ZSM-5 and Fe-ZSM-5 membranes were synthesized on α-Al2O3 by secondary growth. The organic templates were removed at 450℃ in the flowing air environment. After ZSM-5 and Fe-ZSM-5 membranes were treated with NaOH or NaCO3 solution
the hydrophilicity of the membrane surface could be enhanced
leading to improved permeation flux and separation factor in prevoporation of aqueous ethanol solution. After treated by NaOH for 2 h
the permeation flux of Fe-ZSM-5 membrane could reach to 2.01 kg·m-2·h-1 with the separation factor of 21.0.
Molecular simulation of small molecule adsorption and diffusion behavior in PVA hybrid membranes
Zeolite catalysts for catalytic cracking of hydrocarbon to increase light olefins selectivity
Influence of synergistic effect of acid properties and pore structure of ZSM-5 zeolite on the catalytic cracking performance of pentene
Study on the mesoscale mechanism of coking and deactivation of ZSM-5 catalyst in methanol to propylene reaction
Researches on trimethylphosphine and metal oxide modification on ZSM-5 and their influence on catalytic cracking
Related Author
FU Min
CHEN Zijian
TANG Shuai
QIAN Xiliang
WEI Zengxi
ZOU Yun
TONG Zhangfa
LIU Qi
Related Institution
Guangxi Key Laboratory of Petrochemical Resource Processing and Process Intensification Technology, School of Chemistry and Chemical Engineering, Guangxi University
State Key Laboratory of Heavy Oil Processing, Key Laboratory of Catalysis of CNPC, College of Chemical Engineering and Environment, China University of Petroleum
State Key Laboratory of Heavy Oil Processing, China University of Petroleum
Sinopec Shanghai Research Institute of Petrochemical Technology