Results described in an earlier paper on the application of the group-termination coeificient to free-radical polymerizations with size-dependent k t have been used in deriving explicit expressions for polymer molecular weight distributions and related quantities. Three types of polymerization are t
The “group-termination coefficient” in the analysis of kinetic schemes of polymerizations with size-dependent termination coefficients
✍ Scribed by C.H. Bamford
- Publisher
- Elsevier Science
- Year
- 1989
- Tongue
- English
- Weight
- 509 KB
- Volume
- 25
- Category
- Article
- ISSN
- 0014-3057
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✦ Synopsis
The concept of the "group-termination coefficient" is described together with its applications to the kinetic treatment of free-radical polymerizations in which the termination coefficient is a function of radical size. Basically the procedure involves the mean size of a group of radicals and the total radical concentration and leads to expressions for the (instantaneous) radical size distribution and related kinetic functions equivalent to those of the geometric mean approximation. Systems considered in this paper are simple free-radical polymerizations, polymerizations with chain transfer, polymerizations with ideal retardation and systems showing degradative addition to monomer. Rather simple expressions are derived for radical size distributions and mean radical sizes, rates of polymerization, mean kinetic chain lengths and effective mean termination coefficients. The treatment is thus shown to provide a convenient method for analysing the kinetics of a wide variety of free-radical polymerizations. E = <p{mc/(1 + l)(1 + c)b}.~, ¢ = tp[{b + mc/(1 + I)(1 + c)}/l] .
📜 SIMILAR VOLUMES
Al~traet--In earlier studies of the kinetic quantities in non-stationary stages of non-classical free-radical polymerization a relation between the total pre-and after-effects (AMos, AM~, respectively) and the rate coefficients kp kto was proposed. This arose from the results of numerical computatio
Abstraet~Calculations on non-classical systems of the type mentioned in the title have been carried out 'iJsing the treatment described in Part I. As before chain transfer has been neglected. It is shown that the properties of the total pre-effect AMpr ~ are analogous to those previously deduced for
The photosensitized polymerization of styrene in bulk was investigated in the temperature range of 25-70°C with respect to the average rate coefficient of bimolecular chain termination k t , especially its chain length dependence at low conversions, by means of pulsed laser polymerization (PLP). Thr