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A new method of two-phase anaerobic digestion for fruit and vegetable waste treatment
•A novel method of two-phase anaerobic digestion is proposed.•Acid reactor was operated at pH 4.0 with lactate as dominant product.•Effluent from acid reactor was efficiently degraded in UASB.•Lactobacillus was the predominant microorganism in the acid reactor.•Hydrogenotrophic methanogens enriched...
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Published in: | Bioresource technology 2016-07, Vol.211, p.16-23 |
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creator | Wu, Yuanyuan Wang, Cuiping Liu, Xiaoji Ma, Hailing Wu, Jing Zuo, Jiane Wang, Kaijun |
description | •A novel method of two-phase anaerobic digestion is proposed.•Acid reactor was operated at pH 4.0 with lactate as dominant product.•Effluent from acid reactor was efficiently degraded in UASB.•Lactobacillus was the predominant microorganism in the acid reactor.•Hydrogenotrophic methanogens enriched in methane reactor after acclimation.
A novel method of two-phase anaerobic digestion where the acid reactor is operated at low pH 4.0 was proposed and investigated. A completely stirred tank acid reactor and an up-flow anaerobic sludge bed methane reactor were operated to examine the possibility of efficient degradation of lactate and to identify their optimal operating conditions. Lactate with an average concentration of 14.8g/L was the dominant fermentative product and Lactobacillus was the predominant microorganism in the acid reactor. The effluent from the acid reactor was efficiently degraded in the methane reactor and the average methane yield was 261.4ml/gCOD removed. Organisms of Methanosaeta were the predominant methanogen in granular sludge of methane reactor, however, after acclimation hydrogenotrophic methanogens enriched, which benefited for the conversion of lactate to acetate. The two-phase AD system exhibited a low hydraulic retention time of 3.56days and high methane yield of 348.5ml/g VS removed. |
doi_str_mv | 10.1016/j.biortech.2016.03.050 |
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A novel method of two-phase anaerobic digestion where the acid reactor is operated at low pH 4.0 was proposed and investigated. A completely stirred tank acid reactor and an up-flow anaerobic sludge bed methane reactor were operated to examine the possibility of efficient degradation of lactate and to identify their optimal operating conditions. Lactate with an average concentration of 14.8g/L was the dominant fermentative product and Lactobacillus was the predominant microorganism in the acid reactor. The effluent from the acid reactor was efficiently degraded in the methane reactor and the average methane yield was 261.4ml/gCOD removed. Organisms of Methanosaeta were the predominant methanogen in granular sludge of methane reactor, however, after acclimation hydrogenotrophic methanogens enriched, which benefited for the conversion of lactate to acetate. The two-phase AD system exhibited a low hydraulic retention time of 3.56days and high methane yield of 348.5ml/g VS removed.</description><identifier>ISSN: 0960-8524</identifier><identifier>EISSN: 1873-2976</identifier><identifier>DOI: 10.1016/j.biortech.2016.03.050</identifier><identifier>PMID: 26995617</identifier><language>eng</language><publisher>England: Elsevier Ltd</publisher><subject>Anaerobiosis ; Biodegradation, Environmental ; Bioreactors ; Fermentation ; Food ; Fruit ; Fruit and vegetable waste ; Hydrogen-Ion Concentration ; Lactate ; Lactobacillus ; Low pH acidification ; Methane - metabolism ; Methanosaeta ; Sewage ; Two-phase anaerobic digestion ; Upflow anaerobic sludge bed reactor ; Vegetables ; Waste Management - methods</subject><ispartof>Bioresource technology, 2016-07, Vol.211, p.16-23</ispartof><rights>2016 Elsevier Ltd</rights><rights>Copyright © 2016 Elsevier Ltd. All rights reserved.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c467t-e9efe801841c10f25d9efaf6d4b30fb1dc940d9c257a78248bb0d323269d711a3</citedby><cites>FETCH-LOGICAL-c467t-e9efe801841c10f25d9efaf6d4b30fb1dc940d9c257a78248bb0d323269d711a3</cites><orcidid>0000-0001-9779-297X</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27924,27925</link.rule.ids><backlink>$$Uhttps://www.ncbi.nlm.nih.gov/pubmed/26995617$$D View this record in MEDLINE/PubMed$$Hfree_for_read</backlink></links><search><creatorcontrib>Wu, Yuanyuan</creatorcontrib><creatorcontrib>Wang, Cuiping</creatorcontrib><creatorcontrib>Liu, Xiaoji</creatorcontrib><creatorcontrib>Ma, Hailing</creatorcontrib><creatorcontrib>Wu, Jing</creatorcontrib><creatorcontrib>Zuo, Jiane</creatorcontrib><creatorcontrib>Wang, Kaijun</creatorcontrib><title>A new method of two-phase anaerobic digestion for fruit and vegetable waste treatment</title><title>Bioresource technology</title><addtitle>Bioresour Technol</addtitle><description>•A novel method of two-phase anaerobic digestion is proposed.•Acid reactor was operated at pH 4.0 with lactate as dominant product.•Effluent from acid reactor was efficiently degraded in UASB.•Lactobacillus was the predominant microorganism in the acid reactor.•Hydrogenotrophic methanogens enriched in methane reactor after acclimation.
