Basumatary Ashim Kumar, Kumar R Vinoth, Ghoshal Aloke Kumar, Pugazhenthi G
Department of Chemical Engineering, Indian Institute of Technology Guwahati, Guwahati 781039, Assam, India.
Department of Chemical Engineering, Indian Institute of Technology Guwahati, Guwahati 781039, Assam, India.
Chemosphere. 2016 Jun;153:436-46. doi: 10.1016/j.chemosphere.2016.03.077. Epub 2016 Mar 28.
This work describes the removal of Cr (VI) from aqueous solution in cross flow mode using MCM-41, MCM-48 and FAU zeolite membranes prepared on circular shaped porous ceramic support. Ceramic support was manufactured using locally available clay materials via a facile uni-axial compaction method followed by sintering process. A hydrothermal technique was employed for the deposition of zeolites on the ceramic support. The porosity of ceramic support (47%) is reduced by the formation of MCM-41 (23%), MCM-48 (22%) and FAU (33%) zeolite layers. The pore size of the MCM-41, MCM-48 and FAU membrane is found to be 0.173, 0.142, and 0.153 μm, respectively, which is lower than that of the support (1.0 μm). Cross flow ultrafiltration experiments of Cr (VI) were conducted at five different applied pressures (69-345 kPa) and three cross flow rates (1.11 × 10(-7) - 2.22 × 10(-7) m(3)/s). The filtration studies inferred that the performance of the fabricated zeolite composite membranes is optimum at the maximum applied pressure (345 kPa) and the highest rejection is obtained with the lowest cross flow rate (1.11 × 10(-7) m(3)/s) for all three zeolite membrane. The permeate flux of MCM-41, MCM-48 and FAU zeolite composite membranes are almost remained constant in the entire duration of the separation process. The highest removal of 82% is shown by FAU membrane, while MCM-41 and MCM-48 display 75% and 77% of Cr (VI) removal, respectively for the initial feed concentration of 1000 ppm with natural pH of the solution at an applied pressure of 345 kPa.
本工作描述了使用在圆形多孔陶瓷载体上制备的MCM - 41、MCM - 48和FAU沸石膜以错流模式从水溶液中去除Cr(VI)的过程。陶瓷载体是使用当地可得的粘土材料通过简便的单轴压实法然后烧结工艺制造的。采用水热技术在陶瓷载体上沉积沸石。陶瓷载体的孔隙率(47%)因形成MCM - 41(23%)、MCM - 48(22%)和FAU(33%)沸石层而降低。发现MCM - 41、MCM - 48和FAU膜的孔径分别为0.173、0.142和0.153μm,低于载体的孔径(1.0μm)。在五个不同的施加压力(69 - 345 kPa)和三个错流速率(1.11×10⁻⁷ - 2.22×10⁻⁷ m³/s)下进行了Cr(VI)的错流超滤实验。过滤研究推断,所制备的沸石复合膜在最大施加压力(345 kPa)下性能最佳,对于所有三种沸石膜,在最低错流速率(1.11×10⁻⁷ m³/s)下获得最高截留率。在整个分离过程中,MCM - 41、MCM - 48和FAU沸石复合膜的渗透通量几乎保持恒定。对于初始进料浓度为1000 ppm、溶液自然pH值且施加压力为345 kPa的情况,FAU膜显示出最高去除率82%,而MCM - 41和MCM - 48对Cr(VI)的去除率分别为75%和77%。