Reverse Osmosis Performance of Organosilica Membranes and Comparison with the Pervaporation and Gas Permeation Properties

被引:54
作者
Xu, Rong [1 ]
Wang, Jinhui [1 ]
Kanezashi, Masakoto [1 ]
Yoshioka, Tomohisa [1 ]
Tsuru, Toshinori [1 ]
机构
[1] Hiroshima Univ, Dept Chem Engn, Higashihiroshima 7398527, Japan
基金
日本科学技术振兴机构;
关键词
reverse osmosis; membrane; organosilica; solution-diffusion model; pervaporation; HYDROGEN SEPARATION MEMBRANES; MICROPOROUS SILICA; NANOFILTRATION MEMBRANES; HYDROTHERMAL STABILITY; VAPOR PERMEATION; WATER; TEMPERATURE; TRANSPORT; MODEL; DESALINATION;
D O I
10.1002/aic.13885
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Hybrid organosilica membranes were successfully prepared using bis(triethoxysilyl)ethane (BTESE) and applied to reverse osmosis (RO) desalination. The organosilica membrane calcined at 300 degrees C almost completely rejected salts and neutral solutes with low-molecular-weight. Increasing the operating pressure led to an increase in water flux and salt rejection, while the flux and rejection decreased as salt concentration increased. The water permeation mechanism differed from the viscous flow mechanism. Observed activation energies for permeation were larger for membranes with a smaller pore size, and were considerably larger than the activation energy for water viscosity. The organosilica membranes exhibited exceptional hydrothermal stability in temperature cycles up to 90 degrees C. The applicability of the generalized solution-diffusion (SD) model to RO and pervaporation (PV) desalination processes were examined, and the quantitative differences in water permeance were accurately predicted by the application of generalized transport equations. (C) 2012 American Institute of Chemical Engineers AIChE J, 59: 1298-1307, 2013
引用
收藏
页码:1298 / 1307
页数:10
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