Titania and zirconia ceramic nanofiltration membrane fabrication by coating method on mullite and mullite-alumina microfiltration supports for industrial wastewater treatment

被引:0
|
作者
Fooladi, Iman [1 ]
Ghanbarizadeh, Parnian [1 ]
Azari, Ahmad [1 ,2 ]
Abbasi, Mohsen [1 ]
Karami, Rahim [2 ,3 ]
Akrami, Mohammad [1 ,4 ,5 ]
机构
[1] Persian Gulf Univ, Fac Petr Gas & Petrochem Engn, Dept Chem Engn, Bushehr 75169, Iran
[2] Persian Gulf Univ, Oil & Gas Res Ctr, Appl Computat Fluid Dynam Res Grp, Bushehr, Iran
[3] Cent Queensland Univ, Sch Engn & Technol, Rockhampton, Qld 4702, Australia
[4] Univ Exeter, Dept Engn, Exeter EX4 4QF, England
[5] Persian Gulf Univ, Fac Petr Gas & Petrochem Engn FPGPE, Dept Chem Engn, Bushehr 75169, Iran
关键词
Multilayer ceramic membrane; Mullite; Mullite-alumina; Nanofiltration; Titania-Zirconia; Sol-gel; SOL-GEL PROCESS; RETENTION PROPERTIES; PERFORMANCE;
D O I
10.1016/j.arabjc.2024.105973
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Industrial wastewater treatment increasingly relies on membrane separation, with ceramic membranes offering many advantages such as thermal stability and pH resistance. The resistance of ceramic membranes to extreme pH conditions indicates their ability to maintain structure and performance when exposed to highly acidic or alkaline environments. A high-permeability ceramic nanofiltration membrane was developed, boasting excellent rejection rates through a multilayer asymmetric design. Initially, two tubular porous supports, mullite and mullite-alumina, with a weight percent of 50, were fabricated using the extrusion method. Subsequently, a colloidal sol of titania (TiO2) and titania-zirconia (TiO2- ZrO2) was prepared via the sol-gel method and coated on the ceramic supports using the dip-coating method. After analyzing the membrane microstructure using SEM, XRD, and BET, the efficiency of the membranes in treating synthetic oily wastewater was evaluated. The results underscore the significant impact of the Donnan exclusion mechanism on the rejection of nanofiltration (NF) membranes. An increase in pressure led to a rise in rejection rates up to 7 bars. The Chemical Oxygen Demand (COD) rejection for mullite-titania zirconia (MTZ) and mullite-alumina-titania zirconia (MATZ) membranes was 98.65 % and 98 %, respectively. The pure water permeability test results for mullite and mullite-alumina supports, as well as MTZ and MATZ membranes, were recorded as 254, 382, 70, and 89 L bar-1m-2h- 1, respectively.
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页数:11
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