Effect of ammoniacal nitrogen on one-stage and two-stage anaerobic digestion of food waste
•Almost 100% of the biomethane potential of food waste was recovered during AD in a two-stage CSTR.•Recirculation of the liquid fraction of the digestate provided the necessary buffer in the AD reactors.•A higher OLR (0.9gVS/L·d) led to higher accumulation of TAN, which caused more toxicity.•A two-s...
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creator | Ariunbaatar, Javkhlan Scotto Di Perta, Ester Panico, Antonio Frunzo, Luigi Esposito, Giovanni Lens, Piet N.L. Pirozzi, Francesco |
description | •Almost 100% of the biomethane potential of food waste was recovered during AD in a two-stage CSTR.•Recirculation of the liquid fraction of the digestate provided the necessary buffer in the AD reactors.•A higher OLR (0.9gVS/L·d) led to higher accumulation of TAN, which caused more toxicity.•A two-stage reactor is more sensitive to elevated concentrations of ammonia.•The IC50 of TAN for the AD of food waste amounts to 3.8g/L.
This research compares the operation of one-stage and two-stage anaerobic continuously stirred tank reactor (CSTR) systems fed semi-continuously with food waste. The main purpose was to investigate the effects of ammoniacal nitrogen on the anaerobic digestion process. The two-stage system gave more reliable operation compared to one-stage due to: (i) a better pH self-adjusting capacity; (ii) a higher resistance to organic loading shocks; and (iii) a higher conversion rate of organic substrate to biomethane. Also a small amount of biohydrogen was detected from the first stage of the two-stage reactor making this system attractive for biohythane production. As the digestate contains ammoniacal nitrogen, re-circulating it provided the necessary alkalinity in the systems, thus preventing an eventual failure by volatile fatty acids (VFA) accumulation. However, re-circulation also resulted in an ammonium accumulation, yielding a lower biomethane production. Based on the batch experimental results the 50% inhibitory concentration of total ammoniacal nitrogen on the methanogenic activities was calculated as 3.8g/L, corresponding to 146mg/L free ammonia for the inoculum used for this research. The two-stage system was affected by the inhibition more than the one-stage system, as it requires less alkalinity and the physically separated methanogens are more sensitive to inhibitory factors, such as ammonium and propionic acid. |
doi_str_mv | 10.1016/j.wasman.2014.12.001 |
format | Article |
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This research compares the operation of one-stage and two-stage anaerobic continuously stirred tank reactor (CSTR) systems fed semi-continuously with food waste. The main purpose was to investigate the effects of ammoniacal nitrogen on the anaerobic digestion process. The two-stage system gave more reliable operation compared to one-stage due to: (i) a better pH self-adjusting capacity; (ii) a higher resistance to organic loading shocks; and (iii) a higher conversion rate of organic substrate to biomethane. Also a small amount of biohydrogen was detected from the first stage of the two-stage reactor making this system attractive for biohythane production. As the digestate contains ammoniacal nitrogen, re-circulating it provided the necessary alkalinity in the systems, thus preventing an eventual failure by volatile fatty acids (VFA) accumulation. However, re-circulation also resulted in an ammonium accumulation, yielding a lower biomethane production. Based on the batch experimental results the 50% inhibitory concentration of total ammoniacal nitrogen on the methanogenic activities was calculated as 3.8g/L, corresponding to 146mg/L free ammonia for the inoculum used for this research. The two-stage system was affected by the inhibition more than the one-stage system, as it requires less alkalinity and the physically separated methanogens are more sensitive to inhibitory factors, such as ammonium and propionic acid.