Study on the Impact of Coagulation Bath Temperature on the Surface Morphology and Performance of Polyethylene Membrane Prepared by TIPS Method in Purification of Collagen Protein

Document Type : Research Paper

Authors

Faculty of Chemical Engineering; Sahand University of Technology, P.O. Box: 51335-1996,Tabriz, Iran

Abstract

Fabrication of an efficient microfiltration polymeric membrane with low fouling characteristic and high permeation flux is an essential task for developing membrane-related researches and membrane industries. Surface skin layer which decreases the membrane permeation and accelerates the membrane fouling in purification and separation of protein solution is usually observed for all membranes fabricated via thermally induced phase separation (TIPS) method. In this work, the impact of coagulation bath temperature on the skin layer thickness and performance of fabricated membranes was investigated. Collagen protein purification tests were carried out to investigate the impact of skin layer on the performance and determine the fouling mechanisms of the membranes. Obtained results showed that when coagulation bath temperature increases, the thickness of skin layer decreases. In membranes with lower surface porosity, decline in protein permeation is mainly due to the standard blocking fouling mechanism which is a kind of the irreversible fouling phenomenon. In membranes with higher surface porosity, however, decline in protein permeation is mainly due to the intermediate blocking fouling mechanism which is a kind of reversible fouling phenomenon. Obtained results from permeation flux and spectrophotometric analyses of inlet feed and retentate streams within 800 min showed that the collagen recovery ratio for modified and unmodified membranes were 5.6 and less than 1%, respectively. It is worth to mention that for membrane with lower surface porosity the collagen filtration process was stopped within 400 min due to the membrane fouling. For membrane with higher surface porosity, however there was no halting in filtration process within 800 min.

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