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A cascade of a denitrification bioreactor and an aerobic biofilm reactor for heavy oil refinery wastewater treatment
The performance of an efficient denitrification bioreactor-aerobic biofilm reactor cascade for heavy oil refinery wastewater treatment was investigated. Optimum operation parameters for denitrification were found as follows: (1) hydraulic retention time of 8 h; (2) C/NO 3 − -N molar ratio of 3.75 wi...
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Published in: | RSC advances 2019-01, Vol.9 (13), p.7495-754 |
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container_title | RSC advances |
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creator | Dong, Honghong Jiang, Xiaoyan Sun, Shanshan Fang, Li Wang, Wei Cui, Kai Yao, Tiantian Wang, Heming Zhang, Zhiyong Zhang, Ying Zhang, Zhongzhi Fu, Pengcheng |
description | The performance of an efficient denitrification bioreactor-aerobic biofilm reactor cascade for heavy oil refinery wastewater treatment was investigated. Optimum operation parameters for denitrification were found as follows: (1) hydraulic retention time of 8 h; (2) C/NO
3
−
-N molar ratio of 3.75 with acetate as the carbon source; (3) 20% (v/v) carrier filling ratio in the denitrification bioreactor. Under such optimal conditions, a volumetric removal of 0.82 kg N m
−3
d
−1
was obtained. As an alternative low-cost carbon source to acetate, secondary DAF effluent (COD/NO
3
−
-N mass ratio of 5.4) was also detected and a stable activity of denitrification was achieved with adding 25% volume fraction of secondary DAF effluent. Effluent COD of the subsequent aerobic biofilm reactor further decreased satisfying the requirements of the current discharge standards. High-throughput sequencing results exhibited that Rhodocyclaceae and Comamonadaceae were the dominant denitrifiers in the denitrification reactor and
Pseudomonas
was the dominant microbe in the aerobic biofilm reactor.
The performance of an efficient denitrification bioreactor-aerobic biofilm reactor cascade for heavy oil refinery wastewater treatment was investigated. |
doi_str_mv | 10.1039/c8ra10510c |
format | article |
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3
−
-N molar ratio of 3.75 with acetate as the carbon source; (3) 20% (v/v) carrier filling ratio in the denitrification bioreactor. Under such optimal conditions, a volumetric removal of 0.82 kg N m
−3
d
−1
was obtained. As an alternative low-cost carbon source to acetate, secondary DAF effluent (COD/NO
3
−
-N mass ratio of 5.4) was also detected and a stable activity of denitrification was achieved with adding 25% volume fraction of secondary DAF effluent. Effluent COD of the subsequent aerobic biofilm reactor further decreased satisfying the requirements of the current discharge standards. High-throughput sequencing results exhibited that Rhodocyclaceae and Comamonadaceae were the dominant denitrifiers in the denitrification reactor and
Pseudomonas
was the dominant microbe in the aerobic biofilm reactor.
The performance of an efficient denitrification bioreactor-aerobic biofilm reactor cascade for heavy oil refinery wastewater treatment was investigated.</description><identifier>ISSN: 2046-2069</identifier><identifier>EISSN: 2046-2069</identifier><identifier>DOI: 10.1039/c8ra10510c</identifier><identifier>PMID: 35519961</identifier><language>eng</language><publisher>England: Royal Society of Chemistry</publisher><subject>Biofilms ; Bioreactors ; Carbon ; Chemistry ; Denitrification ; Effluents ; Hydraulic retention time ; Optimization ; Petroleum refineries ; Refineries ; Wastewater treatment ; Water treatment</subject><ispartof>RSC advances, 2019-01, Vol.9 (13), p.7495-754</ispartof><rights>This journal is © The Royal Society of Chemistry.