</description><identifier>ISSN: 0956-053X</identifier><identifier>EISSN: 1879-2456</identifier><identifier>DOI: 10.1016/j.wasman.2014.12.001</identifier><identifier>PMID: 25613216</identifier><language>eng</language><publisher>United States: Elsevier Ltd</publisher><subject>ACID NEUTRALIZING CAPACITY ; Alkalinity ; AMMONIA ; Ammonia - metabolism ; Ammonia inhibition ; ANAEROBIC DIGESTION ; Anaerobiosis ; Biofuels - analysis ; Biogas ; Bioreactors ; Buffer capacity ; CARBOXYLIC ACIDS ; Comparison of one-stage and two-stage ; CONCENTRATION RATIO ; ENERGY CONVERSION ; Failure ; FOOD ; Foods ; Garbage ; INORGANIC, ORGANIC, PHYSICAL AND ANALYTICAL CHEMISTRY ; MANAGEMENT OF RADIOACTIVE WASTES, AND NON-RADIOACTIVE WASTES FROM NUCLEAR FACILITIES ; METHANE ; Methane - analysis ; NITROGEN ; Nitrogen - metabolism ; PH VALUE ; PROPIONIC ACID ; Refuse Disposal - methods ; Solid Waste - analysis ; Total ammoniacal nitrogen ; TOXICITY ; VOLATILITY ; WASTES</subject><ispartof>Waste management (Elmsford), 2015-04, Vol.38, p.388-398</ispartof><rights>2014 Elsevier Ltd</rights><rights>Copyright © 2014 Elsevier Ltd. All rights reserved.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c629t-182551aa32d72a864e05653ecddea036686f4dcf79a93f69ea0f08a59a19dbad3</citedby><cites>FETCH-LOGICAL-c629t-182551aa32d72a864e05653ecddea036686f4dcf79a93f69ea0f08a59a19dbad3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.wasman.2014.12.001$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>230,314,780,784,885,3550,27924,27925,45995</link.rule.ids><backlink>$$Uhttps://www.ncbi.nlm.nih.gov/pubmed/25613216$$D View this record in MEDLINE/PubMed$$Hfree_for_read</backlink><backlink>$$Uhttps://www.osti.gov/biblio/22470229$$D View this record in Osti.gov$$Hfree_for_read</backlink></links><search><creatorcontrib>Ariunbaatar, Javkhlan</creatorcontrib><creatorcontrib>Scotto Di Perta, Ester</creatorcontrib><creatorcontrib>Panico, Antonio</creatorcontrib><creatorcontrib>Frunzo, Luigi</creatorcontrib><creatorcontrib>Esposito, Giovanni</creatorcontrib><creatorcontrib>Lens, Piet N.L.</creatorcontrib><creatorcontrib>Pirozzi, Francesco</creatorcontrib><title>Effect of ammoniacal nitrogen on one-stage and two-stage anaerobic digestion of food waste</title><title>Waste management (Elmsford)</title><addtitle>Waste Manag</addtitle><description>•Almost 100% of the biomethane potential of food waste was recovered during AD in a two-stage CSTR.•Recirculation of the liquid fraction of the digestate provided the necessary buffer in the AD reactors.•A higher OLR (0.9gVS/L·d) led to higher accumulation of TAN, which caused more toxicity.•A two-stage reactor is more sensitive to elevated concentrations of ammonia.•The IC50 of TAN for the AD of food waste amounts to 3.8g/L.
This research compares the operation of one-stage and two-stage anaerobic continuously stirred tank reactor (CSTR) systems fed semi-continuously with food waste. The main purpose was to investigate the effects of ammoniacal nitrogen on the anaerobic digestion process. The two-stage system gave more reliable operation compared to one-stage due to: (i) a better pH self-adjusting capacity; (ii) a higher resistance to organic loading shocks; and (iii) a higher conversion rate of organic substrate to biomethane. Also a small amount of biohydrogen was detected from the first stage of the two-stage reactor making this system attractive for biohythane production. As the digestate contains ammoniacal nitrogen, re-circulating it provided the necessary alkalinity in the systems, thus preventing an eventual failure by volatile fatty acids (VFA) accumulation. However, re-circulation also resulted in an ammonium accumulation, yielding a lower biomethane production. Based on the batch experimental results the 50% inhibitory concentration of total ammoniacal nitrogen on the methanogenic activities was calculated as 3.8g/L, corresponding to 146mg/L free ammonia for the inoculum used for this research. The two-stage system was affected by the inhibition more than the one-stage system, as it requires less alkalinity and the physically separated methanogens are more sensitive to inhibitory factors, such as ammonium and propionic acid.