A novel method of two-phase anaerobic digestion where the acid reactor is operated at low pH 4.0 was proposed and investigated. A completely stirred tank acid reactor and an up-flow anaerobic sludge bed methane reactor were operated to examine the possibility of efficient degradation of lactate and to identify their optimal operating conditions. Lactate with an average concentration of 14.8g/L was the dominant fermentative product and Lactobacillus was the predominant microorganism in the acid reactor. The effluent from the acid reactor was efficiently degraded in the methane reactor and the average methane yield was 261.4ml/gCOD removed. Organisms of Methanosaeta were the predominant methanogen in granular sludge of methane reactor, however, after acclimation hydrogenotrophic methanogens enriched, which benefited for the conversion of lactate to acetate. The two-phase AD system exhibited a low hydraulic retention time of 3.56days and high methane yield of 348.5ml/g VS removed.</description><subject>Anaerobiosis</subject><subject>Biodegradation, Environmental</subject><subject>Bioreactors</subject><subject>Fermentation</subject><subject>Food</subject><subject>Fruit</subject><subject>Fruit and vegetable waste</subject><subject>Hydrogen-Ion Concentration</subject><subject>Lactate</subject><subject>Lactobacillus</subject><subject>Low pH acidification</subject><subject>Methane - metabolism</subject><subject>Methanosaeta</subject><subject>Sewage</subject><subject>Two-phase anaerobic digestion</subject><subject>Upflow anaerobic sludge bed reactor</subject><subject>Vegetables</subject><subject>Waste Management - methods</subject><issn>0960-8524</issn><issn>1873-2976</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2016</creationdate><recordtype>article</recordtype><recordid>eNqNkE1P3DAQQK2qVVlo_wLykUvC2E7i-FaESouE1Es5W449Zr3axFvby6r_Hq8WuLan0cy8-dAj5JJBy4AN15t2CjEVtOuW17wF0UIPH8iKjVI0XMnhI1mBGqAZe96dkfOcNwAgmOSfyRkflOoHJlfk8YYueKAzlnV0NHpaDrHZrU1GahaDKU7BUheeMJcQF-pjoj7tQ6ldR5_xCYuZtkgPJhekJaEpMy7lC_nkzTbj19d4QR7vvv--_dk8_Ppxf3vz0NhukKVBhR5HYGPHLAPPe1cLxg-umwT4iTmrOnDK8l4aOfJunCZwgov6vpOMGXFBrk57dyn-2dcf9Ryyxe3WLBj3WTOpqgMGnP0HWkUxIUBVdDihNsWcE3q9S2E26a9moI_29Ua_2ddH-xqErvbr4OXrjf00o3sfe9NdgW8nAKuU54BJZxtwsehCQlu0i-FfN14AzteZXQ</recordid><startdate>201607</startdate><enddate>201607</enddate><creator>Wu, Yuanyuan</creator><creator>Wang, Cuiping</creator><creator>Liu, Xiaoji</creator><creator>Ma, Hailing</creator><creator>Wu, Jing</creator><creator>Zuo, Jiane</creator><creator>Wang, Kaijun</creator><general>Elsevier Ltd</general><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>7X8</scope><scope>7QO</scope><scope>7ST</scope><scope>8FD</scope><scope>C1K</scope><scope>FR3</scope><scope>P64</scope><scope>SOI</scope><orcidid>https://orcid.org/0000-0001-9779-297X</orcidid></search><sort><creationdate>201607</creationdate><title>A new method of two-phase anaerobic digestion for fruit and vegetable waste treatment</title><author>Wu, Yuanyuan ; Wang, Cuiping ; Liu, Xiaoji ; Ma, Hailing ; Wu, Jing ; Zuo, Jiane ; Wang, Kaijun</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c467t-e9efe801841c10f25d9efaf6d4b30fb1dc940d9c257a78248bb0d323269d711a3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2016</creationdate><topic>Anaerobiosis</topic><topic>Biodegradation, Environmental</topic><topic>Bioreactors</topic><topic>Fermentation</topic><topic>Food</topic><topic>Fruit</topic><topic>Fruit and vegetable waste</topic><topic>Hydrogen-Ion Concentration</topic><topic>Lactate</topic><topic>Lactobacillus</topic><topic>Low pH acidification</topic><topic>Methane - metabolism</topic><topic>Methanosaeta</topic><topic>Sewage</topic><topic>Two-phase