Implementation of the IWA anaerobic digestion model No.1 (ADM1) for simulating digestion of blackwater from vacuum toilets
The IWA anaerobic digestion model No.1 (ADM1) is applied to the blackwater anaerobic digestion (BWAD) plant in this work. In order to verify the biochemical kinetics, batch experiments were executed. According to the Monod type kinetics, the maximum uptake rates (km) of butyric acid (HBu), propionic...
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| Veröffentlicht in: | Water science and technology 2006-01, Vol.53 (9), p.253-263 |
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| description | The IWA anaerobic digestion model No.1 (ADM1) is applied to the blackwater anaerobic digestion (BWAD) plant in this work. In order to verify the biochemical kinetics, batch experiments were executed. According to the Monod type kinetics, the maximum uptake rates (km) of butyric acid (HBu), propionic acid (HPr) and acetic acid (HAc) are testified as 18, 14, 13 d(-1), and their half saturation concentrations (Ks) are 110, 120, 160 g COD/m3, respectively. Afterwards, the model was calibrated based on the performance of a laboratory scale BWAD plant (under mesophilic conditions) by three scenario studies, i.e. the reference conditions, different feeding frequencies and high NH4+ concentration. The model successfully simulated three scenarios. The further two virtual scenario studies were achieved based on the calibrated model. First, the performance of BWAD plant was predicted with different hydraulic retention times (HRT); second, the kitchen refuse (KR) was added into the BWAD plant as additional organic loading. The model predicted the perspective of BW plus KR digestion and generated valuable suggestions for the operation of the real BWAD plant. |
| doi_str_mv | 10.2166/wst.2006.273 |
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In order to verify the biochemical kinetics, batch experiments were executed. According to the Monod type kinetics, the maximum uptake rates (km) of butyric acid (HBu), propionic acid (HPr) and acetic acid (HAc) are testified as 18, 14, 13 d(-1), and their half saturation concentrations (Ks) are 110, 120, 160 g COD/m3, respectively. Afterwards, the model was calibrated based on the performance of a laboratory scale BWAD plant (under mesophilic conditions) by three scenario studies, i.e. the reference conditions, different feeding frequencies and high NH4+ concentration. The model successfully simulated three scenarios. The further two virtual scenario studies were achieved based on the calibrated model. First, the performance of BWAD plant was predicted with different hydraulic retention times (HRT); second, the kitchen refuse (KR) was added into the BWAD plant as additional organic loading. The model predicted the perspective of BW plus KR digestion and generated valuable suggestions for the operation of the real BWAD plant.</description><identifier>ISSN: 0273-1223</identifier><identifier>ISBN: 9781843395683</identifier><identifier>ISBN: 1843395681</identifier><identifier>EISSN: 1996-9732</identifier><identifier>DOI: 10.2166/wst.2006.273</identifier><identifier>PMID: 16841750</identifier><language>eng</language><publisher>England: IWA Publishing</publisher><subject>Acetic acid ; Anaerobic digestion ; Anaerobic treatment ; Anaerobiosis ; Biogas ; Blackwater ; Butyric acid ; Computer simulation ; Digestion ; Experiments ; Facility Design and Construction ; Kinetics ; Laboratories ; Mathematical models ; Models, Structural ; Models, Theoretical ; Organic loading ; Parameter estimation ; Propionic acid ; Reactors ; Refuse ; Retention ; Sanitation ; Saturation ; Simulation ; Toilet Facilities ; Toilets ; Uptake ; Vacuum ; Water Purification - methods</subject><ispartof>Water science and technology, 2006-01, Vol.53 (9), p.253-263</ispartof><rights>Copyright IWA Publishing May 