Performance of pulsed plate bioreactor for biodegradation of phenol
Biodegradation of phenol was carried out using Nocardia hydrocarbonoxydans immobilised on glass beads, in a pulsed plate bioreactor. The effect of operating parameters like frequency of pulsation and amplitude of pulsation on the performance of pulsed plate bioreactor for biodegradation of phenol in...
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Veröffentlicht in: | Journal of hazardous materials 2007-02, Vol.140 (1), p.346-352 |
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creator | Shetty, K. Vidya Kalifathulla, I. Srinikethan, G. |
description | Biodegradation of phenol was carried out using
Nocardia hydrocarbonoxydans immobilised on glass beads, in a pulsed plate bioreactor. The effect of operating parameters like frequency of pulsation and amplitude of pulsation on the performance of pulsed plate bioreactor for biodegradation of phenol in a synthetic wastewater containing 500
ppm phenol was studied. Axial concentration profile measurements revealed that the pulsed plate bioreactor shows continuous stirred tank behaviour. As the amplitude was increased, percentage degradation increased, reaching 100% at amplitude of 4.7
cm and higher. Introduction of pulsation is found to increase the percentage degradation. Percentage degradation has increased with increase in frequency and 100% degradation was achieved at 0.5
s
−1 and above. Biofilms developed in a non-pulsed bioreactor were thicker than those in the pulsed plate bioreactor. But biofilm thickness remained almost constant with increasing frequency. Biofilm density was found to be influenced by pulsation. The time required to reach steady state was more for pulsed reactor than the non-pulsed reactor and this start-up time had increased with increase in frequency of pulsation. The performance studies reveal that the pulsed plate bioreactor with immobilized cells has the potential to be an efficient bioreactor for wastewater treatment. |
doi_str_mv | 10.1016/j.jhazmat.2006.09.058 |
format | Article |
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Nocardia hydrocarbonoxydans immobilised on glass beads, in a pulsed plate bioreactor. The effect of operating parameters like frequency of pulsation and amplitude of pulsation on the performance of pulsed plate bioreactor for biodegradation of phenol in a synthetic wastewater containing 500
ppm phenol was studied. Axial concentration profile measurements revealed that the pulsed plate bioreactor shows continuous stirred tank behaviour. As the amplitude was increased, percentage degradation increased, reaching 100% at amplitude of 4.7
cm and higher. Introduction of pulsation is found to increase the percentage degradation. Percentage degradation has increased with increase in frequency and 100% degradation was achieved at 0.5
s
−1 and above. Biofilms developed in a non-pulsed bioreactor were thicker than those in the pulsed plate bioreactor. But biofilm thickness remained almost constant with increasing frequency. Biofilm density was found to be influenced by pulsation. The time required to reach steady state was more for pulsed reactor than the non-pulsed reactor and this start-up time had increased with increase in frequency of pulsation. The performance studies reveal that the pulsed plate bioreactor with immobilized cells has the potential to be an efficient bioreactor for wastewater treatment.</description><identifier>ISSN: 0304-3894</identifier><identifier>EISSN: 1873-3336</identifier><identifier>DOI: 10.1016/j.jhazmat.2006.09.058</identifier><identifier>PMID: 17092642</identifier><identifier>CODEN: JHMAD9</identifier><language>eng</language><publisher>Amsterdam: Elsevier B.V</publisher><subject>Amplitude ; Applied sciences ; Biodegradation ; Biodegradation, Environmental ; Biofilm ; Biofilms ; Biological and medical sciences ; Bioreactors - standards ; Biotechnology ; Chemical engineering ; Exact sciences and technology ; Frequency ; Fundamental and applied biological sciences. Psychology ; General purification processes ; Immobilised cells ; Methods. Procedures. Technologies ; Mixing ; Nocardia ; Others ; Phenol - metabolism ; Pollution ; Pulsed plate bioreactor ; Reactors ; Various methods and equipments ; Waste Disposal, Fluid ; Wastewaters ; Water Pollutants - metabolism ; Water treatment and pollution</subject><ispartof>Journal of hazardous materials, 2007-02, Vol.140 (1), p.346-352</ispartof><rights>2006 Elsevier B.V.