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Kinetic evaluation and performance of a mesophilic anaerobic contact reactor treating medium-strength food-processing wastewater
High rate mesophilic anaerobic contact reactors (MACR) represent a proven sustainable technology for a wide range of different industrial effluents. These reactors demonstrate quite similar features to their aerobic counterparts, activated sludge systems. A lab-scale high rate mesophilic anaerobic c...
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| Published in: | Bioresource technology 2010-06, Vol.101 (11), p.3970-3977 |
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| container_title | Bioresource technology |
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| creator | Şentürk, E. İnce, M. Onkal Engin, G. |
| description | High rate mesophilic anaerobic contact reactors (MACR) represent a proven sustainable technology for a wide range of different industrial effluents. These reactors demonstrate quite similar features to their aerobic counterparts, activated sludge systems. A lab-scale high rate mesophilic anaerobic contact reactor was operated with wastewater originated from a potato-processing plant, at six different loading rates of 1.1–5
g COD/L per day. The operational performance of MACR was monitored from start-up by assessing COD removal efficiency, total volatile fatty acid production and biogas composition. Furthermore, various kinetic models have been successfully applied to the experimental data to determine substrate balance, maximum utilization rate and volumetric methane production. The COD removal efficiencies were found to be 78–92% and the methane percentage of the biogas produced was 80–89%. Additionally, the methane yield coefficient was found to be 0.394 L CH
4/gTCOD
rem. |
| doi_str_mv | 10.1016/j.biortech.2010.01.034 |
| format | article |
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g COD/L per day. The operational performance of MACR was monitored from start-up by assessing COD removal efficiency, total volatile fatty acid production and biogas composition. Furthermore, various kinetic models have been successfully applied to the experimental data to determine substrate balance, maximum utilization rate and volumetric methane production. The COD removal efficiencies were found to be 78–92% and the methane percentage of the biogas produced was 80–89%. Additionally, the methane yield coefficient was found to be 0.394 L CH
4/gTCOD
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g COD/L per day. The operational performance of MACR was monitored from start-up by assessing COD removal efficiency, total volatile fatty acid production and biogas composition. Furthermore, various kinetic models have been successfully applied to the experimental data to determine substrate balance, maximum utilization rate and volumetric methane production. The COD removal efficiencies were found to be 78–92% and the methane percentage of the biogas produced was 80–89%. Additionally, the methane yield coefficient was found to be 0.394 L CH
4/gTCOD
rem.</description><subject>Anaerobic contact reactor</subject><subject>anaerobic digestion</subject><subject>Anaerobiosis</subject><subject>Applied sciences</subject><subject>biodegradation</subject><subject>Biofuels</subject><subject>Biological and medical sciences</subject><subject>Bioreactors</subject><subject>Biotechnology</subject><subject>chemical oxygen demand</subject><subject>Contact</subject><subject>Crack opening displacement</subject><subject>Effluents</subject><subject>Exact sciences and technology</subject><subject>Fatty acids</subject><subject>Fatty Acids, Volatile - biosynthesis</subject><subject>Food industries</subject><subject>Food Industry</subject><subject>food processing wastes</subject><subject>Fundamental and applied biological sciences. Psychology</subject><subject>Grau second-order multi-component substrate removal model</subject><subject>industrial effluents</subject><subject>Industrial Waste</subject><subject>Kinetic evaluation</subject><subject>Kinetics</subject><subject>Mesophilic</subject><subject>mesophilic anaerobic contact reactors</subject><subject>Methane</subject><subject>methane production</subject><subject>Methods. Procedures. Technologies</subject><subject>Michaelis-Menten model</subject><subject>Organic loading rate</subject><subject>Pollution</subject><subject>Reaction kinetics</subject><subject>Reactors</subject><subject>Solanum tuberosum</subject><subject>Stover-Kincannon model</subject><subject>substrate balance model</subject><subject>Various methods and equipments</subject><subject>Volatile fatty acids</subject><subject>Waste water</subject><subject>wastewater treatment</subject><subject>Wastewaters</subject><subject>Water Pollutants - metabolism</subject><subject>Water treatment and pollution</subject><issn>0960-8524</issn><issn>1873-2976</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2010</creationdate><recordtype>article</recordtype><recordid>eNqFkUtv1DAQgC0EokvhL5RcEKcstvNybqCqPEQlDtCzNbHHu14l8WI7rbjx05lot3DkYo_G34xH3zB2JfhWcNG-O2wHH2JGs99KTkkutryqn7CNUF1Vyr5rn7IN71teqkbWF-xFSgfOeSU6-ZxdUEmlGq427PdXP2P2psB7GBfIPswFzLY4YnQhTjAbLIIroJgwhePej4TCDBjDQJEJcwaTi4h0hlhkCrKfd0Rbv0xlosS8y_vChWDLYwwGU1rfHyBlfICM8SV75mBM-Op8X7K7jzc_rj-Xt98-fbn-cFuauqly6ZxsJFjRW2ENr2tl1dC3yPkgnAXnGuF61UJjBlsPTvU0EEqsBMjBNU7x6pK9PfWlKX4umLKefDI4jjBjWJLu6rqVbd83RLYn0sSQUkSnj9FPEH9pwfUqXx_0o3y9ytdcaJJPhVfnL5aBBPwte7RNwJszAMnA6CLp9ekfJ1u-bo641yfOQdCwi8TcfV-7cKF413drp_cnAknZvceok_FIy7I-osnaBv-_af8Asoaz_w</recordid><startdate>20100601</startdate><enddate>20100601</enddate><creator>Şentürk, E.</creator><creator>İnce, M.</creator><creator>Onkal Engin, G.