2006</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c311t-5c27bbf67a19cea7e31e65ded7378d56b6325880e5dfadfd5d0efb0e889afb793</citedby></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>309,310,314,776,780,785,786,27901,27902</link.rule.ids><backlink>$$Uhttps://www.ncbi.nlm.nih.gov/pubmed/16841750$$D View this record in MEDLINE/PubMed$$Hfree_for_read</backlink></links><search><contributor>Wang, XC</contributor><creatorcontrib>Feng, Y</creatorcontrib><creatorcontrib>Behrendt, J</creatorcontrib><creatorcontrib>Wendland, C</creatorcontrib><creatorcontrib>Otterpohl, R</creatorcontrib><title>Implementation of the IWA anaerobic digestion model No.1 (ADM1) for simulating digestion of blackwater from vacuum toilets</title><title>Water science and technology</title><addtitle>Water Sci Technol</addtitle><description>The IWA anaerobic digestion model No.1 (ADM1) is applied to the blackwater anaerobic digestion (BWAD) plant in this work. In order to verify the biochemical kinetics, batch experiments were executed. According to the Monod type kinetics, the maximum uptake rates (km) of butyric acid (HBu), propionic acid (HPr) and acetic acid (HAc) are testified as 18, 14, 13 d(-1), and their half saturation concentrations (Ks) are 110, 120, 160 g COD/m3, respectively. Afterwards, the model was calibrated based on the performance of a laboratory scale BWAD plant (under mesophilic conditions) by three scenario studies, i.e. the reference conditions, different feeding frequencies and high NH4+ concentration. The model successfully simulated three scenarios. The further two virtual scenario studies were achieved based on the calibrated model. First, the performance of BWAD plant was predicted with different hydraulic retention times (HRT); second, the kitchen refuse (KR) was added into the BWAD plant as additional organic loading. The model predicted the perspective of BW plus KR digestion and generated valuable suggestions for the operation of the real BWAD plant.</description><subject>Acetic acid</subject><subject>Anaerobic digestion</subject><subject>Anaerobic treatment</subject><subject>Anaerobiosis</subject><subject>Biogas</subject><subject>Blackwater</subject><subject>Butyric acid</subject><subject>Computer simulation</subject><subject>Digestion</subject><subject>Experiments</subject><subject>Facility Design and Construction</subject><subject>Kinetics</subject><subject>Laboratories</subject><subject>Mathematical models</subject><subject>Models, Structural</subject><subject>Models, Theoretical</subject><subject>Organic loading</subject><subject>Parameter estimation</subject><subject>Propionic acid</subject><subject>Reactors</subject><subject>Refuse</subject><subject>Retention</subject><subject>Sanitation</subject><subject>Saturation</subject><subject>Simulation</subject><subject>Toilet Facilities</subject><subject>Toilets</subject><subject>Uptake</subject><subject>Vacuum</subject><subject>Water Purification - methods</subject><issn>0273-1223</issn><issn>1996-9732</issn><isbn>9781843395683</isbn><isbn>1843395681</isbn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2006</creationdate><recordtype>article</recordtype><sourceid>EIF</sourceid><sourceid>BENPR</sourceid><recordid>eNqFkctu1DAUQC0eosPQHWtkCQkViQx-xK_lqPQxUoENiGXkxNclJY6ndkJFv76ediQQC1h54eOj63sQeknJilEp39_kacUIkSum-CO0oMbIyijOHqNDozTVNedGSM2foAUpSEUZ4wfoec5XhBDFa_IMHVCpa6oEWaDbTdgOEGCc7NTHEUePp--AN9_W2I4WUmz7Drv-EvL9dYgOBvwprig-Wn_4SN9iHxPOfZiH8n68_AMtpnaw3Y8bO0HCPsWAf9pungOeYj_AlF-gp94OGQ735xJ9PT35cnxeXXw-2xyvL6qOUzpVomOqbb1UlpoOrAJOQQoHTnGlnZCt5ExoTUA4b513whHwLQGtjfWtMnyJ3jx4tylez2W6JvS5g2GwI8Q5N1JLLoQi_wWp4XVZ78549G-QsFoKyiUr6Ou_0Ks4p7H8t-hqLum9conePVBdijkn8M029cGmX0XV7Ko3pXqzq96UpAV_tZfObQD3G95n5XcpbqXE</recordid><startdate>20060101</startdate><enddate>20060101</enddate><creator>Feng, Y</creator><creator>Behrendt, J</creator><creator>Wendland, C</creator><creator>Otterpohl, R</creator><general>IWA Publishing</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>3V.