</rights><rights>2007 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c492t-ce0a0108b87094c527fcb450b95502b4e0ca2f1ae0c44d0f4d770c0aa697fd593</citedby><cites>FETCH-LOGICAL-c492t-ce0a0108b87094c527fcb450b95502b4e0ca2f1ae0c44d0f4d770c0aa697fd593</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.jhazmat.2006.09.058$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>315,781,785,3551,27928,27929,45999</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=18492309$$DView record in Pascal Francis$$Hfree_for_read</backlink><backlink>$$Uhttps://www.ncbi.nlm.nih.gov/pubmed/17092642$$D View this record in MEDLINE/PubMed$$Hfree_for_read</backlink></links><search><creatorcontrib>Shetty, K. Vidya</creatorcontrib><creatorcontrib>Kalifathulla, I.</creatorcontrib><creatorcontrib>Srinikethan, G.</creatorcontrib><title>Performance of pulsed plate bioreactor for biodegradation of phenol</title><title>Journal of hazardous materials</title><addtitle>J Hazard Mater</addtitle><description>Biodegradation of phenol was carried out using
Nocardia hydrocarbonoxydans immobilised on glass beads, in a pulsed plate bioreactor. The effect of operating parameters like frequency of pulsation and amplitude of pulsation on the performance of pulsed plate bioreactor for biodegradation of phenol in a synthetic wastewater containing 500
ppm phenol was studied. Axial concentration profile measurements revealed that the pulsed plate bioreactor shows continuous stirred tank behaviour. As the amplitude was increased, percentage degradation increased, reaching 100% at amplitude of 4.7
cm and higher. Introduction of pulsation is found to increase the percentage degradation. Percentage degradation has increased with increase in frequency and 100% degradation was achieved at 0.5
s
−1 and above. Biofilms developed in a non-pulsed bioreactor were thicker than those in the pulsed plate bioreactor. But biofilm thickness remained almost constant with increasing frequency. Biofilm density was found to be influenced by pulsation. The time required to reach steady state was more for pulsed reactor than the non-pulsed reactor and this start-up time had increased with increase in frequency of pulsation. The performance studies reveal that the pulsed plate bioreactor with immobilized cells has the potential to be an efficient bioreactor for wastewater treatment.</description><subject>Amplitude</subject><subject>Applied sciences</subject><subject>Biodegradation</subject><subject>Biodegradation, Environmental</subject><subject>Biofilm</subject><subject>Biofilms</subject><subject>Biological and medical sciences</subject><subject>Bioreactors - standards</subject><subject>Biotechnology</subject><subject>Chemical engineering</subject><subject>Exact sciences and technology</subject><subject>Frequency</subject><subject>Fundamental and applied biological sciences. Psychology</subject><subject>General purification processes</subject><subject>Immobilised cells</subject><subject>Methods. Procedures. Technologies</subject><subject>Mixing</subject><subject>Nocardia</subject><subject>Others</subject><subject>Phenol - metabolism</subject><subject>Pollution</subject><subject>Pulsed plate bioreactor</subject><subject>Reactors</subject><subject>Various methods and equipments</subject><subject>Waste Disposal, Fluid</subject><subject>Wastewaters</subject><subject>Water Pollutants - metabolism</subject><subject>Water treatment and pollution</subject><issn>0304-3894</issn><issn>1873-3336</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2007</creationdate><recordtype>article</recordtype><sourceid>EIF</sourceid><recordid>eNqNkcFq3DAQhkVpSTZpHqHFl-ZmZ2RLtnUqZWmSQqA5pGcxlkaNFnu1lbyB5umrzRpybE6D4Ps1M98w9olDxYG3V5tq84jPE85VDdBWoCqQ_Tu24n3XlE3TtO_ZChoQZdMrccrOUtoAAO-kOGGnvANVt6JesfU9RRfihFtDRXDFbj8mssVuxJmKwYdIaOYQi8wcnpZ-R7Q4-7B9oR9pG8aP7IPDHLtY6jn7df39YX1b3v28-bH-dlcaoeq5NAQIHPqhz92FkXXnzCAkDEpKqAdBYLB2HHMVwoITtuvAAGKrOmelas7Z5fHfXQx_9pRmPflkaBxxS2GfNFdtX3PevwXsBJcyg_IImhhSiuT0LvoJ41_NQR80641eNOuDZg1KZ80593lpsB8msq-pxWsGviwAJoOji9mvT69cn400cFjp65Gj7O3JU9TJeMq3sD6SmbUN_j-j_AO4eJ3I</recordid><startdate>20070209</startdate><enddate>20070209</enddate><creator>Shetty, K. 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Vidya ; Kalifathulla, I. ; Srinikethan, G.