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Bibliographic Data
001
309805
005
20150706092923.AM
008
150706s |||||||||b ||00|||
040
##
$aSTII-DOST
090
##
$aScienceDirect
100
1#
$a Chung Lim Law
100
1#
$aMei Fong Chong
100
1#
$aYi Jing Chan
245
00
$aBiological treatment of anaerobically digested palm oil mill effluent (POME) using a Lab-Scale Sequencing Batch Reactor (SBR)$cby Yi Jing Chan, Mei Fong Chong and Chung Lim Law
260
##
$aAmsterdam$bElsevier Ltd.$c2010
300
##
$apages 1738-1746$bcomputer file; text; 534kb
504
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$aIncludes bibliographical references
520
3#
$aThe production of highly polluting palm oil mill effluent (POME) has resulted in serious environmental hazards. While anaerobic digestion is widely accepted as an effective method for the treatment of POME, anaerobic treatment of POME alone has difficulty meeting discharge limits due to the high organic strength of POME. Hence, subsequent post-treatment following aerobic treatment is vital to meet the discharge limits. The objective of the present study is to investigate the aerobic treatment of anaerobically digested POME by using a sequencing batch reactor (SBR). The SBR performance was assessed by measuring Chemical Oxygen Demand (COD), Biochemical Oxygen Demand (BOD) and Total Suspended Solids (TSS) removal as well as Sludge Volume Index (SVI). The operating pH and dissolved oxygen concentrations were found to be 8.25-9.14 and 1.5-6.4 mg/L, respectively, throughout the experiment. The experimental results demonstrate that MLVSS, OLR and sludge loading rate (SLR) play a significant role in the organic removal efficiency of SBR systems and therefore, further investigation on these parameters was conducted to attain optimum SBR performance. Maximum COD (95-96%), BOD (97-98%) and TSS (98-99%) removal efficiencies were achieved at optimum OLR, SLR and MLVSS concentration ranges of 1.8-4.2 kg COD/m(3)day, 2.5-4.6 kg TSS/m(3)day and 22,000-25,000 mg/L, respectively. The effluent quality remained stable and complied with the discharge limit. At the same time, the sludge showed good settling properties with average SVI of 65. It is envisaged that the SBR process could complement the anaerobic treatment to produce final treated effluent which meets the discharge limit.
650
04
$aEcology
650
04
$aEnvironmental Remediation$xMethods
650
04
$aPlant Oil$xMetabolism
650
04
$aWaste Disposal$xFluid$vMethos
852
##
$aDOST$bSTII$hScienceDirect$jNONPRINTS$kNP$p13-14777$t1$x13-14777$yOnline/Download$12010-12-01
991
##
$wNONPRINTS
Physical Location
Department of Science and Technology
Science and Technology Information Institute
ScienceDirect
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