Performance study of mullite and mullite-alumina ceramic MF membranes for oily wastewaters treatment

被引:162
作者
Abbasi, Mohsen [1 ]
Mirfendereski, Mojtaba [1 ]
Nikbakht, Mandi [1 ]
Golshenas, Meysam [1 ]
Mohammadi, Toraj [1 ]
机构
[1] Iran Univ Sci & Technol, Res Ctr Membrane Separat Proc, Fac Chem Engn, Tehran, Iran
关键词
Ceramic membranes; Oil-in-water emulsions; Fouling; Rejection; Wastewater treatment; WASTE-WATER TREATMENT; CROSS-FLOW MICROFILTRATION; ULTRAFILTRATION; SEPARATION; FILTRATION; EMULSIONS; REMOVAL;
D O I
10.1016/j.desal.2010.04.013
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this paper, results of an experimental study on separation of oil from actual and synthetic oily wastewaters with mullite and mullite-alumina tubular ceramic membranes are presented. Mullite and mullite-alumina microfiltration (MF) symmetric membranes were synthesized from kaolin clay and alpha-alumina powder. The effects of different operating parameters such as pressure (0.5-4 bar), cross flow velocity (0-2 m/s), temperature (15-55 degrees C), oil concentration (250-3000 ppm) and salt concentration (0-200 g/L) on permeation flux (PF), fouling resistance (FR), fouling and rejection (R) of mullite and mullite-alumina membranes for treatment of synthetic wastewaters were investigated. In order to determine the best operating conditions, 250-3000 ppm condensate gas in water emulsions was employed as synthetic oily wastewaters using mullite membrane. At the best operating conditions (3 bar pressure, 1.5 m/s cross flow velocity and 35 degrees C temperature), performance of mullite and mullite-alumina membranes for treatment of real and synthetic wastewaters were also compared. The results for treatment of emulsions showed that the mullite ceramic membrane has the highest R (93.8%) and the lowest FR (28.97%). Also, the mullite-alumina ceramic membrane with 75% alumina performs high PF (244 L/m(2) h) and low R (81.3%). Also for all the membranes, R for the real wastewater is lower than that for the synthetic wastewaters. (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:169 / 178
页数:10
相关论文
共 35 条
[21]   Crossflow microfiltration of oily water [J].
Mueller, J ;
Cen, YW ;
Davis, RH .
JOURNAL OF MEMBRANE SCIENCE, 1997, 129 (02) :221-235
[22]   Effects of pore size on separation mechanisms of microfiltration of oily water, using porous glass tubular membrane [J].
Ohya, H ;
Kim, JJ ;
Chinen, A ;
Aihara, M ;
Semenova, SI ;
Negishi, Y ;
Mori, O ;
Yasuda, M .
JOURNAL OF MEMBRANE SCIENCE, 1998, 145 (01) :1-14
[23]   Permeate flux decline during UF of oily wastewater: Experimental and modeling [J].
Salahi, Abdolhamid ;
Abbasi, Mohsen ;
Mohammadi, Toraj .
DESALINATION, 2010, 251 (1-3) :153-160
[24]   Oily wastewater treatment using ultrafiltration [J].
Salahi, Abdolhamid ;
Mohammadi, Toraj ;
Pour, Ali Rahmat ;
Rekabdar, Fatemeh .
DESALINATION AND WATER TREATMENT, 2009, 6 (1-3) :289-298
[25]   Intensified membrane filtration with corrugated membranes [J].
Scott, K ;
Mahmood, AJ ;
Jachuck, RJ ;
Hu, B .
JOURNAL OF MEMBRANE SCIENCE, 2000, 173 (01) :1-16
[26]   Separation of nutmeg essential oil and dense CO2 with a cellulose acetate reverse osmosis membrane [J].
Spricigo, CB ;
Bolzan, A ;
Machado, RAF ;
Carlson, LHC ;
Petrus, JCC .
JOURNAL OF MEMBRANE SCIENCE, 2001, 188 (02) :173-179
[27]   Unstable secondary oil water emulsion treatment using ultrafiltration: fouling control by backflushing [J].
Srijaroonrat, P ;
Julien, E ;
Aurelle, Y .
JOURNAL OF MEMBRANE SCIENCE, 1999, 159 (1-2) :11-20
[28]   Demulsification of water-in-oil emulsion by using porous glass membrane [J].
Sun, DZ ;
Duan, XD ;
Li, WX ;
Zhou, D .
JOURNAL OF MEMBRANE SCIENCE, 1998, 146 (01) :65-72
[29]   Treatment of bilge water using a combination of ultrafiltration and reverse osmosis [J].
Tomaszewska, M ;
Orecki, A ;
Karakulski, K .
DESALINATION, 2005, 185 (1-3) :203-212
[30]   A pilot study of the treatment of waste rolling emulsion using zirconia microfiltration membranes [J].
Wang, P ;
Xu, NP ;
Shi, J .
JOURNAL OF MEMBRANE SCIENCE, 2000, 173 (02) :159-166