Fabrication of industrially feasible zeolite membrane for the removal of hexavalent chromium

被引:0
|
作者
Kumar, R. Vinoth [1 ]
Basumatary, Ashim Kumar [2 ]
Pugazhenthi, G. [3 ]
机构
[1] Natl Inst Technol Andhra Pradesh, Dept Chem Engn, Tadepalligudem 534101, Andhra Pradesh, India
[2] Assam Engn Coll, Dept Chem Engn, Gauhati 781013, Assam, India
[3] Indian Inst Technol Guwahati, Dept Chem Engn, Gauhati 781039, Assam, India
关键词
Faujasite; hydrothermal treatment; zeolite membrane; chromium removal; contact angle; tubular membrane; Indian clays; low-cost membrane; zeta potential; composite membrane; CERAMIC MEMBRANE; ANALCIME-C; COMPOSITE MEMBRANE; SEPARATION; DEHYDRATION; PERFORMANCE; IONS; MICROFILTRATION; SILICALITE-1; SURFACE;
D O I
10.1504/IJESD.2023.133822
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The present study proposed fabricating an industrially feasible zeolite membrane on an indigenously developed inexpensive tubular ceramic substrate. A type of zeolite framework, Faujasite, was deposited on the substrate using source materials, such as alumina and silica, by hydrothermal treatment. The membrane was characterised by XRD, FESEM, zeta potential, and contact angle analyses. Distinguishable physical and structural characteristics of the zeolite membrane from ceramic substrate substantiated a formation of the composite membrane. Further, the potentiality of the membrane was assessed on the removal of hexavalent chromium from synthetic wastewater at various operating parameters in a crossflow system. The prepared membrane offered a maximum chromium removal of 82% with a flux of 5.05 x 10(-5) m(3)m(-2)s(-1) at the operating conditions of 1,000 ppm concentration, 345 kPa pressure, and 1.11 x 10(-6) m(3)s(-1) crossflow rate. The membrane revealed its essential employment by providing a higher flux with better rejection than other membranes applied in chromium removal.
引用
收藏
页码:375 / 392
页数:19
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