</creator><general>Elsevier Ltd</general><general>[New York, NY]: Elsevier Ltd</general><general>Elsevier</general><scope>FBQ</scope><scope>IQODW</scope><scope>CGR</scope><scope>CUY</scope><scope>CVF</scope><scope>ECM</scope><scope>EIF</scope><scope>NPM</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7SU</scope><scope>7TB</scope><scope>8FD</scope><scope>C1K</scope><scope>FR3</scope><scope>KR7</scope></search><sort><creationdate>20100601</creationdate><title>Kinetic evaluation and performance of a mesophilic anaerobic contact reactor treating medium-strength food-processing wastewater</title><author>Şentürk, E. ; İnce, M. ; Onkal Engin, G.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c453t-ff252ad19d1dc0448d8b96e00b1fdaff51f986a5cbd4bf89eace2e31a2bf5f803</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2010</creationdate><topic>Anaerobic contact reactor</topic><topic>anaerobic digestion</topic><topic>Anaerobiosis</topic><topic>Applied sciences</topic><topic>biodegradation</topic><topic>Biofuels</topic><topic>Biological and medical sciences</topic><topic>Bioreactors</topic><topic>Biotechnology</topic><topic>chemical oxygen demand</topic><topic>Contact</topic><topic>Crack opening displacement</topic><topic>Effluents</topic><topic>Exact sciences and technology</topic><topic>Fatty acids</topic><topic>Fatty Acids, Volatile - biosynthesis</topic><topic>Food industries</topic><topic>Food Industry</topic><topic>food processing wastes</topic><topic>Fundamental and applied biological sciences. Psychology</topic><topic>Grau second-order multi-component substrate removal model</topic><topic>industrial effluents</topic><topic>Industrial Waste</topic><topic>Kinetic evaluation</topic><topic>Kinetics</topic><topic>Mesophilic</topic><topic>mesophilic anaerobic contact reactors</topic><topic>Methane</topic><topic>methane production</topic><topic>Methods. Procedures. Technologies</topic><topic>Michaelis-Menten model</topic><topic>Organic loading rate</topic><topic>Pollution</topic><topic>Reaction kinetics</topic><topic>Reactors</topic><topic>Solanum tuberosum</topic><topic>Stover-Kincannon model</topic><topic>substrate balance model</topic><topic>Various methods and equipments</topic><topic>Volatile fatty acids</topic><topic>Waste water</topic><topic>wastewater treatment</topic><topic>Wastewaters</topic><topic>Water Pollutants - metabolism</topic><topic>Water treatment and pollution</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Şentürk, E.</creatorcontrib><creatorcontrib>İnce, M.</creatorcontrib><creatorcontrib>Onkal Engin, G.</creatorcontrib><collection>AGRIS</collection><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>Environmental Engineering Abstracts</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Engineering Research Database</collection><collection>Civil Engineering Abstracts</collection><jtitle>Bioresource technology</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Şentürk, E.</au><au>İnce, M.</au><au>Onkal Engin, G.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Kinetic evaluation and performance of a mesophilic anaerobic contact reactor treating medium-strength food-processing wastewater</atitle><jtitle>Bioresource technology</jtitle><addtitle>Bioresour Technol</addtitle><date>2010-06-01</date><risdate>2010</risdate><volume>101</volume><issue>11</issue><spage>3970</spage><epage>3977</epage><pages>3970-3977</pages><issn>0960-8524</issn><eissn>1873-2976</eissn><notes>http://dx.doi.org/10.1016/j.biortech.2010.01.034</notes><notes>ObjectType-Article-1</notes><notes>SourceType-Scholarly Journals-1</notes><notes>ObjectType-Feature-2</notes><notes>content type line 23</notes><abstract>High rate mesophilic anaerobic contact reactors (MACR) represent a proven sustainable technology for a wide range of different industrial effluents. These reactors demonstrate quite similar features to their aerobic counterparts, activated sludge systems. A lab-scale high rate mesophilic anaerobic contact reactor was operated with wastewater originated from a potato-processing plant, at six different loading rates of 1.1–5
g COD/L per day. The operational performance of MACR was monitored from start-up by assessing COD removal efficiency, total volatile fatty acid production and biogas composition. Furthermore, various kinetic models have been successfully applied to the experimental data to determine substrate balance, maximum utilization rate and volumetric methane production. The COD removal efficiencies were found to be 78–92% and the methane percentage of the biogas produced was 80–89%. Additionally, the methane yield coefficient was found to be 0.394 L CH
4/gTCOD
rem.</abstract><cop>Kidlington</cop><pub>Elsevier Ltd</pub><pmid>20138508</pmid><doi>10.1016/j.biortech.2010.01.034</doi><tpages>8</tpages></addata></record> |
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| subjects | Anaerobic contact reactor anaerobic digestion Anaerobiosis Applied sciences biodegradation Biofuels Biological and medical sciences Bioreactors Biotechnology chemical oxygen demand Contact Crack opening displacement Effluents Exact sciences and technology Fatty acids Fatty Acids, Volatile - biosynthesis Food industries Food Industry food processing wastes Fundamental and applied biological sciences. Psychology Grau second-order multi-component substrate removal model industrial effluents Industrial Waste Kinetic evaluation Kinetics Mesophilic mesophilic anaerobic contact reactors Methane methane production Methods. Procedures. Technologies Michaelis-Menten model Organic loading rate Pollution Reaction kinetics Reactors Solanum tuberosum Stover-Kincannon model substrate balance model Various methods and equipments Volatile fatty acids Waste water wastewater treatment Wastewaters Water Pollutants - metabolism Water treatment and pollution |
| title | Kinetic evaluation and performance of a mesophilic anaerobic contact reactor treating medium-strength food-processing wastewater |
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