Tackling colour issue of anaerobically-treated palm oil mill effluent using membrane technology

被引:42
|
作者
Amat, N. A. Ali [1 ]
Tan, Y. H. [1 ]
Lau, W. J. [1 ]
Lai, G. S. [1 ]
Ong, C. S. [2 ]
Mokhtar, N. M. [3 ]
Sani, N. A. A. [1 ]
Ismail, A. F. [1 ]
Goh, P. S. [1 ]
Chong, K. C. [4 ]
Lai, S. O. [4 ]
机构
[1] Univ Teknol Malaysia, Adv Membrane Technol Res Ctr AMTEC, Skudai 81310, Johor, Malaysia
[2] SEGi Univ, Fac Engn & Built Environm, Discipline Chem Engn, Petaling Jaya 47810, Selangor, Malaysia
[3] Univ Malaysia Pahang, Fac Engn Technol, Gambang 26300, Pahang, Malaysia
[4] Univ Tunku Abdul Rahman, Lee Kong Chian Fac Engn & Sci, Dept Chem Engn, Kajang 43000, Selangor, Malaysia
关键词
Palm oil mill effluent; Colour; Membrane; Fouling; Cleaning;
D O I
10.1016/j.jwpe.2015.10.010
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
In this work, the performances of membranes with different properties were evaluated for their capabilities in treating anaerobically-treated palm oil mill effluent (AT-POME). Unlike raw POME, AT-POME is the effluent that has been biologically treated to reduce mainly the organic compounds present in the effluent. The treated effluent however still demonstrates brownish by the time it is discharged to receiving water bodies. The samples treated by membranes were assessed with respect to two colour parameters, i.e. absorbance at 370 nm wavelength and ADMI value. Other parameters also considered were total organic carbon (TOC) and total nitrogen (TN). Results showed that nanofiltration membrane (NF270) always demonstrated greater colour removal efficiencies in comparison to ultrafiltration membranes (UF 10 kDa and UF 30kDa). The NF270 membrane achieved 97.4-97.9% colour removal compared to 72.4-75.4% and 48.1-50.5% shown by UF 10 kDa and UF 30 kDa, respectively. Further sample quality analyses revealed that NF membrane could achieve higher TOC and TN removal than those of UF membranes. Although NF membrane demonstrated excellent separation, its performance was compromised by low water flux (6.58 L/m(2) h at 10 bar). Since the treated effluent is not targeted for reuse, employing UF 10 kDa membrane with reasonably good rejection rate coupled high water flux (9.66 L/m(2) h at 5 bar) is considered good enough to meet the discharged requirements. Further investigations have shown that UF 10 kDa membrane is less susceptible to fouling when it is operated at low pressure and for the fouled membrane, chemical cleaning could be employed to retrieve water flux. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:221 / 226
页数:6
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