anaerobic digestion</topic><topic>Upflow anaerobic sludge bed reactor</topic><topic>Vegetables</topic><topic>Waste Management - methods</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Wu, Yuanyuan</creatorcontrib><creatorcontrib>Wang, Cuiping</creatorcontrib><creatorcontrib>Liu, Xiaoji</creatorcontrib><creatorcontrib>Ma, Hailing</creatorcontrib><creatorcontrib>Wu, Jing</creatorcontrib><creatorcontrib>Zuo, Jiane</creatorcontrib><creatorcontrib>Wang, Kaijun</creatorcontrib><collection>Medline</collection><collection>MEDLINE</collection><collection>MEDLINE (Ovid)</collection><collection>MEDLINE</collection><collection>MEDLINE</collection><collection>PubMed</collection><collection>CrossRef</collection><collection>MEDLINE - Academic</collection><collection>Biotechnology Research Abstracts</collection><collection>Environment 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><collection>Environment Abstracts</collection><jtitle>Bioresource technology</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Wu, Yuanyuan</au><au>Wang, Cuiping</au><au>Liu, Xiaoji</au><au>Ma, Hailing</au><au>Wu, Jing</au><au>Zuo, Jiane</au><au>Wang, Kaijun</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>A new method of two-phase anaerobic digestion for fruit and vegetable waste treatment</atitle><jtitle>Bioresource technology</jtitle><addtitle>Bioresour Technol</addtitle><date>2016-07</date><risdate>2016</risdate><volume>211</volume><spage>16</spage><epage>23</epage><pages>16-23</pages><issn>0960-8524</issn><eissn>1873-2976</eissn><abstract>•A novel method of two-phase anaerobic digestion is proposed.•Acid reactor was operated at pH 4.0 with lactate as dominant product.•Effluent from acid reactor was efficiently degraded in UASB.•Lactobacillus was the predominant microorganism in the acid reactor.•Hydrogenotrophic methanogens enriched in methane reactor after acclimation.
A novel method of two-phase anaerobic digestion where the acid reactor is operated at low pH 4.0 was proposed and investigated. A completely stirred tank acid reactor and an up-flow anaerobic sludge bed methane reactor were operated to examine the possibility of efficient degradation of lactate and to identify their optimal operating conditions. Lactate with an average concentration of 14.8g/L was the dominant fermentative product and Lactobacillus was the predominant microorganism in the acid reactor. The effluent from the acid reactor was efficiently degraded in the methane reactor and the average methane yield was 261.4ml/gCOD removed. Organisms of Methanosaeta were the predominant methanogen in granular sludge of methane reactor, however, after acclimation hydrogenotrophic methanogens enriched, which benefited for the conversion of lactate to acetate. The two-phase AD system exhibited a low hydraulic retention time of 3.56days and high methane yield of 348.5ml/g VS removed.</abstract><cop>England</cop><pub>Elsevier Ltd</pub><pmid>26995617</pmid><doi>10.1016/j.biortech.2016.03.050</doi><tpages>8</tpages><orcidid>https://orcid.org/0000-0001-9779-297X</orcidid></addata></record> |
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subjects | Anaerobiosis Biodegradation, Environmental Bioreactors Fermentation Food Fruit Fruit and vegetable waste Hydrogen-Ion Concentration Lactate Lactobacillus Low pH acidification Methane - metabolism Methanosaeta Sewage Two-phase anaerobic digestion Upflow anaerobic sludge bed reactor Vegetables Waste Management - methods |
title | A new method of two-phase anaerobic digestion for fruit and vegetable waste treatment |
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