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removal of 1,4-dioxane from polyester manufacturing process wastewater using an up-flow Biological Aerated Filter (UBAF) packed with tire chips

1,4-Dioxane is one of the by-products from the polyester manufacturing process, which has been carelessly discharged into water bodies and is a weak human carcinogen. In this study, a laboratory-scale, up-flow biological aerated filter (UBAF), packed with tire chips, was investigated for the treatme...

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Published in:Journal of environmental science and health. Part A, Toxic/hazardous substances & environmental engineering Toxic/hazardous substances & environmental engineering, 2012, Vol.47 (1), p.117-129
Main Authors: Han, Thi-Hiep, Han, Ji-Sun, So, Myung-Ho, Seo, Jang-Won, Ahn, Chang-Min, Min, Dong Hee, Yoo, Yeon Sun, Cha, Daniel K, Kim, Chang Gyun
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container_title Journal of environmental science and health. Part A, Toxic/hazardous substances & environmental engineering
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creator Han, Thi-Hiep
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Kim, Chang Gyun
description 1,4-Dioxane is one of the by-products from the polyester manufacturing process, which has been carelessly discharged into water bodies and is a weak human carcinogen. In this study, a laboratory-scale, up-flow biological aerated filter (UBAF), packed with tire chips, was investigated for the treatment of 1,4-dioxane. The UBAF was fed with effluent, containing an average of 31 mg/L of 1,4-dioxane, discharged from an anaerobic treatment unit at H Co. in the Gumi Industrial Complex, South Korea. In the batch, a maximum of 99.5 % 1,4-dioxane was removed from an influent containing 25.6 mg/L. In the continuous mode, the optimal empty bed contact time (EBCT) and air to liquid flow rate (A:L) were 8.5 hours and 30:1, respectively. It was also found that the removal efficiency of 1,4-dioxane increased with increasing loading rate within the range 0.04 to 0.31 kg 1,4-dioxane/m³·day. However, as the COD:1,4-dioxane ratio was increased within the range 3 to 46 (mg/L COD)/(mg/L 1,4-dioxane), the removal efficiency unexpectedly decreased.
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However, as the COD:1,4-dioxane ratio was increased within the range 3 to 46 (mg/L COD)/(mg/L 1,4-dioxane), the removal efficiency unexpectedly decreased.</description><identifier>ISSN: 1532-4117</identifier><identifier>ISSN: 1093-4529</identifier><identifier>EISSN: 1532-4117</identifier><identifier>DOI: 10.1080/10934529.2012.630291</identifier><identifier>PMID: 22217090</identifier><language>eng</language><publisher>Philadelphia, PA: Taylor &amp; Francis Group</publisher><subject>1,4-dioxane ; Aerobiosis ; air ; Applied sciences ; Bacteria, Aerobic - classification ; Bacteria, Aerobic - genetics ; Bacteria, Aerobic - metabolism ; Biodegradation ; Biofilms - classification ; biofilters ; Biological Oxygen Demand Analysis ; Bioreactors - microbiology ; byproducts ; Carcinogens ; Chemical compounds ; chemical oxygen demand ; Dioxanes - metabolism ; DNA, Bacterial - genetics ; DNA, Ribosomal - genetics ; Exact sciences and technology ; Filters ; Filtration ; General purification processes ; humans ; Industrial Waste ; manufacturing ; Microscopy, Electron, Scanning ; Oxygen - analysis ; Pollution ; polyester manufacturing process ; Polyesters ; Sewage - microbiology ; surface water ; tires ; up-flow biological aeration filer (UBAF) ; Waste Disposal, Fluid - methods ; wastewater ; Wastewaters ; Water Pollutants, Chemical - metabolism ; Water treatment ; Water treatment and pollution</subject><ispartof>Journal of environmental science and health. 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Part A, Toxic/hazardous substances &amp; environmental engineering</title><addtitle>J Environ Sci Health A Tox Hazard Subst Environ Eng</addtitle><description>1,4-Dioxane is one of the by-products from the polyester manufacturing process, which has been carelessly discharged into water bodies and is a weak human carcinogen. In this study, a laboratory-scale, up-flow biological aerated filter (UBAF), packed with tire chips, was investigated for the treatment of 1,4-dioxane. The UBAF was fed with effluent, containing an average of 31 mg/L of 1,4-dioxane, discharged from an anaerobic treatment unit at H Co. in the Gumi Industrial Complex, South Korea. In the batch, a maximum of 99.5 % 1,4-dioxane was removed from an influent containing 25.6 mg/L. In the continuous mode, the optimal empty bed contact time (EBCT) and air to liquid flow rate (A:L) were 8.5 hours and 30:1, respectively. It was also found that the removal efficiency of 1,4-dioxane increased with increasing loading rate within the range 0.04 to 0.31 kg 1,4-dioxane/m³·day. However, as the COD:1,4-dioxane ratio was increased within the range 3 to 46 (mg/L COD)/(mg/L 1,4-dioxane), the removal efficiency unexpectedly decreased.