2012
DOI: 10.1016/j.biortech.2012.01.017
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Use of the composite membrane of poly(ether-block-amide) and carbon nanotubes (CNTs) in a pervaporation system incorporated with fermentation for butanol production by Clostridium acetobutylicum

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Cited by 67 publications
(27 citation statements)
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“…MMM such as poly(ether-block-amide) (PEBA) filled with ZIF-71, a subclass of metal-organic framework (MOFs) with superhydrophobic properties, gave a high total flux of 520 g/m 2 ·h and butanol separation factor of 18.8 using ABE solution as feed at 37°C23. With the addition of 5% CNTs in PEBA, the hybrid membrane increased the total flux and butanol separation factor from 85 g/m 2 ·h and 17.4 to 153 g/m 2 ·h and 19.4, respectively, compared to the control without CNTs addition24.…”
Section: Discussionmentioning
confidence: 99%
“…MMM such as poly(ether-block-amide) (PEBA) filled with ZIF-71, a subclass of metal-organic framework (MOFs) with superhydrophobic properties, gave a high total flux of 520 g/m 2 ·h and butanol separation factor of 18.8 using ABE solution as feed at 37°C23. With the addition of 5% CNTs in PEBA, the hybrid membrane increased the total flux and butanol separation factor from 85 g/m 2 ·h and 17.4 to 153 g/m 2 ·h and 19.4, respectively, compared to the control without CNTs addition24.…”
Section: Discussionmentioning
confidence: 99%
“…This is the primary factor impeding commercial acceptance of butanol production from renewable feedstock. Several separation techniques have thus been integrated with butanol fermentation processes for in situ solvent removal during batch and continuous butanol fermentation, and these include distillation, liquid–liquid extraction, adsorption by molecular sieves, and membrane separation [1315]. To make butanol competitive with fossil fuels, the production costs must be reduced.…”
Section: Introductionmentioning
confidence: 99%
“…Inhibition from butanol in fermentation-PV coupled process was reported and ABE productivity was 0.38 g/(L h) due to the presence of 7 g/L butanol in fermenter [31]. Although improving membrane flux [34] or increasing the membrane area [26] could increase solvent productivity to the level of 0.58 and 0.50 g/(L h), it would increase the ABE production cost too. High glucose consumption rate of 2.63 g/(L h) was observed, suggesting that there was no serious inhibition on C. beijerinckii BT14.…”
Section: Membranementioning
confidence: 95%
“…Silicalite-1 filled polydimethylsiloxane (PDMS)/polyacrylonitrile (PAN) composite membrane has been applied in ABE fermentation and the solvent productivity reached 0.51 g/(L h) in batch ABE fermentation [16]. Solvent productivity increased to 0.58 g/(L h) when using a poly ether-block-amide (PEBA)/carbon nanotubes (CNTs) membrane with high butanol flux [34]. However, the butanol removal efficiency of these membranes was still less than butanol production rate, which led to accumulation of butanol in fermentation broth and consequently cause inhibition.…”
Section: Introductionmentioning
confidence: 98%