</scope><scope>7QH</scope><scope>7UA</scope><scope>7X7</scope><scope>7XB</scope><scope>88E</scope><scope>8FE</scope><scope>8FG</scope><scope>8FI</scope><scope>8FJ</scope><scope>8FK</scope><scope>ABJCF</scope><scope>ABUWG</scope><scope>AEUYN</scope><scope>AFKRA</scope><scope>BENPR</scope><scope>BGLVJ</scope><scope>BHPHI</scope><scope>BKSAR</scope><scope>C1K</scope><scope>CCPQU</scope><scope>DWQXO</scope><scope>F1W</scope><scope>FYUFA</scope><scope>GHDGH</scope><scope>H96</scope><scope>H97</scope><scope>HCIFZ</scope><scope>K9.</scope><scope>L.G</scope><scope>L6V</scope><scope>M0S</scope><scope>M1P</scope><scope>M7S</scope><scope>PCBAR</scope><scope>PQEST</scope><scope>PQQKQ</scope><scope>PQUKI</scope><scope>PTHSS</scope><scope>7X8</scope></search><sort><creationdate>20060101</creationdate><title>Implementation of the IWA anaerobic digestion model No.1 (ADM1) for simulating digestion of blackwater from vacuum toilets</title><author>Feng, Y ; Behrendt, J ; Wendland, C ; Otterpohl, R</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c311t-5c27bbf67a19cea7e31e65ded7378d56b6325880e5dfadfd5d0efb0e889afb793</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2006</creationdate><topic>Acetic acid</topic><topic>Anaerobic digestion</topic><topic>Anaerobic treatment</topic><topic>Anaerobiosis</topic><topic>Biogas</topic><topic>Blackwater</topic><topic>Butyric acid</topic><topic>Computer simulation</topic><topic>Digestion</topic><topic>Experiments</topic><topic>Facility Design and Construction</topic><topic>Kinetics</topic><topic>Laboratories</topic><topic>Mathematical models</topic><topic>Models, Structural</topic><topic>Models, Theoretical</topic><topic>Organic loading</topic><topic>Parameter estimation</topic><topic>Propionic acid</topic><topic>Reactors</topic><topic>Refuse</topic><topic>Retention</topic><topic>Sanitation</topic><topic>Saturation</topic><topic>Simulation</topic><topic>Toilet Facilities</topic><topic>Toilets</topic><topic>Uptake</topic><topic>Vacuum</topic><topic>Water Purification - methods</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Feng, Y</creatorcontrib><creatorcontrib>Behrendt, J</creatorcontrib><creatorcontrib>Wendland, C</creatorcontrib><creatorcontrib>Otterpohl, R</creatorcontrib><collection>Medline</collection><collection>MEDLINE</collection><collection>MEDLINE (Ovid)</collection><collection>MEDLINE</collection><collection>MEDLINE</collection><collection>PubMed</collection><collection>CrossRef</collection><collection>ProQuest Central (Corporate)</collection><collection>Aqualine</collection><collection>Water Resources Abstracts</collection><collection>Health & Medical Collection</collection><collection>ProQuest Central (purchase pre-March 2016)</collection><collection>Medical Database (Alumni Edition)</collection><collection>ProQuest SciTech Collection</collection><collection>ProQuest Technology Collection</collection><collection>Hospital Premium Collection</collection><collection>Hospital Premium Collection (Alumni Edition)</collection><collection>ProQuest Central (Alumni) (purchase pre-March 2016)</collection><collection>Materials Science & Engineering Collection</collection><collection>ProQuest Central (Alumni Edition)</collection><collection>ProQuest One Sustainability</collection><collection>ProQuest Central UK/Ireland</collection><collection>ProQuest Central</collection><collection>Technology Collection</collection><collection>Natural Science Collection</collection><collection>Earth, Atmospheric & Aquatic Science Collection</collection><collection>Environmental Sciences and Pollution Management</collection><collection>ProQuest One Community College</collection><collection>ProQuest Central Korea</collection><collection>ASFA: Aquatic Sciences and Fisheries Abstracts</collection><collection>Health Research Premium