</rights><rights>Copyright Royal Society of Chemistry 2019</rights><rights>This journal is © The Royal Society of Chemistry 2019 The Royal Society of Chemistry</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c494t-236b502ef469d2a71e6d0e68d9ddaa98ac2c09c711d1745cbe3a4e78d9c50eb43</citedby><cites>FETCH-LOGICAL-c494t-236b502ef469d2a71e6d0e68d9ddaa98ac2c09c711d1745cbe3a4e78d9c50eb43</cites><orcidid>0000-0002-6937-9149 ; 0000-0002-2451-5354</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://www.ncbi.nlm.nih.gov/pmc/articles/PMC9061216/pdf/$$EPDF$$P50$$Gpubmedcentral$$Hfree_for_read</linktopdf><linktohtml>$$Uhttps://www.ncbi.nlm.nih.gov/pmc/articles/PMC9061216/$$EHTML$$P50$$Gpubmedcentral$$Hfree_for_read</linktohtml><link.rule.ids>230,314,723,776,780,881,27901,27902,53766,53768</link.rule.ids><backlink>$$Uhttps://www.ncbi.nlm.nih.gov/pubmed/35519961$$D View this record in MEDLINE/PubMed$$Hfree_for_read</backlink></links><search><creatorcontrib>Dong, Honghong</creatorcontrib><creatorcontrib>Jiang, Xiaoyan</creatorcontrib><creatorcontrib>Sun, Shanshan</creatorcontrib><creatorcontrib>Fang, Li</creatorcontrib><creatorcontrib>Wang, Wei</creatorcontrib><creatorcontrib>Cui, Kai</creatorcontrib><creatorcontrib>Yao, Tiantian</creatorcontrib><creatorcontrib>Wang, Heming</creatorcontrib><creatorcontrib>Zhang, Zhiyong</creatorcontrib><creatorcontrib>Zhang, Ying</creatorcontrib><creatorcontrib>Zhang, Zhongzhi</creatorcontrib><creatorcontrib>Fu, Pengcheng</creatorcontrib><title>A cascade of a denitrification bioreactor and an aerobic biofilm reactor for heavy oil refinery wastewater treatment</title><title>RSC advances</title><addtitle>RSC Adv</addtitle><description>The performance of an efficient denitrification bioreactor-aerobic biofilm reactor cascade for heavy oil refinery wastewater treatment was investigated. Optimum operation parameters for denitrification were found as follows: (1) hydraulic retention time of 8 h; (2) C/NO
3
−
-N molar ratio of 3.75 with acetate as the carbon source; (3) 20% (v/v) carrier filling ratio in the denitrification bioreactor. Under such optimal conditions, a volumetric removal of 0.82 kg N m
−3
d
−1
was obtained. As an alternative low-cost carbon source to acetate, secondary DAF effluent (COD/NO
3
−
-N mass ratio of 5.4) was also detected and a stable activity of denitrification was achieved with adding 25% volume fraction of secondary DAF effluent. Effluent COD of the subsequent aerobic biofilm reactor further decreased satisfying the requirements of the current discharge standards. High-throughput sequencing results exhibited that Rhodocyclaceae and Comamonadaceae were the dominant denitrifiers in the denitrification reactor and
Pseudomonas
was the dominant microbe in the aerobic biofilm reactor.
The performance of an efficient denitrification bioreactor-aerobic biofilm reactor cascade for heavy oil refinery wastewater treatment was investigated.</description><subject>Biofilms</subject><subject>Bioreactors</subject><subject>Carbon</subject><subject>Chemistry</subject><subject>Denitrification</subject><subject>Effluents</subject><subject>Hydraulic retention time</subject><subject>Optimization</subject><subject>Petroleum refineries</subject><subject>Refineries</subject><subject>Wastewater treatment</subject><subject>Water treatment</subject><issn>2046-2069</issn><issn>2046-2069</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2019</creationdate><recordtype>article</recordtype><recordid>eNpdklFrHCEUhaU0NCHNS99bhL6UwDZeZ3THl8KytGkhEAjts9zRO41hZkzVTdh_X9NNtmmFi-L5OF49MvYGxEcQjTlzXUIQCoR7wY6kaPVCCm1ePlsfspOcb0QdWoHU8IodNkqBMRqOWFlxh9mhJx4HjtzTHEoKQ3BYQpx5H2IidCUmjrOvxZFS7IN7UIYwTvxJHmpdE95teQxj3R3CTGnL7zEXusdCiZeKlonm8podDDhmOnmcj9mPL5-_r78uLi7Pv61XFwvXmrYsZKN7JSQNrTZe4hJIe0G688Z7RNOhk04YtwTwsGyV66nBlpZVd0pQ3zbH7NPO93bTT-RdPTrhaG9TmDBtbcRg_1XmcG1_xjtrhAYJuhp8eDRI8deGcrFTyI7GEWeKm2yl1iA62Xaqou__Q2_iJs31elZCZ5SATopKne4ol2LO9ZH2zYCwD3nadXe1-pPnusLvnre_R5_Sq8DbHZCy26t_P0TzG5QJpv4</recordid><startdate>20190101</startdate><enddate>20190101</enddate><creator>Dong, Honghong</creator><creator>Jiang, Xiaoyan</creator><creator>Sun, Shanshan</creator><creator>Fang, Li</creator><creator>Wang, Wei</creator><creator>Cui, Kai</creator><creator>Yao, Tiantian</creator><creator>Wang, Heming</creator><creator>Zhang, Zhiyong</creator><creator>Zhang, Ying</creator><creator>Zhang, Zhongzhi</creator><creator>Fu, Pengcheng</creator><general>Royal Society of Chemistry</general><general>The Royal Society of Chemistry</general><scope>NPM</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7SR</scope><scope>8BQ</scope><scope>8FD</scope><scope>JG9</scope><scope>7X8</scope><scope>5PM</scope><orcidid>https://orcid.org/0000-0002-6937-9149</orcidid><orcidid>https://orcid.org/0000-0002-2451-5354</orcidid></search><sort><creationdate>20190101</creationdate><title>A cascade of a denitrification bioreactor and an aerobic biofilm reactor for heavy oil refinery wastewater treatment</title><author>Dong, Honghong ; Jiang, Xiaoyan ; Sun, Shanshan ; Fang, Li ; Wang, Wei ; Cui, Kai ; Yao, Tiantian ; Wang, Heming ; Zhang, Zhiyong ; Zhang, Ying ; Zhang, Zhongzhi ; Fu, Pengcheng</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c494t-236b502ef469d2a71e6d0e68d9ddaa98ac2c09c711d1745cbe3a4e78d9c50eb43</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2019</creationdate><topic>Biofilms</topic><topic>Bioreactors</topic><topic>Carbon</topic><topic>Chemistry</topic><topic>Denitrification</topic><topic>Effluents</topic><topic>Hydraulic retention time</topic><topic>Optimization</topic><topic>Petroleum refineries</topic><topic>Refineries</topic><topic>Wastewater treatment</topic><topic>Water treatment</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Dong, Honghong</creatorcontrib><creatorcontrib>Jiang, Xiaoyan</creatorcontrib><creatorcontrib>Sun, Shanshan</creatorcontrib><creatorcontrib>Fang, Li</creatorcontrib><creatorcontrib>Wang, Wei</creatorcontrib><creatorcontrib>Cui, Kai</creatorcontrib><creatorcontrib>Yao, Tiantian</creatorcontrib><creatorcontrib>Wang, Heming</creatorcontrib><creatorcontrib>Zhang, Zhiyong</creatorcontrib><creatorcontrib>Zhang, Ying</creatorcontrib><creatorcontrib>Zhang, Zhongzhi</creatorcontrib><creatorcontrib>Fu, Pengcheng</creatorcontrib><collection>PubMed</collection><collection>CrossRef</collection><collection>Engineered Materials Abstracts</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Materials Research Database</collection><collection>MEDLINE - Academic</collection><collection>PubMed Central (Full Participant titles)</collection><jtitle>RSC advances</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Dong, Honghong</au><au>Jiang, Xiaoyan</au><au>Sun, Shanshan</au><au>Fang, Li</au><au>Wang, Wei</au><au>Cui, Kai</au><au>Yao, Tiantian</au><au>Wang, Heming</au><au>Zhang, Zhiyong</au><au>Zhang, Ying</au><au>Zhang, Zhongzhi</au><au>Fu, Pengcheng</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>A cascade of a denitrification bioreactor and an aerobic biofilm reactor for heavy oil refinery wastewater treatment</atitle><jtitle>RSC advances</jtitle><addtitle>RSC Adv</addtitle><date>2019-01-01</date><risdate>2019</risdate><volume>9</volume><issue>13</issue><spage>7495</spage><epage>754</epage><pages>7495-754</pages><issn>2046-2069</issn><eissn>2046-2069</eissn><abstract>The performance of an efficient denitrification bioreactor-aerobic biofilm reactor cascade for heavy oil refinery wastewater treatment was investigated. Optimum operation parameters for denitrification were found as follows: (1) hydraulic retention time of 8 h; (2) C/NO
3
−
-N molar ratio of 3.75 with acetate as the carbon source; (3) 20% (v/v) carrier filling ratio in the denitrification bioreactor. Under such optimal conditions, a volumetric removal of 0.82 kg N m
−3
d
−1
was obtained. As an alternative low-cost carbon source to acetate, secondary DAF effluent (COD/NO
3
−
-N mass ratio of 5.4) was also detected and a stable activity of denitrification was achieved with adding 25% volume fraction of secondary DAF effluent. Effluent COD of the subsequent aerobic biofilm reactor further decreased satisfying the requirements of the current discharge standards. High-throughput sequencing results exhibited that Rhodocyclaceae and Comamonadaceae were the dominant denitrifiers in the denitrification reactor and
Pseudomonas
was the dominant microbe in the aerobic biofilm reactor.
The performance of an efficient denitrification bioreactor-aerobic biofilm reactor cascade for heavy oil refinery wastewater treatment was investigated.</abstract><cop>England</cop><pub>Royal Society of Chemistry</pub><pmid>35519961</pmid><doi>10.1039/c8ra10510c</doi><tpages>1</tpages><orcidid>https://orcid.org/0000-0002-6937-9149</orcidid><orcidid>https://orcid.org/0000-0002-2451-5354</orcidid><oa>free_for_read</oa></addata></record> |
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language | eng |
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source | Open Access: PubMed Central |
subjects | Biofilms Bioreactors Carbon Chemistry Denitrification Effluents Hydraulic retention time Optimization Petroleum refineries Refineries Wastewater treatment Water treatment |
title | A cascade of a denitrification bioreactor and an aerobic biofilm reactor for heavy oil refinery wastewater treatment |
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