</description><subject>ACID NEUTRALIZING CAPACITY</subject><subject>Alkalinity</subject><subject>AMMONIA</subject><subject>Ammonia - metabolism</subject><subject>Ammonia inhibition</subject><subject>ANAEROBIC DIGESTION</subject><subject>Anaerobiosis</subject><subject>Biofuels - analysis</subject><subject>Biogas</subject><subject>Bioreactors</subject><subject>Buffer capacity</subject><subject>CARBOXYLIC ACIDS</subject><subject>Comparison of one-stage and two-stage</subject><subject>CONCENTRATION RATIO</subject><subject>ENERGY CONVERSION</subject><subject>Failure</subject><subject>FOOD</subject><subject>Foods</subject><subject>Garbage</subject><subject>INORGANIC, ORGANIC, PHYSICAL AND ANALYTICAL CHEMISTRY</subject><subject>MANAGEMENT OF RADIOACTIVE WASTES, AND NON-RADIOACTIVE WASTES FROM NUCLEAR FACILITIES</subject><subject>METHANE</subject><subject>Methane - analysis</subject><subject>NITROGEN</subject><subject>Nitrogen - metabolism</subject><subject>PH VALUE</subject><subject>PROPIONIC ACID</subject><subject>Refuse Disposal - methods</subject><subject>Solid Waste - analysis</subject><subject>Total ammoniacal nitrogen</subject><subject>TOXICITY</subject><subject>VOLATILITY</subject><subject>WASTES</subject><issn>0956-053X</issn><issn>1879-2456</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2015</creationdate><recordtype>article</recordtype><sourceid>EIF</sourceid><recordid>eNqNkV9rFTEQxYMo9lr9BiIBX_qya_5sspsXQUprhYIvLYgvYW4yueZyN6mbvRa_vVm29rEKgSHhNzMn5xDylrOWM64_7Nt7KCOkVjDetVy0jPFnZMOH3jSiU_o52TCjdMOU_HZCXpWyr0A3cPaSnAiluRRcb8j3ixDQzTQHCuOYUwQHB5riPOUdJpqXg02ZYYcUkqfzfX68AU55Gx31cYdljgsbaMjZ06psxtfkRYBDwTcP9ZTcXl7cnF81118_fzn_dN04Lczc8EEoxQGk8L2AQXfIlFYSnfcITGo96NB5F3oDRgZt6mNgAygD3PgteHlK3q9zcxVhi4szuh8up1T_ZYXoeiaEqdTZSt1N-eex6rVjLA4PB0iYj8XyvnLVnU79Byor2fFB_xvVujeqH5SsaLeibsqlTBjs3RRHmH5bzuySqN3bNVG7JGq5sDWw2vbuYcNxO6J_bPobYQU-rgBWj39FnBYLMDn0cVoc8Dk-veEPiyuydQ</recordid><startdate>20150401</startdate><enddate>20150401</enddate><creator>Ariunbaatar, Javkhlan</creator><creator>Scotto Di Perta, Ester</creator><creator>Panico, Antonio</creator><creator>Frunzo, Luigi</creator><creator>Esposito, Giovanni</creator><creator>Lens, Piet N.L.</creator><creator>Pirozzi, Francesco</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>7ST</scope><scope>7TV</scope><scope>C1K</scope><scope>SOI</scope><scope>7QQ</scope><scope>8FD</scope><scope>FR3</scope><scope>JG9</scope><scope>KR7</scope><scope>OTOTI</scope></search><sort><creationdate>20150401</creationdate><title>Effect of ammoniacal nitrogen on one-stage and two-stage anaerobic digestion of food waste</title><author>Ariunbaatar, Javkhlan ; Scotto Di Perta, Ester ; Panico, Antonio ; Frunzo, Luigi ; Esposito, Giovanni ; Lens, Piet N.L. ; Pirozzi, Francesco</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c629t-182551aa32d72a864e05653ecddea036686f4dcf79a93f69ea0f08a59a19dbad3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2015</creationdate><topic>ACID NEUTRALIZING CAPACITY</topic><topic>Alkalinity</topic><topic>AMMONIA</topic><topic>Ammonia - metabolism</topic><topic>Ammonia inhibition</topic><topic>ANAEROBIC DIGESTION</topic><topic>Anaerobiosis</topic><topic>Biofuels - analysis</topic><topic>Biogas</topic><topic>Bioreactors</topic><topic>Buffer capacity</topic><topic>CARBOXYLIC ACIDS</topic><topic>Comparison of one-stage and two-stage</topic><topic>CONCENTRATION RATIO</topic><topic>ENERGY CONVERSION</topic><topic>Failure</topic><topic>FOOD</topic><topic>Foods</topic><topic>Garbage</topic><topic>INORGANIC, ORGANIC, PHYSICAL AND ANALYTICAL CHEMISTRY</topic><topic>MANAGEMENT OF RADIOACTIVE WASTES, AND NON-RADIOACTIVE WASTES FROM NUCLEAR FACILITIES</topic><topic>METHANE</topic><topic>Methane - analysis</topic><topic>NITROGEN</topic><topic>Nitrogen - metabolism</topic><topic>PH VALUE</topic><topic>PROPIONIC ACID</topic><topic>Refuse Disposal - methods</topic><topic>Solid Waste - analysis</topic><topic>Total ammoniacal nitrogen</topic><topic>TOXICITY</topic><topic>VOLATILITY</topic><topic>WASTES</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Ariunbaatar, Javkhlan</creatorcontrib><creatorcontrib>Scotto Di Perta, Ester</creatorcontrib><creatorcontrib>Panico, Antonio</creatorcontrib><creatorcontrib>Frunzo, Luigi</creatorcontrib><creatorcontrib>Esposito, Giovanni</creatorcontrib><creatorcontrib>Lens, Piet N.L.