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dc.contributor.authorTsai, Jen-Chiehen_US
dc.contributor.authorKumar, Mathavaen_US
dc.contributor.authorChen, Shen-Yien_US
dc.contributor.authorLin, Jih-Gawen_US
dc.date.accessioned2014-12-08T15:13:00Z-
dc.date.available2014-12-08T15:13:00Z-
dc.date.issued2007-12-01en_US
dc.identifier.issn1383-5866en_US
dc.identifier.urihttp://dx.doi.org/10.1016/j.seppur.2007.07.022en_US
dc.identifier.urihttp://hdl.handle.net/11536/10032-
dc.description.abstractThe feasibility of nano-bubble flotation technology (NBFT) with coagulation/flocculation process for the enhanced treatment of chemical mechanical polishing (CMP) wastewater was investigated through laboratory and pilot-scale experiments. As a precursor, the effective combination of activator/collector was identified using a laboratory-scale flotation reactor. The results showed that polyaluminum chloride (PAC)/sodium oleate (NaOl) was the best combination of activator/collector, respectively and its application in the NBFT with coagulation process increased the wastewater clarification efficiency by 40% as compared with traditional coagulation/flocculation process. More than 95% turbidity, total solids and total silica removal efficiencies were observed in the pilot-scale flotation experiments. From the results, it was found that NBFT with coagulation process could be performed effectively at an optimum PAC concentration of 50-60 mg/L (as Al), NaOl concentration of 5-10 mg/L with a recycle ratio of 10-20% and I h hydraulic retention time HRT. The cost and performance assessment reflected that CMP wastewater could be treated efficiently at a minimum cost using the present approach. (c) 2007 Elsevier B.V. All rights reserved.en_US
dc.language.isoen_USen_US
dc.subjectchemical mechanical polishingen_US
dc.subjectcoagulationen_US
dc.subjectflotationen_US
dc.subjectnano-bubbleen_US
dc.subjectresponse surface methodologyen_US
dc.titleNano-bubble flotation technology with coagulation process for the cost-effective treatment of chemical mechanical polishing wastewateren_US
dc.typeArticleen_US
dc.identifier.doi10.1016/j.seppur.2007.07.022en_US
dc.identifier.journalSEPARATION AND PURIFICATION TECHNOLOGYen_US
dc.citation.volume58en_US
dc.citation.issue1en_US
dc.citation.spage61en_US
dc.citation.epage67en_US
dc.contributor.department環境工程研究所zh_TW
dc.contributor.departmentInstitute of Environmental Engineeringen_US
dc.identifier.wosnumberWOS:000251183500011-
dc.citation.woscount16-
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