Pretreatment of silk-dyeing industrial wastewater by UASB reactor

The objective of this study was to investigate the performance of the upflow anaerobic sludge blanket (UASB) reactor as the pretreatment system for silk-dyeing wastewater. Two laboratory-scale UASB reactors, with working volume of 15.59 I, were used during May 1998 to June 1999. The actual wastewate...

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Main Authors: Karnchanawong S., Sawangpanyangkura T.
Format: Article
Language:English
Published: 2014
Online Access:http://www.scopus.com/inward/record.url?eid=2-s2.0-8844285957&partnerID=40&md5=1a58d5b9680ccb1010d29cac0ba39c9c
http://www.ncbi.nlm.nih.gov/pubmed/15566202
http://cmuir.cmu.ac.th/handle/6653943832/1507
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Institution: Chiang Mai University
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spelling th-cmuir.6653943832-15072014-08-29T09:29:24Z Pretreatment of silk-dyeing industrial wastewater by UASB reactor Karnchanawong S. Sawangpanyangkura T. The objective of this study was to investigate the performance of the upflow anaerobic sludge blanket (UASB) reactor as the pretreatment system for silk-dyeing wastewater. Two laboratory-scale UASB reactors, with working volume of 15.59 I, were used during May 1998 to June 1999. The actual wastewater was diluted to reduce ammonium ion toxicity on anaerobic bacteria. The experiments were conducted at the organic loading rates (OLRs) of 0.52, 1.01, 1.04, 1.54 and 2.56 kgCOD/(m3.d), treating only wastewater generated from the acid-dye process of mixed-species raw silk. It took approximately 4 1/2 months to reach the steady-state conditions. It was found that the COD removal was in the ranges of 74.1-85.3%, except at OLR 2.56 kgCOD/(m3.d) where efficiency significantly dropped to 55.2%. The apparent color removal was in the similar trend as COD. During the study periods, wastewater input had various color shades while the effluent generally looked pale yellowish. The methane generation rates ranged from 0.18-0.31 m3/kg COD removed, with methane composition 81.0-88.1% in biogas. The average granule size in the sludge bed had slowly increased to 0.73 mm in the last experiment. It can be concluded that the UASB reactor is suitable as a pretreatment system for silk-dyeing wastewater. An OLR of 1 kgCOD/(m3.d) and an influent concentration diluted to 2,600 mgCOD/I are suggested while COD and apparent color removal efficiency of 80% and 70%, respectively, can be expected. © IWA Publishing 2004. 2014-08-29T09:29:24Z 2014-08-29T09:29:24Z 2004 Article 02731223 15566202 WSTED http://www.scopus.com/inward/record.url?eid=2-s2.0-8844285957&partnerID=40&md5=1a58d5b9680ccb1010d29cac0ba39c9c http://www.ncbi.nlm.nih.gov/pubmed/15566202 http://cmuir.cmu.ac.th/handle/6653943832/1507 English
institution Chiang Mai University
building Chiang Mai University Library
country Thailand
collection CMU Intellectual Repository
language English
description The objective of this study was to investigate the performance of the upflow anaerobic sludge blanket (UASB) reactor as the pretreatment system for silk-dyeing wastewater. Two laboratory-scale UASB reactors, with working volume of 15.59 I, were used during May 1998 to June 1999. The actual wastewater was diluted to reduce ammonium ion toxicity on anaerobic bacteria. The experiments were conducted at the organic loading rates (OLRs) of 0.52, 1.01, 1.04, 1.54 and 2.56 kgCOD/(m3.d), treating only wastewater generated from the acid-dye process of mixed-species raw silk. It took approximately 4 1/2 months to reach the steady-state conditions. It was found that the COD removal was in the ranges of 74.1-85.3%, except at OLR 2.56 kgCOD/(m3.d) where efficiency significantly dropped to 55.2%. The apparent color removal was in the similar trend as COD. During the study periods, wastewater input had various color shades while the effluent generally looked pale yellowish. The methane generation rates ranged from 0.18-0.31 m3/kg COD removed, with methane composition 81.0-88.1% in biogas. The average granule size in the sludge bed had slowly increased to 0.73 mm in the last experiment. It can be concluded that the UASB reactor is suitable as a pretreatment system for silk-dyeing wastewater. An OLR of 1 kgCOD/(m3.d) and an influent concentration diluted to 2,600 mgCOD/I are suggested while COD and apparent color removal efficiency of 80% and 70%, respectively, can be expected. © IWA Publishing 2004.
format Article
author Karnchanawong S.
Sawangpanyangkura T.
spellingShingle Karnchanawong S.
Sawangpanyangkura T.
Pretreatment of silk-dyeing industrial wastewater by UASB reactor
author_facet Karnchanawong S.
Sawangpanyangkura T.
author_sort Karnchanawong S.
title Pretreatment of silk-dyeing industrial wastewater by UASB reactor
title_short Pretreatment of silk-dyeing industrial wastewater by UASB reactor
title_full Pretreatment of silk-dyeing industrial wastewater by UASB reactor
title_fullStr Pretreatment of silk-dyeing industrial wastewater by UASB reactor
title_full_unstemmed Pretreatment of silk-dyeing industrial wastewater by UASB reactor
title_sort pretreatment of silk-dyeing industrial wastewater by uasb reactor
publishDate 2014
url http://www.scopus.com/inward/record.url?eid=2-s2.0-8844285957&partnerID=40&md5=1a58d5b9680ccb1010d29cac0ba39c9c
http://www.ncbi.nlm.nih.gov/pubmed/15566202
http://cmuir.cmu.ac.th/handle/6653943832/1507
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