Sugarcane Bagasse as a Co-Substrate with Oil-Refinery Biological Sludge for Biogas Production Using Batch Mesophilic Anaerobic Co-Digestion Technology: Effect of Carbon/Nitrogen Ratio
Man-made organic waste leads to the rapid proliferation of pollution around the globe. Effective bio-waste management can help to reduce the adverse effects of organic waste while contributing to the circular economy at the same time. The toxic oily-biological sludge generated from oil refineries’ w...
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creator | Ghaleb, Aiban Abdulhakim Saeed Kutty, Shamsul Rahman Mohamed Salih, Gasim Hayder Ahmed Jagaba, Ahmad Hussaini Noor, Azmatullah Kumar, Vicky Almahbashi, Najib Mohammed Yahya Saeed, Anwar Ameen Hezam Saleh Al-dhawi, Baker Nasser |
description | Man-made organic waste leads to the rapid proliferation of pollution around the globe. Effective bio-waste management can help to reduce the adverse effects of organic waste while contributing to the circular economy at the same time. The toxic oily-biological sludge generated from oil refineries’ wastewater treatment plants is a potential source for biogas energy recovery via anaerobic digestion. However, the oily-biological sludge’s carbon/nitrogen (C/N) ratio is lower than the ideal 20–30 ratio required by anaerobic digestion technology for biogas production. Sugarcane bagasse can be digested as a high C/N co-substrate while the oily-biological sludge acts as a substrate and inoculum to improve biogas production. In this study, the best C/N with co-substrate volatile solids (VS)/inoculum VS ratios for the co-digestion process of mixtures were determined empirically through batch experiments at temperatures of 35–37 °C, pH (6–8) and 60 rpm mixing. The raw materials were pre-treated mechanically and thermo-chemically to further enhance the digestibility. The best condition for the sugarcane bagasse delignification process was 1% (w/v) sodium hydroxide, 1:10 solid-liquid ratio, at 100 °C, and 150 rpm for 1 h. The results from a 33-day batch anaerobic digestion experiment indicate that the production of biogas and methane yield were concurrent with the increasing C/N and co-substrate VS/inoculum VS ratios. The total biogas yields from C/N 20.0 with co-substrate VS/inoculum VS 0.06 and C/N 30.0 with co-substrate VS/inoculum VS 0.18 ratios were 2777.0 and 9268.0 mL, respectively, including a methane yield of 980.0 and 3009.3 mL, respectively. The biogas and methane yield from C/N 30.0 were higher than the biogas and methane yields from C/N 20.0 by 70.04 and 67.44%, respectively. The highest biogas and methane yields corresponded with the highest C/N with co-substrate VS/inoculum VS ratios (30.0 and 0.18), being 200.6 mL/g VSremoved and 65.1 mL CH4/g VSremoved, respectively. |
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Effective bio-waste management can help to reduce the adverse effects of organic waste while contributing to the circular economy at the same time. The toxic oily-biological sludge generated from oil refineries’ wastewater treatment plants is a potential source for biogas energy recovery via anaerobic digestion. However, the oily-biological sludge’s carbon/nitrogen (C/N) ratio is lower than the ideal 20–30 ratio required by anaerobic digestion technology for biogas production. Sugarcane bagasse can be digested as a high C/N co-substrate while the oily-biological sludge acts as a substrate and inoculum to improve biogas production. In this study, the best C/N with co-substrate volatile solids (VS)/inoculum VS ratios for the co-digestion process of mixtures were determined empirically through batch experiments at temperatures of 35–37 °C, pH (6–8) and 60 rpm mixing. The raw materials were pre-treated mechanically and thermo-chemically to further enhance the digestibility. The best condition for the sugarcane bagasse delignification process was 1% (w/v) sodium hydroxide, 1:10 solid-liquid ratio, at 100 °C, and 150 rpm for 1 h. The results from a 33-day batch anaerobic digestion experiment indicate that the production of biogas and methane yield were concurrent with the increasing C/N and co-substrate VS/inoculum VS ratios. The total biogas yields from C/N 20.0 with co-substrate VS/inoculum VS 0.06 and C/N 30.0 with co-substrate VS/inoculum VS 0.18 ratios were 2777.0 and 9268.0 mL, respectively, including a methane yield of 980.0 and 3009.3 mL, respectively. The biogas and methane yield from C/N 30.0 were higher than the biogas and methane yields from C/N 20.0 by 70.04 and 67.44%, respectively. The highest biogas and methane yields corresponded with the highest C/N with co-substrate VS/inoculum VS ratios (30.0 and 0.18), being 200.6 mL/g VSremoved and 65.1 mL CH4/g VSremoved, respectively.