Pervaporation performance of surface-modified zeolite/PU mixed matrix membranes for separation of phenol from water

被引:17
|
作者
Ye, Hong [1 ,2 ]
Zhang, Xiang [1 ]
Zhao, Zixuan [1 ]
Song, Boyu [3 ]
Zhang, Zhongguo [3 ]
Song, Weiwei
机构
[1] Beijing Technol & Business Univ, Beijing Engn & Technol Res Ctr Food Addit, Beijing 100048, Peoples R China
[2] Beijing Technol & Business Univ, Beijing Higher Inst Engn Res Ctr Food Addit & Ing, Beijing 100048, Peoples R China
[3] Beijing Acad Sci & Technol, Environm Protect Res Inst Light Ind, Beijing 100089, Peoples R China
基金
中国国家自然科学基金; 北京市自然科学基金;
关键词
Pervaporation; ZSM-5; Polyurethane; Modification; Membrane; DILUTE AQUEOUS-SOLUTIONS; WASTE-WATER; CO2/CH4; SEPARATION; CO2; PU MEMBRANES; ADSORPTION; REMOVAL; DEGRADATION; POLYURETHANEUREA; NANOPARTICLES;
D O I
10.1007/s13726-017-0509-1
中图分类号
O63 [高分子化学(高聚物)];
学科分类号
070305 ; 080501 ; 081704 ;
摘要
Polyurethane (PU) is a kind of promising pervaporation membrane material and silica-rich zeolite is a potential modifier to PU, but the pristine zeolite particles suffer from the bad dispersion in the polymer. This work presents a new route to modify zeolite (ZSM-5) particles via bridging with isocyanate to prepare a membrane for the recovery of phenol from the water. Zeolite ZSM-5 particles were successfully grafted by TDI, beta-cyclodextrin, and oleyl alcohol, consecutively. The corresponding zeolites filled PU membranes were prepared and characterized by FTIR, TGA and SEM techniques. The effects of the grafted structures on the pervaporation performances of the zeolites/ PU membranes were investigated in the recovery of phenol from the water. The results showed that the modified ZSM-5 particles had a good dispersion in PU, while the pristine ones demonstrated an obvious sedimentation. The modified zeolite/polyurethane membranes achieved better comprehensive separation performance than the neat PU and pristine ZSM-5 modified PU membranes. Depending on the good affinity of the a-cyclodextrin to phenol, ZSM-5 particles grafted by toluene diisocyanate and beta-cyclodextrin (ZSM-TC) showed the optimal separation performance with the flux of 46.03 kg mu m m(-2) h(-1) and the separation factor of 15.64 for the 0.3 wt% aqueous phenol solution at 80 degrees C. With the increase in the zeolite loading from 5 to 25%, ZSM-5/PU membrane showed the decreased separation factor and flux comparing to the neat PU. However, ZSM-TC/PU membrane showed higher flux and better selectivity than the neat PU and pristine ZSM-5 filled PU membranes.
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页码:193 / 203
页数:11
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