Efficiencies of residual organic pollutants removal from secondary effluent by switching of coagulation- air flotation -filtration processes
It is an essential task to remove the residual organic pollutants (ROP) from secondary effluent of a Wastewater Treatment Plant (WWTP) in wastewater reclamation and reuse processes. Four different compared flow schemes would be achieved for further purification of the secondary effluent by switching...
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| Veröffentlicht in: | Water science and technology 2006-01, Vol.54 (11-12), p.215-224 |
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| creator | Huang, R Zhang, J Ma, L Jiang, A Kong, X J Li, X K Bao, L |
| description | It is an essential task to remove the residual organic pollutants (ROP) from secondary effluent of a Wastewater Treatment Plant (WWTP) in wastewater reclamation and reuse processes. Four different compared flow schemes would be achieved for further purification of the secondary effluent by switching of different valves. In order to mainly remove non-biodegradable residual organic pollutants under various operating conditions, the optimum technology and economic process was obtained in the advanced purification flow scheme at a flow of 3200 m(3)/d in Harbin Wenchang WWTP. Conclusions under a lot of experiments show that: choosing the coagulation-settler plus biofilm filter for advanced purification process is reasonable; during the stable operation phase, this process showed good performance in removing the COD, BOD5, TP, NH3-N and SS; the removal rates are 50%, 39%, 67%, 50%, 80% respectively. The effluent is able to excel the requirements for wastewater reuse standards. The unit cost of the water is 0.542 yuan/m(3), which is far below the fee paid for supply water, long-distance transfer water or seawater desalination through economic analysis. |
| doi_str_mv | 10.2166/wst.2006.850 |
| format | Article |
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Four different compared flow schemes would be achieved for further purification of the secondary effluent by switching of different valves. In order to mainly remove non-biodegradable residual organic pollutants under various operating conditions, the optimum technology and economic process was obtained in the advanced purification flow scheme at a flow of 3200 m(3)/d in Harbin Wenchang WWTP. Conclusions under a lot of experiments show that: choosing the coagulation-settler plus biofilm filter for advanced purification process is reasonable; during the stable operation phase, this process showed good performance in removing the COD, BOD5, TP, NH3-N and SS; the removal rates are 50%, 39%, 67%, 50%, 80% respectively. The effluent is able to excel the requirements for wastewater reuse standards. The unit cost of the water is 0.542 yuan/m(3), which is far below the fee paid for supply water, long-distance transfer water or seawater desalination through economic analysis.</description><identifier>ISSN: 0273-1223</identifier><identifier>ISBN: 184339586X</identifier><identifier>ISBN: 9781843395867</identifier><identifier>EISSN: 1996-9732</identifier><identifier>DOI: 10.2166/wst.2006.850</identifier><identifier>PMID: 17302323</identifier><language>eng</language><publisher>England: IWA Publishing</publisher><subject>Ammonia ; Ammonia - analysis ; Ammonia - isolation & purification ; Biodegradability ; Biodegradation ; Biofilms ; Chemical analysis ; Coagulation ; Conservation of Natural Resources ; Desalination ; Drug Residues - analysis ; Economic analysis ; Economics ; Effluents ; Filtration ; Flotation ; Organic Chemicals - analysis ; Pollutants ; Purification ; Reclamation ; Removal ; Seawater ; Switching ; Waste Disposal, Fluid - instrumentation ; Waste Disposal, Fluid - methods ; Wastewater ; Wastewater renovation ; Wastewater reuse ; Wastewater treatment ; Wastewater treatment plants ; Water - analysis ; Water desalting ; Water purification ; Water reclamation ; Water reuse ; Water treatment plants</subject><ispartof>Water science and technology, 2006-01, Vol.54 (11-12), p.215-224</ispartof><rights>Copyright IWA Publishing Dec 2006</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,776,780,27901,27902</link.rule.ids><backlink>$$Uhttps://www.ncbi.nlm.nih.gov/pubmed/17302323$$D View this record in MEDLINE/PubMed$$Hfree_for_read</backlink></links><search><contributor>Kroiss, H</contributor><creatorcontrib>Huang, R</creatorcontrib><creatorcontrib>Zhang, J</creatorcontrib><creatorcontrib>Ma, L</creatorcontrib><creatorcontrib>Jiang, A</creatorcontrib><creatorcontrib>Kong, X J</creatorcontrib><creatorcontrib>Li, X K</creatorcontrib><creatorcontrib>Bao, L</creatorcontrib><title>Efficiencies of residual organic pollutants removal from secondary effluent by switching of coagulation- air flotation -filtration processes</title><title>Water science and technology</title><addtitle>Water Sci Technol</addtitle><description>It is an essential task to remove the residual organic pollutants (ROP) from secondary effluent of a Wastewater Treatment Plant (WWTP) in wastewater reclamation and reuse processes. Four different compared flow schemes would be achieved for further purification of the secondary effluent by switching of different valves. In order to mainly remove non-biodegradable residual organic pollutants under various operating conditions, the optimum technology and economic process was obtained in the advanced purification flow scheme at a flow of 3200 m(3)/d in Harbin Wenchang WWTP. Conclusions under a lot of experiments show that: choosing the coagulation-settler plus biofilm filter for advanced purification process is reasonable; during the stable operation phase, this process showed good performance in removing the COD, BOD5, TP, NH3-N and SS; the removal rates are 50%, 39%, 67%, 50%, 80% respectively. The effluent is able to excel the requirements for wastewater reuse standards. The unit cost of the water is 0.542 yuan/m(3), which is far below the fee paid for supply water, long-distance transfer water or seawater desalination through economic analysis.