</description><identifier>ISSN: 2073-4441</identifier><identifier>EISSN: 2073-4441</identifier><identifier>DOI: 10.3390/w13050590</identifier><language>eng</language><publisher>Basel: MDPI AG</publisher><subject>Agricultural production ; Air pollution ; Alternative energy sources ; Anaerobic digestion ; Bagasse ; Biogas ; Biomass energy ; Carbon ; Carbon/nitrogen ratio ; Caustic soda ; Cellulose ; Combustion ; Digestibility ; Electric utilities ; Emissions ; Energy recovery ; Fourier transforms ; Greenhouse gases ; Inoculum ; Lignin ; Methane ; Methods ; Moisture content ; Nitrogen ; Oil refineries ; Organic wastes ; Petroleum industry ; Pollution effects ; Raw materials ; Refineries ; Refinery wastes ; Refuse as fuel ; Sludge ; Sludge digestion ; Sodium hydroxide ; Substrates ; Sugarcane ; Technology ; Volatile solids ; Waste management ; Wastewater treatment ; Wastewater treatment plants ; Water treatment ; Yield</subject><ispartof>Water (Basel), 2021-03, Vol.13 (5), p.590</ispartof><rights>COPYRIGHT 2021 MDPI AG</rights><rights>2021. This work is licensed under http://creativecommons.org/licenses/by/3.0/ (the “License”). Notwithstanding the ProQuest Terms and Conditions, you may use this content in accordance with the terms of the License.</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c331t-7861880fa16f5c97a4173db6bb89e295e689f2011caaa9249127dabeef8235e93</citedby><cites>FETCH-LOGICAL-c331t-7861880fa16f5c97a4173db6bb89e295e689f2011caaa9249127dabeef8235e93</cites><orcidid>0000-0003-0728-7676 ; 0000-0002-0241-8764 ; 0000-0002-8624-8394 ; 0000-0001-6095-5739 ; 0000-0002-6022-4749 ; 0000-0002-3304-3790 ; 0000-0002-2677-0367</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27923,27924</link.rule.ids></links><search><creatorcontrib>Ghaleb, Aiban Abdulhakim Saeed</creatorcontrib><creatorcontrib>Kutty, Shamsul Rahman Mohamed</creatorcontrib><creatorcontrib>Salih, Gasim Hayder Ahmed</creatorcontrib><creatorcontrib>Jagaba, Ahmad Hussaini</creatorcontrib><creatorcontrib>Noor, Azmatullah</creatorcontrib><creatorcontrib>Kumar, Vicky</creatorcontrib><creatorcontrib>Almahbashi, Najib Mohammed Yahya</creatorcontrib><creatorcontrib>Saeed, Anwar Ameen Hezam</creatorcontrib><creatorcontrib>Saleh Al-dhawi, Baker Nasser</creatorcontrib><title>Sugarcane Bagasse as a Co-Substrate with Oil-Refinery Biological Sludge for Biogas Production Using Batch Mesophilic Anaerobic Co-Digestion Technology: Effect of Carbon/Nitrogen Ratio</title><title>Water (Basel)</title><description>Man-made organic waste leads to the rapid proliferation of pollution around the globe. Effective bio-waste management can help to reduce the adverse effects of organic waste while contributing to the circular economy at the same time. The toxic oily-biological sludge generated from oil refineries’ wastewater treatment plants is a potential source for biogas energy recovery via anaerobic digestion. However, the oily-biological sludge’s carbon/nitrogen (C/N) ratio is lower than the ideal 20–30 ratio required by anaerobic digestion technology for biogas production. Sugarcane bagasse can be digested as a high C/N co-substrate while the oily-biological sludge acts as a substrate and inoculum to improve biogas production. In this study, the best C/N with co-substrate volatile solids (VS)/inoculum VS ratios for the co-digestion process of mixtures were determined empirically through batch experiments at temperatures of 35–37 °C, pH (6–8) and 60 rpm mixing. The raw materials were pre-treated mechanically and thermo-chemically to further enhance the digestibility. The best condition for the sugarcane bagasse delignification process was 1% (w/v) sodium hydroxide, 1:10 solid-liquid ratio, at 100 °C, and 150 rpm for 1 h. The results from a 33-day batch anaerobic digestion experiment indicate that the production of biogas and methane yield were concurrent with the increasing C/N and co-substrate VS/inoculum VS ratios. The total biogas yields from C/N 20.0 with co-substrate VS/inoculum VS 0.06 and C/N 30.0 with co-substrate VS/inoculum VS 0.18 ratios were 2777.0 and 9268.0 mL, respectively, including a methane yield of 980.0 and 3009.3 mL, respectively. The biogas and methane yield from C/N 30.0 were higher than the biogas and methane yields from C/N 20.0 by 70.04 and 67.44%, respectively. The highest biogas and methane yields corresponded with the highest C/N with co-substrate VS/inoculum VS ratios (30.0 and 0.18), being 200.6 mL/g VSremoved and 65.1 mL CH4/g VSremoved, respectively.