Hydrophobic mullite ceramic hollow fibre membrane (Hy-MHFM) for seawater desalination via direct contact membrane distillation (DCMD)

被引:33
|
作者
Twibi, Mohamed Farag [1 ,3 ]
Othman, Mohd Hafiz Dzarfan [1 ]
Hubadillah, Siti Khadijah [2 ]
Alftessi, Saber Abdulhamid [1 ,3 ]
Bin Adam, Mohd Ridhwan [1 ]
Ismail, Ahmad Fauzi [1 ]
Rahman, Mukhlis A. [1 ]
Jaafar, Juhana [1 ]
Raji, Yusuf Olabode [1 ]
Abd Aziz, Mohd Haiqal [1 ]
Sokri, Mohd Nazri Bin Mohd [1 ]
Abdullah, Huda [4 ]
Naim, Rosmawati [5 ]
机构
[1] Univ Teknol Malaysia, Adv Membrane Technol Res Ctr AMTEC, Sch Chem & Energy Engn, Skudai 81310, Johor, Malaysia
[2] Univ Utara Malaysia, Sch Technol Management & Logist, Sintok 06010, Kedah, Malaysia
[3] Higher Inst Sci & Technol Soqalkhamis Imsehel, Tripoli, Libya
[4] Univ Kebangsaan Malaysia, Fac Engn & Built Environm, Dept Elect Elect & Syst Engn, Bangi, Selangor, Malaysia
[5] Univ Malaysia Pahang, Fac Chem & Proc Engn Technol, Kuantan 26300, Pahang, Malaysia
关键词
Mullite; Ceramic membrane; Direct contact membrane distillation; Seawater desalination; Hydrophobic membrane; PORE-SIZE DISTRIBUTION; SURFACE MODIFICATION; COMPOSITE MEMBRANE; WATER; SEPARATION; PERFORMANCE; TECHNOLOGY; ALUMINA; ENERGY; CLAY;
D O I
10.1016/j.jeurceramsoc.2021.06.024
中图分类号
TQ174 [陶瓷工业]; TB3 [工程材料学];
学科分类号
0805 ; 080502 ;
摘要
A low-cost hydrophobic mullite hollow fibre membrane (Hy-MHFM) fabricated via phase inversion/sintering technique followed by fluoroalkyl silane (FAS) grafting is presented in this study. The prepared CHFMs were characterized before and after the grafting step using different characterization techniques. The pore size of the CHFM surface was also determined using ImageJ software. The desalination performance of the grafted membrane was evaluated in direct contact membrane distillation (DCMD) using synthetic seawater of varying salt concentrations for 2 h at various feedwater temperatures. The outcome of the evaluations showed declines in the permeate flux of the membrane at increasing feed concentration, as well as increased flux with increased feed temperature. The long-term stability of the membrane was achieved at time 20 h, feed temperature 60 degrees C, and permeate temperature 10 degrees C, the membrane achieved a salt rejection performance of about 99.99 % and a water flux value of 22.51 kg/ m(2)h.
引用
收藏
页码:6578 / 6585
页数:8
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