the weight-fraction polymer and hence of monomer concentration in the aqueous phase. The results are in accord with a model for the entry process (i.e., for the initiator efficiency) based on aqueous-phase propagation and termination being the rate-controlling events.


Processes ◽  
2017 ◽  
Vol 5 (4) ◽  
pp. 19 ◽  
Author(s):  
Iñaki Emaldi ◽  
Shaghayegh Hamzehlou ◽  
Jorge Sanchez-Dolado ◽  
Jose Leiza

Author(s):  
Joseph Zeaiter ◽  
Jose Romagnoli ◽  
Vincent G Gomes

Particle formation is a key step in emulsion polymerization reactions and has been the subject of extensive investigations in the past few decades. The main aim of this work was to investigate, both theoretically and experimentally, the conditions for secondary nucleation and particle evolution in batch and semi-batch emulsion polymerization. The effects of variation in monomer and emulsifier concentration in the feed, the distribution between the charge and the feed, temperature and the emulsion feed rate on polystyrene particle size distribution were investigated both theoretically and experimentally. The population balance and kinetic models developed were employed for predicting the product attributes for a range of reactor operating conditions. The sets of nonlinear algebraic and integro-differential evolution equations were solved efficiently for this work.Monomer and surfactant feed rates were found to have significant effects on the growth of polymer particles and consequently on the particle size. Different particle sizes and distributions were obtained using the same procedure with variable operating mode. A semi-batch reactor with variable monomer emulsion feed can produce latexes with variable polydispersity. A high initial rate of particle formation could lead to reduction in secondary nucleation and hence to the formation of a mono-modal PSD. This can be achieved by using high initiator and emulsifier concentrations in the feed, a high temperature, or a low monomer concentration in the charge. A low initial rate of nucleation increases the possibility of secondary nucleation and the formation of a bimodal PSD. The evolution of a bimodal PSD requires secondary nucleation after primary nucleation occurs.


2021 ◽  
Vol 608 ◽  
pp. 412745
Author(s):  
Mohamed N. Abd-el Salam ◽  
E.R. Shaaban ◽  
F. Benabdallah ◽  
Abdelwahab M.A. Hussein ◽  
Mansour Mohamed

Langmuir ◽  
2002 ◽  
Vol 18 (8) ◽  
pp. 3027-3033 ◽  
Author(s):  
Wolfram Vogelsberger ◽  
Andreas Seidel ◽  
Tilo Breyer

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