</creatorcontrib><creatorcontrib>Pirozzi, Francesco</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>Environment Abstracts</collection><collection>Pollution Abstracts</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Environment Abstracts</collection><collection>Ceramic Abstracts</collection><collection>Technology Research Database</collection><collection>Engineering Research Database</collection><collection>Materials Research Database</collection><collection>Civil Engineering Abstracts</collection><collection>OSTI.GOV</collection><jtitle>Waste management (Elmsford)</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Ariunbaatar, Javkhlan</au><au>Scotto Di Perta, Ester</au><au>Panico, Antonio</au><au>Frunzo, Luigi</au><au>Esposito, Giovanni</au><au>Lens, Piet N.L.</au><au>Pirozzi, Francesco</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Effect of ammoniacal nitrogen on one-stage and two-stage anaerobic digestion of food waste</atitle><jtitle>Waste management (Elmsford)</jtitle><addtitle>Waste Manag</addtitle><date>2015-04-01</date><risdate>2015</risdate><volume>38</volume><spage>388</spage><epage>398</epage><pages>388-398</pages><issn>0956-053X</issn><eissn>1879-2456</eissn><abstract>•Almost 100% of the biomethane potential of food waste was recovered during AD in a two-stage CSTR.•Recirculation of the liquid fraction of the digestate provided the necessary buffer in the AD reactors.•A higher OLR (0.9gVS/L·d) led to higher accumulation of TAN, which caused more toxicity.•A two-stage reactor is more sensitive to elevated concentrations of ammonia.•The IC50 of TAN for the AD of food waste amounts to 3.8g/L.
This research compares the operation of one-stage and two-stage anaerobic continuously stirred tank reactor (CSTR) systems fed semi-continuously with food waste. The main purpose was to investigate the effects of ammoniacal nitrogen on the anaerobic digestion process. The two-stage system gave more reliable operation compared to one-stage due to: (i) a better pH self-adjusting capacity; (ii) a higher resistance to organic loading shocks; and (iii) a higher conversion rate of organic substrate to biomethane. Also a small amount of biohydrogen was detected from the first stage of the two-stage reactor making this system attractive for biohythane production. As the digestate contains ammoniacal nitrogen, re-circulating it provided the necessary alkalinity in the systems, thus preventing an eventual failure by volatile fatty acids (VFA) accumulation. However, re-circulation also resulted in an ammonium accumulation, yielding a lower biomethane production. Based on the batch experimental results the 50% inhibitory concentration of total ammoniacal nitrogen on the methanogenic activities was calculated as 3.8g/L, corresponding to 146mg/L free ammonia for the inoculum used for this research. The two-stage system was affected by the inhibition more than the one-stage system, as it requires less alkalinity and the physically separated methanogens are more sensitive to inhibitory factors, such as ammonium and propionic acid.</abstract><cop>United States</cop><pub>Elsevier Ltd</pub><pmid>25613216</pmid><doi>10.1016/j.wasman.2014.12.001</doi><tpages>11</tpages></addata></record> |
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subjects | ACID NEUTRALIZING CAPACITY Alkalinity AMMONIA Ammonia - metabolism Ammonia inhibition ANAEROBIC DIGESTION Anaerobiosis Biofuels - analysis Biogas Bioreactors Buffer capacity CARBOXYLIC ACIDS Comparison of one-stage and two-stage CONCENTRATION RATIO ENERGY CONVERSION Failure FOOD Foods Garbage INORGANIC, ORGANIC, PHYSICAL AND ANALYTICAL CHEMISTRY MANAGEMENT OF RADIOACTIVE WASTES, AND NON-RADIOACTIVE WASTES FROM NUCLEAR FACILITIES METHANE Methane - analysis NITROGEN Nitrogen - metabolism PH VALUE PROPIONIC ACID Refuse Disposal - methods Solid Waste - analysis Total ammoniacal nitrogen TOXICITY VOLATILITY WASTES |
title | Effect of ammoniacal nitrogen on one-stage and two-stage anaerobic digestion of food waste |
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