Full Paper
Mathematical Modeling of Temperature Rising Elution Fractionation (TREF) of Polyethylene and Ethylene/1-Olefin Copolymers
Article first published online: 8 AUG 2012
DOI: 10.1002/macp.201200238
Copyright © 2012 WILEY-VCH Verlag GmbH & Co. KGaA, Weinheim
Additional Information
How to Cite
Siriwongsarn, E., Anantawaraskul, S., Chokputtanawuttilerd, N., Alghyamah, A. A. and Soares, J. B. P. (2012), Mathematical Modeling of Temperature Rising Elution Fractionation (TREF) of Polyethylene and Ethylene/1-Olefin Copolymers. Macromol. Chem. Phys., 213: 1892–1906. doi: 10.1002/macp.201200238
Publication History
- Issue published online: 12 SEP 2012
- Article first published online: 8 AUG 2012
- Manuscript Revised: 12 JUN 2012
- Manuscript Received: 1 MAY 2012
- Abstract
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Keywords:
- crystallization kinetics;
- dissolution kinetics;
- modeling;
- polyethylene;
- temperature rising elution fractionation
Abstract
Temperature rising elution fractionation (TREF) is a characterization technique widely used to estimate chemical composition distribution (CCD) of semicrystalline copolymers. Although several mathematical models have been previously proposed to elucidate the TREF fractionation mechanism, all previous TREF models assume equilibrium fractionation; thus, they cannot describe important kinetics effects observed in TREF experiments. In this work, a new TREF model is developed incorporating crystallization and dissolution kinetic models during the fractionation process. The proposed model describes the effects of molecular weight, comonomer content, cooling rate, heating rate, and solvent flow rate on experimental TREF profiles for both polyethylene and ethylene/1-olefin copolymers very well.

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