The attainable ยฎalues of molecular-weight distribution MWD specified by the degree of polymerization and the polydispersity in a batch free-radical polymerization reactor are described. The two-step method based on the quadratic profile of the instantaneous degree of polymerization is used to obtain
Polymer reactors and molecular weight distribution: Part II. Free radical polymerization in a batch reactor
โ Scribed by A. E. Hamielec; J. W. Hodgins; K. Tebbens
- Publisher
- American Institute of Chemical Engineers
- Year
- 1967
- Tongue
- English
- Weight
- 438 KB
- Volume
- 13
- Category
- Article
- ISSN
- 0001-1541
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โฆ Synopsis
fhe free radical polymerization of styrene in benzene was studied theoretically and experimentally over ranges of monomer and catalyst (AIEN) concentrations and temperature in an isothermal, stirred batch reactor. Molecular weight distributions were measured with a gel permeation chromatograph. Tung's hermite polynomial method was used to correct for imperfect resolution.
The differential rate equations have been solved to predict the conversion of monomer and molecular weight distribution of the polymer as a function of time. These solutions were used to interpret the experimental rate data.
Good agreement between theory and experiment was found for narrow and broad distribution, provided the variation of the termination constant with solvent concentration was accounted for.
The agreement between the experimental and calculated molecular weight distribution suggests the utility of gel pemeation chroma'tography in the investigation of polymer reaction kinetics.
๐ SIMILAR VOLUMES
A new method is presented for modeling and controlling polymer molecular weight distribution (MWD) and tensile strength in a batch suspension polymerization of styrene. The molecular weight distribution is modeled by computing the weight fraction of the polymer in different chain length intervals. T