Collection</collection><collection>Health Research Premium Collection (Alumni)</collection><collection>Aquatic Science & Fisheries Abstracts (ASFA) 2: Ocean Technology, Policy & Non-Living Resources</collection><collection>Aquatic Science & Fisheries Abstracts (ASFA) 3: Aquatic Pollution & Environmental Quality</collection><collection>SciTech Premium Collection</collection><collection>ProQuest Health & Medical Complete (Alumni)</collection><collection>Aquatic Science & Fisheries Abstracts (ASFA) Professional</collection><collection>ProQuest Engineering Collection</collection><collection>Health & Medical Collection (Alumni Edition)</collection><collection>Medical Database</collection><collection>Engineering Database</collection><collection>Earth, Atmospheric & Aquatic Science Database</collection><collection>ProQuest One Academic Eastern Edition (DO NOT USE)</collection><collection>ProQuest One Academic</collection><collection>ProQuest One Academic UKI Edition</collection><collection>Engineering Collection</collection><collection>MEDLINE - Academic</collection><jtitle>Water science and technology</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Feng, Y</au><au>Behrendt, J</au><au>Wendland, C</au><au>Otterpohl, R</au><au>Wang, XC</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Implementation of the IWA anaerobic digestion model No.1 (ADM1) for simulating digestion of blackwater from vacuum toilets</atitle><jtitle>Water science and technology</jtitle><addtitle>Water Sci Technol</addtitle><date>2006-01-01</date><risdate>2006</risdate><volume>53</volume><issue>9</issue><spage>253</spage><epage>263</epage><pages>253-263</pages><issn>0273-1223</issn><eissn>1996-9732</eissn><isbn>9781843395683</isbn><isbn>1843395681</isbn><abstract>The IWA anaerobic digestion model No.1 (ADM1) is applied to the blackwater anaerobic digestion (BWAD) plant in this work. In order to verify the biochemical kinetics, batch experiments were executed. According to the Monod type kinetics, the maximum uptake rates (km) of butyric acid (HBu), propionic acid (HPr) and acetic acid (HAc) are testified as 18, 14, 13 d(-1), and their half saturation concentrations (Ks) are 110, 120, 160 g COD/m3, respectively. Afterwards, the model was calibrated based on the performance of a laboratory scale BWAD plant (under mesophilic conditions) by three scenario studies, i.e. the reference conditions, different feeding frequencies and high NH4+ concentration. The model successfully simulated three scenarios. The further two virtual scenario studies were achieved based on the calibrated model. First, the performance of BWAD plant was predicted with different hydraulic retention times (HRT); second, the kitchen refuse (KR) was added into the BWAD plant as additional organic loading. The model predicted the perspective of BW plus KR digestion and generated valuable suggestions for the operation of the real BWAD plant.</abstract><cop>England</cop><pub>IWA Publishing</pub><pmid>16841750</pmid><doi>10.2166/wst.2006.273</doi><tpages>11</tpages></addata></record> |
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| ispartof | Water science and technology, 2006-01, Vol.53 (9), p.253-263 |
| issn | 0273-1223 1996-9732 |
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| subjects | Acetic acid Anaerobic digestion Anaerobic treatment Anaerobiosis Biogas Blackwater Butyric acid Computer simulation Digestion Experiments Facility Design and Construction Kinetics Laboratories Mathematical models Models, Structural Models, Theoretical Organic loading Parameter estimation Propionic acid Reactors Refuse Retention Sanitation Saturation Simulation Toilet Facilities Toilets Uptake Vacuum Water Purification - methods |
| title | Implementation of the IWA anaerobic digestion model No.1 (ADM1) for simulating digestion of blackwater from vacuum toilets |
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