TY - JOUR
T1 - Preparation of ZIF-78/ZnO membranes and their application in gasoline vapor recovery
AU - Li, Jing
AU - Xu, Rong
AU - Jiang, Wei Hua
AU - Chen, Ruo Yu
AU - Zhong, Jing
AU - Huang, Wei Qiu
AU - Gu, Xue Hong
N1 - Publisher Copyright:
©, 2015, Zhejiang University. All right reserved.
PY - 2015/8/1
Y1 - 2015/8/1
N2 - ZIF-78 membranes were prepared on ZnO supports (zinc source) via a reactive seeding synthesis method, and XRD, TGA and SEM were employed to characterize the synthesized powder and membranes. The prepared ZIF-78/ZnO membranes were applied for gasoline vapor recovery, and the effects of operating pressure and temperature, feed concentration and cutting aspect ratio on the separation performance of the ZIF-78 membranes were investigated. The results show that the separation factor increases with the increase of feed concentration, and it reaches maximum under conditions of feed pressure 0.06 MPa, operating temperature 20℃ and cutting aspect ratio 0.2. The permeability of the membrane increases with the increase of operating pressure, feed concentration, operating temperature and cutting aspect ratio. (C5~C7)/N2 mixtures were used as the model for evaluating membrane performance under different operating pressures. At 20℃, the separation factors of the membrane for n-C5H12/N2, n-C6H14/N2 and n-C7H16/N2 are 2.45, 2.27 and 2.13 respectively, with corresponding permeability of 9.20×10-8, 6.22×10-8 and 3.96×10-8 mol·(m2·s·Pa)-1 at a feeding pressure of 0.06 MPa and alkane volume fraction of 30 %(V).
AB - ZIF-78 membranes were prepared on ZnO supports (zinc source) via a reactive seeding synthesis method, and XRD, TGA and SEM were employed to characterize the synthesized powder and membranes. The prepared ZIF-78/ZnO membranes were applied for gasoline vapor recovery, and the effects of operating pressure and temperature, feed concentration and cutting aspect ratio on the separation performance of the ZIF-78 membranes were investigated. The results show that the separation factor increases with the increase of feed concentration, and it reaches maximum under conditions of feed pressure 0.06 MPa, operating temperature 20℃ and cutting aspect ratio 0.2. The permeability of the membrane increases with the increase of operating pressure, feed concentration, operating temperature and cutting aspect ratio. (C5~C7)/N2 mixtures were used as the model for evaluating membrane performance under different operating pressures. At 20℃, the separation factors of the membrane for n-C5H12/N2, n-C6H14/N2 and n-C7H16/N2 are 2.45, 2.27 and 2.13 respectively, with corresponding permeability of 9.20×10-8, 6.22×10-8 and 3.96×10-8 mol·(m2·s·Pa)-1 at a feeding pressure of 0.06 MPa and alkane volume fraction of 30 %(V).
KW - Alkane (C5-C7)/N separation
KW - Gasoline vapor recovery
KW - Operating conditions
KW - ZIF-78/ZnO membrane
UR - http://www.scopus.com/inward/record.url?scp=84942062384&partnerID=8YFLogxK
U2 - 10.3969/j.issn.1003-9015.2015.04.011
DO - 10.3969/j.issn.1003-9015.2015.04.011
M3 - 文章
AN - SCOPUS:84942062384
SN - 1003-9015
VL - 29
SP - 843
EP - 850
JO - Gao Xiao Hua Xue Gong Cheng Xue Bao/Journal of Chemical Engineering of Chinese Universities
JF - Gao Xiao Hua Xue Gong Cheng Xue Bao/Journal of Chemical Engineering of Chinese Universities
IS - 4
ER -