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c492t-ce0a0108b87094c527fcb450b95502b4e0ca2f1ae0c44d0f4d770c0aa697fd593</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2007</creationdate><topic>Amplitude</topic><topic>Applied sciences</topic><topic>Biodegradation</topic><topic>Biodegradation, Environmental</topic><topic>Biofilm</topic><topic>Biofilms</topic><topic>Biological and medical sciences</topic><topic>Bioreactors - standards</topic><topic>Biotechnology</topic><topic>Chemical engineering</topic><topic>Exact sciences and technology</topic><topic>Frequency</topic><topic>Fundamental and applied biological sciences. Psychology</topic><topic>General purification processes</topic><topic>Immobilised cells</topic><topic>Methods. Procedures. Technologies</topic><topic>Mixing</topic><topic>Nocardia</topic><topic>Others</topic><topic>Phenol - metabolism</topic><topic>Pollution</topic><topic>Pulsed plate bioreactor</topic><topic>Reactors</topic><topic>Various methods and equipments</topic><topic>Waste Disposal, Fluid</topic><topic>Wastewaters</topic><topic>Water Pollutants - metabolism</topic><topic>Water treatment and pollution</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Shetty, K. Vidya</creatorcontrib><creatorcontrib>Kalifathulla, I.</creatorcontrib><creatorcontrib>Srinikethan, G.</creatorcontrib><collection>Pascal-Francis</collection><collection>Medline</collection><collection>MEDLINE</collection><collection>MEDLINE (Ovid)</collection><collection>MEDLINE</collection><collection>MEDLINE</collection><collection>PubMed</collection><collection>CrossRef</collection><collection>Bacteriology Abstracts (Microbiology B)</collection><collection>Biotechnology Research Abstracts</collection><collection>Industrial and Applied Microbiology Abstracts (Microbiology A)</collection><collection>Pollution Abstracts</collection><collection>Toxicology Abstracts</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Engineering Research Database</collection><collection>Biotechnology and BioEngineering Abstracts</collection><jtitle>Journal of hazardous materials</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Shetty, K. Vidya</au><au>Kalifathulla, I.</au><au>Srinikethan, G.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Performance of pulsed plate bioreactor for biodegradation of phenol</atitle><jtitle>Journal of hazardous materials</jtitle><addtitle>J Hazard Mater</addtitle><date>2007-02-09</date><risdate>2007</risdate><volume>140</volume><issue>1</issue><spage>346</spage><epage>352</epage><pages>346-352</pages><issn>0304-3894</issn><eissn>1873-3336</eissn><coden>JHMAD9</coden><abstract>Biodegradation of phenol was carried out using
Nocardia hydrocarbonoxydans immobilised on glass beads, in a pulsed plate bioreactor. The effect of operating parameters like frequency of pulsation and amplitude of pulsation on the performance of pulsed plate bioreactor for biodegradation of phenol in a synthetic wastewater containing 500
ppm phenol was studied. Axial concentration profile measurements revealed that the pulsed plate bioreactor shows continuous stirred tank behaviour. As the amplitude was increased, percentage degradation increased, reaching 100% at amplitude of 4.7
cm and higher. Introduction of pulsation is found to increase the percentage degradation. Percentage degradation has increased with increase in frequency and 100% degradation was achieved at 0.5
s
−1 and above. Biofilms developed in a non-pulsed bioreactor were thicker than those in the pulsed plate bioreactor. But biofilm thickness remained almost constant with increasing frequency. Biofilm density was found to be influenced by pulsation. The time required to reach steady state was more for pulsed reactor than the non-pulsed reactor and this start-up time had increased with increase in frequency of pulsation. The performance studies reveal that the pulsed plate bioreactor with immobilized cells has the potential to be an efficient bioreactor for wastewater treatment.</abstract><cop>Amsterdam</cop><pub>Elsevier B.V</pub><pmid>17092642</pmid><doi>10.1016/j.jhazmat.2006.09.058</doi><tpages>7</tpages></addata></record> |
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subjects | Amplitude Applied sciences Biodegradation Biodegradation, Environmental Biofilm Biofilms Biological and medical sciences Bioreactors - standards Biotechnology Chemical engineering Exact sciences and technology Frequency Fundamental and applied biological sciences. Psychology General purification processes Immobilised cells Methods. Procedures. Technologies Mixing Nocardia Others Phenol - metabolism Pollution Pulsed plate bioreactor Reactors Various methods and equipments Waste Disposal, Fluid Wastewaters Water Pollutants - metabolism Water treatment and pollution |
title | Performance of pulsed plate bioreactor for biodegradation of phenol |
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