Please use this identifier to cite or link to this item: http://nopr.niscpr.res.in/handle/123456789/14529
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dc.contributor.authorDin, M F Md-
dc.contributor.authorHuey, S C-
dc.contributor.authorYunus, S Muhd-
dc.contributor.authorAhmad, M A-
dc.contributor.authorPonraj, M-
dc.contributor.authorUjang, Z-
dc.contributor.authorShreeshivadasan, Chelliapan-
dc.date.accessioned2012-08-07T06:01:16Z-
dc.date.available2012-08-07T06:01:16Z-
dc.date.issued2012-08-
dc.identifier.issn0975-1084 (Online); 0022-4456 (Print)-
dc.identifier.urihttp://hdl.handle.net/123456789/14529-
dc.description573-578en_US
dc.description.abstractThis study presents treatment performance of cafeteria waste and polyhydroxyalkanoate (PHA) production in two stage process through an up-flow anaerobic sludge bed (UASB) and sequencing batch reactor (SBR). COD removal efficiency was found as follows: SBR, 93; and UASB - SBR, 95.4%. In addition, 30% ammoniacal nitrogen (AN) was noted at high aerobic condition and phosphate (PO4) removal efficiency increased at high anoxic conditions. Volatile fatty acid (VFA) intermediates such as acetic acid increased from 505 up to 4315 mg.l-1 in effluent of UASB reactor and successfully consumed in SBR for PHA production. Acetic acid concentration was reduced significantly in SBR from 4315 to 50 mg.l-1. During this period, PHA production was increased to 68% over cell dried weight, confirming effectiveness of sequential UASB-SBR system in producing bioplastic from cafeteria waste.en_US
dc.language.isoen_USen_US
dc.publisherNISCAIR-CSIR, Indiaen_US
dc.rights CC Attribution-Noncommercial-No Derivative Works 2.5 Indiaen_US
dc.sourceJSIR Vol.71(08) [August 2012]en_US
dc.subjectCafeteria wasteen_US
dc.subjectPolyhydroxyalkonate (PHA)en_US
dc.subjectSequencing batch reactoren_US
dc.subjectUp-flow anaerobic sludge beden_US
dc.titleRaw material resource for biodegradable plastic production from cafeteria wastesen_US
dc.typeArticleen_US
Appears in Collections:JSIR Vol.71(08) [August 2012]

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