</description><subject>Ammonia</subject><subject>Ammonia - analysis</subject><subject>Ammonia - isolation & purification</subject><subject>Biodegradability</subject><subject>Biodegradation</subject><subject>Biofilms</subject><subject>Chemical analysis</subject><subject>Coagulation</subject><subject>Conservation of Natural Resources</subject><subject>Desalination</subject><subject>Drug Residues - analysis</subject><subject>Economic analysis</subject><subject>Economics</subject><subject>Effluents</subject><subject>Filtration</subject><subject>Flotation</subject><subject>Organic Chemicals - analysis</subject><subject>Pollutants</subject><subject>Purification</subject><subject>Reclamation</subject><subject>Removal</subject><subject>Seawater</subject><subject>Switching</subject><subject>Waste Disposal, Fluid - 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Chemicals - analysis</topic><topic>Pollutants</topic><topic>Purification</topic><topic>Reclamation</topic><topic>Removal</topic><topic>Seawater</topic><topic>Switching</topic><topic>Waste Disposal, Fluid - instrumentation</topic><topic>Waste Disposal, Fluid - methods</topic><topic>Wastewater</topic><topic>Wastewater renovation</topic><topic>Wastewater reuse</topic><topic>Wastewater treatment</topic><topic>Wastewater treatment plants</topic><topic>Water - analysis</topic><topic>Water desalting</topic><topic>Water purification</topic><topic>Water reclamation</topic><topic>Water reuse</topic><topic>Water treatment plants</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Huang, R</creatorcontrib><creatorcontrib>Zhang, J</creatorcontrib><creatorcontrib>Ma, L</creatorcontrib><creatorcontrib>Jiang, A</creatorcontrib><creatorcontrib>Kong, X J</creatorcontrib><creatorcontrib>Li, X K</creatorcontrib><creatorcontrib>Bao, 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Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Huang, R</au><au>Zhang, J</au><au>Ma, L</au><au>Jiang, A</au><au>Kong, X J</au><au>Li, X K</au><au>Bao, L</au><au>Kroiss, H</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Efficiencies of residual organic pollutants removal from secondary effluent by switching of coagulation- air flotation -filtration processes</atitle><jtitle>Water science and technology</jtitle><addtitle>Water Sci Technol</addtitle><date>2006-01-01</date><risdate>2006</risdate><volume>54</volume><issue>11-12</issue><spage>215</spage><epage>224</epage><pages>215-224</pages><issn>0273-1223</issn><eissn>1996-9732</eissn><isbn>184339586X</isbn><isbn>9781843395867</isbn><abstract>It is an essential task to remove the residual organic pollutants (ROP) from secondary effluent of a Wastewater Treatment Plant (WWTP) in wastewater reclamation and reuse processes. Four different compared flow schemes would be achieved for further purification of the secondary effluent by switching of different valves. In order to mainly remove non-biodegradable residual organic pollutants under various operating conditions, the optimum technology and economic process was obtained in the advanced purification flow scheme at a flow of 3200 m(3)/d in Harbin Wenchang WWTP. Conclusions under a lot of experiments show that: choosing the coagulation-settler plus biofilm filter for advanced purification process is reasonable; during the stable operation phase, this process showed good performance in removing the COD, BOD5, TP, NH3-N and SS; the removal rates are 50%, 39%, 67%, 50%, 80% respectively. The effluent is able to excel the requirements for wastewater reuse standards. The unit cost of the water is 0.542 yuan/m(3), which is far below the fee paid for supply water, long-distance transfer water or seawater desalination through economic analysis.</abstract><cop>England</cop><pub>IWA Publishing</pub><pmid>17302323</pmid><doi>10.2166/wst.2006.850</doi><tpages>10</tpages></addata></record> |
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| ispartof | Water science and technology, 2006-01, Vol.54 (11-12), p.215-224 |
| issn | 0273-1223 1996-9732 |
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| source | MEDLINE; Elektronische Zeitschriftenbibliothek - Frei zugängliche E-Journals |
| subjects | Ammonia Ammonia - analysis Ammonia - isolation & purification Biodegradability Biodegradation Biofilms Chemical analysis Coagulation Conservation of Natural Resources Desalination Drug Residues - analysis Economic analysis Economics Effluents Filtration Flotation Organic Chemicals - analysis Pollutants Purification Reclamation Removal Seawater Switching Waste Disposal, Fluid - instrumentation Waste Disposal, Fluid - methods Wastewater Wastewater renovation Wastewater reuse Wastewater treatment Wastewater treatment plants Water - analysis Water desalting Water purification Water reclamation Water reuse Water treatment plants |
| title | Efficiencies of residual organic pollutants removal from secondary effluent by switching of coagulation- air flotation -filtration processes |
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