Preparation, characterization and application of powdered activated carbon-cellulose acetate phthalate mixed matrix membrane for treatment of steel plant effluent

被引:15
作者
Mukherjee, Raka [1 ]
De, Sirshendu [1 ]
机构
[1] Indian Inst Technol, Dept Chem Engn, Kharagpur 721302, W Bengal, India
关键词
powdered activated carbon; mixed matrix membrane; phenolic compounds; breakthrough time; PHENOLIC-COMPOUNDS; WASTE-WATER; GAS SEPARATION; REMOVAL; ADSORPTION; POLYSULFONE; ULTRAFILTRATION; PERFORMANCE; ADSORBENTS; POLYMER;
D O I
10.1002/pat.3690
中图分类号
O63 [高分子化学(高聚物)];
学科分类号
070305 ; 080501 ; 081704 ;
摘要
Preparation, characterization and industrial application of a mixed matrix membrane (MMM) using powdered activated carbon (PAC) in cellulose acetate phthalate (CAP) have been reported in this study. The objective of this work is to fabricate a less energy intensive, highly selective (to phenolic compounds) adsorptive membrane with high throughput in a scalable platform for simultaneous removal of organic as well chemical oxygen demand (COD) from a steel plant effluent. The membrane with 25wt% PAC has maximum adsorption capacity of phenol 35mg/g at pH5.5. Effluent with total phenolic compounds (23mg/g) and COD of 5200mg/l is treated in continuous cross-flow configuration. Breakthrough time is 44hr for a filtration area of 0.008m(2) with total phenol concentration in permeate as per World Health Organization (WHO), 1mg/l. Throughput of the system is high, 40l/m(2)hr at transmembrane pressure drop 276kPa and cross-flow rate 20l/hr. Maximum rejection of phenol is obtained at low pressure and cross-flow rate. Removal of phenolic compounds is achieved by adsorption by PAC in CAP matrix and satisfactory reduction of COD and complete removal of non-volatile solids are due of sieving mechanism. A simple chemical regeneration method is proposed to recover the permeate flux beyond 90%. Copyright (c) 2015 John Wiley & Sons, Ltd.
引用
收藏
页码:444 / 459
页数:16
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