Synthesis of silicalite-1 membrane with two silicon source by secondary growth method and its pervaporation performance

被引:65
作者
Shen, Dong [2 ]
Xiao, Wei [1 ]
Yang, Jianhua [1 ]
Chu, Naibo [1 ]
Lu, Jinming [1 ]
Yin, Dehong [1 ]
Wang, Jinqu [1 ]
机构
[1] Dalian Univ Technol, State Key Lab Fine Chem, Dalian 116012, Peoples R China
[2] Sinopec Ningbo Engn Co Ltd SNEC, Proc Syst Dept, Ningbo 315106, Peoples R China
关键词
Silicalite-1; membrane; Two silicon source; Secondary growth; Pervaporation; ZEOLITE MEMBRANES; SEPARATION; MIXTURES; IMPROVEMENT; PERMEATION; EXTRACTION; PARAMETERS;
D O I
10.1016/j.seppur.2010.10.021
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Silicalite-1 membranes supported on macroporous alumina (alpha-Al2O3) tubes for pervaporation were successfully prepared by introducing ethyl triethoxysilane (ETES) during the preparation of synthesis solutions. The effects of synthesis parameters (i.e., FETES] content, crystallization time, and crystallization temperature) on the membranes thickness and pervaporation performance were investigated for silicalite-1 membranes grown onto seeded supports. The as-synthesized membranes were characterized by X-ray diffraction (XRD), scanning electron microscopy (SEM) and pervaporation testing. The results indicated that the as-synthesized membranes were typical MFI-type zeolite membranes and the ETES promoted the crystal growth of the silicalite-1 membranes. The optimum molar composition (1TEOS:0.17TPAOH:120H(2)O:[0.02-0.04]ETES:4EtOH), more than 16h crystallization time at low-temperature (413K) was better for obtaining a dense and continuous silicalite-1 membranes with a good pervaporation performance. The M-3 membrane shows a relatively low selectivity for ethanol/water system but a high selectivity for acetone/water and butanol/water systems. The total fluxes of the M-3 membrane were 1.55, 0.10, and 1.51 kg m(-2) h(-1) towards acetone/H2O, butanol/H2O and ethanol/H2O mixtures, respectively for 3 wt.% acetone/water, 2 wt.% butanol/water and 5 wt.% ethanol/water mixture, respectively and the corresponding separation factor was 211, 150, and 39, respectively. (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:308 / 315
页数:8
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