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dc.contributor.authorChen, TKen_US
dc.contributor.authorNi, CHen_US
dc.contributor.authorChen, JNen_US
dc.date.accessioned2014-12-08T15:41:27Z-
dc.date.available2014-12-08T15:41:27Z-
dc.date.issued2003en_US
dc.identifier.issn1093-4529en_US
dc.identifier.urihttp://hdl.handle.net/11536/28205-
dc.identifier.urihttp://dx.doi.org/10.1081/ESE-120023346en_US
dc.description.abstractThis research focused on the biological treatment of high-strength organic nitrogen wastewater, and presented the results from the nitrification and denitrification of an actual industrial wastewater using anoxic/aerobic process, The opto-electronic industrial wastewater often contains a significant quantity of organic nitrogen compounds and has a ratio over 95% in organic nitrogen (Org-N) to total nitrogen (T-N). In this study, a 2-stage anoxic/aerobic process was established and evaluated the efficiency of wastewater treatment. Raw wastewater from an actual TFT-LCD manufacturing plant was obtained as the sample for looking into the feasibility of opto-electronic industrial wastewater treatment. After toxicity identification evaluation (TIE) test of raw wastewater, the inhibition was related to organic nitrogen (TMAH, MEA) and unionized ammonia (free ammonia, NH3) with high pH. Therefore, pH control is important for biological treatment of high-strength organic nitrogen industrial wastewater. Besides, hydraulic retention time (HRT) and mixed liquor recycled rate (MLR) were controlled independently to distinguish between the effects of these two factors. Under suitable HRT (> 1.7d) and mixed liquor recycled rate (< 4Q). effluent of Nh(4)-N, No-3-N+NO2-N, and COD can fall below 20mg/L, 30mg/L, and 80 mg/L. The anoxic/aerobic process removed 92-98% of the carbon source, and approximately 80% of TKN, 70% of T-N.en_US
dc.language.isoen_USen_US
dc.subjectbiological treatmenten_US
dc.subjectdenitrificationen_US
dc.subjectindustrial wastewateren_US
dc.subjectnitrificationen_US
dc.titleNitrification-denitrification of opto-electronic industrial wastewater by anoxic/aerobic processen_US
dc.typeArticle; Proceedings Paperen_US
dc.identifier.doi10.1081/ESE-120023346en_US
dc.identifier.journalJOURNAL OF ENVIRONMENTAL SCIENCE AND HEALTH PART A-TOXIC/HAZARDOUS SUBSTANCES & ENVIRONMENTAL ENGINEERINGen_US
dc.citation.volume38en_US
dc.citation.issue10en_US
dc.citation.spage2157en_US
dc.citation.epage2167en_US
dc.contributor.department環境工程研究所zh_TW
dc.contributor.departmentInstitute of Environmental Engineeringen_US
dc.identifier.wosnumberWOS:000185542300016-
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