</description><subject>1,4-dioxane</subject><subject>Aerobiosis</subject><subject>air</subject><subject>Applied sciences</subject><subject>Bacteria, Aerobic - classification</subject><subject>Bacteria, Aerobic - genetics</subject><subject>Bacteria, Aerobic - metabolism</subject><subject>Biodegradation</subject><subject>Biofilms - classification</subject><subject>biofilters</subject><subject>Biological Oxygen Demand Analysis</subject><subject>Bioreactors - microbiology</subject><subject>byproducts</subject><subject>Carcinogens</subject><subject>Chemical compounds</subject><subject>chemical oxygen demand</subject><subject>Dioxanes - metabolism</subject><subject>DNA, Bacterial - genetics</subject><subject>DNA, Ribosomal - genetics</subject><subject>Exact sciences and technology</subject><subject>Filters</subject><subject>Filtration</subject><subject>General purification processes</subject><subject>humans</subject><subject>Industrial Waste</subject><subject>manufacturing</subject><subject>Microscopy, Electron, Scanning</subject><subject>Oxygen - analysis</subject><subject>Pollution</subject><subject>polyester manufacturing process</subject><subject>Polyesters</subject><subject>Sewage - microbiology</subject><subject>surface water</subject><subject>tires</subject><subject>up-flow biological aeration filer (UBAF)</subject><subject>Waste Disposal, Fluid - methods</subject><subject>wastewater</subject><subject>Wastewaters</subject><subject>Water Pollutants, Chemical - metabolism</subject><subject>Water treatment</subject><subject>Water treatment and pollution</subject><issn>1532-4117</issn><issn>1093-4529</issn><issn>1532-4117</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2012</creationdate><recordtype>article</recordtype><recordid>eNqFkt2K1DAcxYso7oe-gWgQFlewYz7b9EpmF0eFBS90rkuaJrNZ26YmrXWewlf2Xzqj4oVehITkdw45OUmSJwSvCJb4NcEF44IWK4oJXWUM04LcS06JYDTlhOT3_1ifJGcx3mFMJCPiYXJCKSU5LvBp8iOY1n9TDfIWkVc8rZ3_rjqDbPAt6n2zN3EwAbWqG63Swxhct0N98NrEiCYFh5OagTHOB6pDY5_axk_oyvnG75wG67UJwNRo45oZvdxerTcvUa_0F9ic3HCLBhcM0reuj4-SB1Y10Tw-zOfJdvP28_X79Objuw_X65tU8zwbUqI5rinTFhvCikrLGleS2UxVBgsrsK1VTQtlCkkpz42UFgvOawIAq4QQ7Dx5sfhClq8jhCxbF7VpGgjvx1gWhGdZgbEE8vKfJMGEwyCiAPT5X-idH0MHOcAvZzyHqgDiC6SDjzEYW_bBtSrswamcmy2PzZZzs-XSLMieHrzHqjX1L9GxSgAuDoCK8Oo2qE67-JsTnGVSznneLJzrrA-tmnxo6nJQ-8aHo4j95yrPFgerfKl2AQTbTwBw-GAZYVSwnxjbyAA</recordid><startdate>2012</startdate><enddate>2012</enddate><creator>Han, Thi-Hiep</creator><creator>Han, Ji-Sun</creator><creator>So, Myung-Ho</creator><creator>Seo, Jang-Won</creator><creator>Ahn, Chang-Min</creator><creator>Min, Dong Hee</creator><creator>Yoo, Yeon Sun</creator><creator>Cha, Daniel K</creator><creator>Kim, Chang Gyun</creator><general>Taylor &amp; 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Part A, Toxic/hazardous substances &amp; environmental engineering</jtitle><addtitle>J Environ Sci Health A Tox Hazard Subst Environ Eng</addtitle><date>2012</date><risdate>2012</risdate><volume>47</volume><issue>1</issue><spage>117</spage><epage>129</epage><pages>117-129</pages><issn>1532-4117</issn><issn>1093-4529</issn><eissn>1532-4117</eissn><abstract>1,4-Dioxane is one of the by-products from the polyester manufacturing process, which has been carelessly discharged into water bodies and is a weak human carcinogen. In this study, a laboratory-scale, up-flow biological aerated filter (UBAF), packed with tire chips, was investigated for the treatment of 1,4-dioxane. The UBAF was fed with effluent, containing an average of 31 mg/L of 1,4-dioxane, discharged from an anaerobic treatment unit at H Co. in the Gumi Industrial Complex, South Korea. In the batch, a maximum of 99.5 % 1,4-dioxane was removed from an influent containing 25.6 mg/L. In the continuous mode, the optimal empty bed contact time (EBCT) and air to liquid flow rate (A:L) were 8.5 hours and 30:1, respectively. It was also found that the removal efficiency of 1,4-dioxane increased with increasing loading rate within the range 0.04 to 0.31 kg 1,4-dioxane/m³·day. However, as the COD:1,4-dioxane ratio was increased within the range 3 to 46 (mg/L COD)/(mg/L 1,4-dioxane), the removal efficiency unexpectedly decreased.</abstract><cop>Philadelphia, PA</cop><pub>Taylor &amp; Francis Group</pub><pmid>22217090</pmid><doi>10.1080/10934529.2012.630291</doi><tpages>13</tpages></addata></record>
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identifier ISSN: 1532-4117
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subjects 1,4-dioxane
Aerobiosis
air
Applied sciences
Bacteria, Aerobic - classification
Bacteria, Aerobic - genetics
Bacteria, Aerobic - metabolism
Biodegradation
Biofilms - classification
biofilters
Biological Oxygen Demand Analysis
Bioreactors - microbiology
byproducts
Carcinogens
Chemical compounds
chemical oxygen demand
Dioxanes - metabolism
DNA, Bacterial - genetics
DNA, Ribosomal - genetics
Exact sciences and technology
Filters
Filtration
General purification processes
humans
Industrial Waste
manufacturing
Microscopy, Electron, Scanning
Oxygen - analysis
Pollution
polyester manufacturing process
Polyesters
Sewage - microbiology
surface water
tires
up-flow biological aeration filer (UBAF)
Waste Disposal, Fluid - methods
wastewater
Wastewaters
Water Pollutants, Chemical - metabolism
Water treatment
Water treatment and pollution
title removal of 1,4-dioxane from polyester manufacturing process wastewater using an up-flow Biological Aerated Filter (UBAF) packed with tire chips
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