</description><subject>Agricultural production</subject><subject>Air pollution</subject><subject>Alternative energy sources</subject><subject>Anaerobic digestion</subject><subject>Bagasse</subject><subject>Biogas</subject><subject>Biomass energy</subject><subject>Carbon</subject><subject>Carbon/nitrogen ratio</subject><subject>Caustic soda</subject><subject>Cellulose</subject><subject>Combustion</subject><subject>Digestibility</subject><subject>Electric utilities</subject><subject>Emissions</subject><subject>Energy recovery</subject><subject>Fourier transforms</subject><subject>Greenhouse gases</subject><subject>Inoculum</subject><subject>Lignin</subject><subject>Methane</subject><subject>Methods</subject><subject>Moisture content</subject><subject>Nitrogen</subject><subject>Oil refineries</subject><subject>Organic wastes</subject><subject>Petroleum industry</subject><subject>Pollution effects</subject><subject>Raw materials</subject><subject>Refineries</subject><subject>Refinery wastes</subject><subject>Refuse as fuel</subject><subject>Sludge</subject><subject>Sludge digestion</subject><subject>Sodium hydroxide</subject><subject>Substrates</subject><subject>Sugarcane</subject><subject>Technology</subject><subject>Volatile solids</subject><subject>Waste management</subject><subject>Wastewater treatment</subject><subject>Wastewater treatment plants</subject><subject>Water treatment</subject><subject>Yield</subject><issn>2073-4441</issn><issn>2073-4441</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2021</creationdate><recordtype>article</recordtype><sourceid>ABUWG</sourceid><sourceid>AFKRA</sourceid><sourceid>AZQEC</sourceid><sourceid>BENPR</sourceid><sourceid>CCPQU</sourceid><sourceid>DWQXO</sourceid><recordid>eNpNkc1OHDEMx0cVlYqAQ9_AUk8cBpLJfCTclmWhSLRULJxHnowzGzQk22RGaJ-sr9dst6pqH2xZP_9t2Vn2mbMLIRS7fOeCVaxS7EN2XLBG5GVZ8qP_8k_ZWYyvLFmppKzYcfZrPQ8YNDqCaxwwRgKMgLD0-Xru4hRwIni30wYe7Zg_kbGOwg6urR_9YDWOsB7nfiAwPuyrSQJ-BN_PerLewUu0bkjKk97AN4p-u7Gj1bBwSMF3KUtzbuxA8Q_9THrj9sK7K1gZQ3oCb2CJofPu8rudgh_IwRMm-DT7aHCMdPY3nmQvt6vn5df84fHufrl4yLUQfMobWXMpmUFem0qrBkveiL6ru04qKlRFtVSmYJxrRFRFqXjR9NgRGVmIipQ4yb4cdLfB_5zTnu2rn4NLI9tEl5KxumaJujhQA47UWmd8OpxO3tOb1d6ls6X6olGiqFkly9RwfmjQwccYyLTbYN8w7FrO2v0v23-_FL8BEtmSHg</recordid><startdate>20210301</startdate><enddate>20210301</enddate><creator>Ghaleb, Aiban Abdulhakim Saeed</creator><creator>Kutty, Shamsul Rahman Mohamed</creator><creator>Salih, Gasim Hayder Ahmed</creator><creator>Jagaba, Ahmad Hussaini</creator><creator>Noor, Azmatullah</creator><creator>Kumar, Vicky</creator><creator>Almahbashi, Najib Mohammed Yahya</creator><creator>Saeed, Anwar Ameen Hezam</creator><creator>Saleh Al-dhawi, Baker Nasser</creator><general>MDPI AG</general><scope>AAYXX</scope><scope>CITATION</scope><scope>ABUWG</scope><scope>AFKRA</scope><scope>AZQEC</scope><scope>BENPR</scope><scope>CCPQU</scope><scope>DWQXO</scope><scope>PIMPY</scope><scope>PQEST</scope><scope>PQQKQ</scope><scope>PQUKI</scope><scope>PRINS</scope><orcidid>https://orcid.org/0000-0003-0728-7676</orcidid><orcidid>https://orcid.org/0000-0002-0241-8764</orcidid><orcidid>https://orcid.org/0000-0002-8624-8394</orcidid><orcidid>https://orcid.org/0000-0001-6095-5739</orcidid><orcidid>https://orcid.org/0000-0002-6022-4749</orcidid><orcidid>https://orcid.org/0000-0002-3304-3790</orcidid><orcidid>https://orcid.org/0000-0002-2677-0367</orcidid></search><sort><creationdate>20210301</creationdate><title>Sugarcane Bagasse as a Co-Substrate with Oil-Refinery Biological Sludge for Biogas Production Using Batch Mesophilic Anaerobic Co-Digestion Technology: Effect of Carbon/Nitrogen Ratio</title><author>Ghaleb, Aiban Abdulhakim Saeed ; Kutty, Shamsul Rahman Mohamed ; Salih, