Please use this identifier to cite or link to this item: https://doi.org/10.1016/j.ces.2009.08.034
Title: Butanol isomer separation using polyamide-imide/CD mixed matrix membranes via pervaporation
Authors: Wang, Y. 
Chung, T.S. 
Wang, H. 
Goh, S.H. 
Keywords: Butanol isomer
Membranes
Pervaporation
Selectivity
Separations
Simulation
Issue Date: 2009
Citation: Wang, Y., Chung, T.S., Wang, H., Goh, S.H. (2009). Butanol isomer separation using polyamide-imide/CD mixed matrix membranes via pervaporation. Chemical Engineering Science 64 (24) : 5198-5209. ScholarBank@NUS Repository. https://doi.org/10.1016/j.ces.2009.08.034
Abstract: Mixed matrix membranes (MMMs) comprising polyamide-imide (PAI) and α-, β- or γ-cyclodextrin (CD) have been investigated experimentally and computationally for isomeric n-butanol/tert-butanol (n-BuOH/t-BuOH) separation via pervaporation. Consistent with molecular simulation, experimental results show that the CD inclusion ability and butanol discrimination ability are dependent on both CD cavity size and butanol molecular size. The PAI membrane incorporated with α-CD has the smallest cavity and has the highest discrimination ability for the n-BuOH/t-BuOH pair but with a low butanol flux. The mixed matrix membrane embedded with γ-CD has the lowest selectivity and the highest flux. The PAI/β-CD membrane has a comparable selectivity and flux, and exhibits preferential sorption and diffusion selectivity toward n-BuOH. A maximum separation factor of 1.53 with a corresponding flux of 4.4 g/m2 h are obtained at an optimal β-CD loading of 15 wt%. Further increments in the CD content eventually lead to a decrease in separation performance because of CD agglomeration and severe phase separation. To better understand the influence of CD on the separation performance of mixed matrix membranes, SEM, FTIR and XRD have been employed for membrane characterizations. The effect of n-butanol/t-butanol ratio in the feed composition has also been studied. It is found that both flux and separation factor decrease with increasing n-butanol content in the feed. The decline is attributed to the change in total vapor pressure at the upstream and the mutual drag effect of isomeric butanol molecules. © 2009 Elsevier Ltd. All rights reserved.
Source Title: Chemical Engineering Science
URI: http://scholarbank.nus.edu.sg/handle/10635/88600
ISSN: 00092509
DOI: 10.1016/j.ces.2009.08.034
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