TY - JOUR
T1 - Preparation and characterization of ZSM-5/PDMS hybrid pervaporation membranes
T2 - Laboratory results and pilot-scale performance
AU - Liu, Jie
AU - Chen, Jinxun
AU - Zhan, Xia
AU - Fang, Manquan
AU - Wang, Tao
AU - Li, Jiding
N1 - Publisher Copyright:
© 2015 Elsevier B.V.
PY - 2015/7/14
Y1 - 2015/7/14
N2 - Abstract ZSM-5 zeolites/Polydimethylsiloxane (PDMS) hybrid membranes were prepared and subsequently applied in ethanol recovery from an ethanol-water mixture by pervaporation (PV) using a pilot-plant with spiral-wound membrane module. The influences of calcination temperature on PV performances as well as zeolites properties were studied. Meanwhile, the optimum zeolites loading was turned out to be 30 wt%, the SEM indicated that ZSM-5/PDMS was coated uniformly on the surface of porous PVDF substrate, and the separation layer was dense with the thickness of 8.9 μm. The effects of feed temperature and feed flow velocity on the performance of the pilot-scale PV system were investigated. It was found that with increasing feed temperature, the permeation flux increased, whereas the separation factor firstly increased, then it decreased rapidly. As the feed flow velocity increased, both the permeation flux and separation factor increased. Under the optimum process conditions, the pilot-plant showed a total flux of 1170 g/m2 h with ethanol concentration of 60.00 wt% at a feed temperature of 60 °C, a feed flow velocity of 3.2 cm/s and a permeation side pressure of about 2300 Pa with a feed concentration of 10.0 wt% ethanol. A long term run consisted of 1000 h of continuous PV experiments exhibited satisfying performance stability, indicating that the pilot-plant was a promising approach to separate ethanol from ethanol-water mixture and had long-term stability required for industrial application.
AB - Abstract ZSM-5 zeolites/Polydimethylsiloxane (PDMS) hybrid membranes were prepared and subsequently applied in ethanol recovery from an ethanol-water mixture by pervaporation (PV) using a pilot-plant with spiral-wound membrane module. The influences of calcination temperature on PV performances as well as zeolites properties were studied. Meanwhile, the optimum zeolites loading was turned out to be 30 wt%, the SEM indicated that ZSM-5/PDMS was coated uniformly on the surface of porous PVDF substrate, and the separation layer was dense with the thickness of 8.9 μm. The effects of feed temperature and feed flow velocity on the performance of the pilot-scale PV system were investigated. It was found that with increasing feed temperature, the permeation flux increased, whereas the separation factor firstly increased, then it decreased rapidly. As the feed flow velocity increased, both the permeation flux and separation factor increased. Under the optimum process conditions, the pilot-plant showed a total flux of 1170 g/m2 h with ethanol concentration of 60.00 wt% at a feed temperature of 60 °C, a feed flow velocity of 3.2 cm/s and a permeation side pressure of about 2300 Pa with a feed concentration of 10.0 wt% ethanol. A long term run consisted of 1000 h of continuous PV experiments exhibited satisfying performance stability, indicating that the pilot-plant was a promising approach to separate ethanol from ethanol-water mixture and had long-term stability required for industrial application.
KW - Calcination
KW - Ethanol recovery
KW - PDMS
KW - Pilot-scale pervaporation
KW - ZSM-5 zeolites
UR - http://www.scopus.com/inward/record.url?scp=84936948739&partnerID=8YFLogxK
U2 - 10.1016/j.seppur.2015.06.036
DO - 10.1016/j.seppur.2015.06.036
M3 - Article
AN - SCOPUS:84936948739
SN - 1383-5866
VL - 150
SP - 257
EP - 267
JO - Separation and Purification Technology
JF - Separation and Purification Technology
M1 - 12408
ER -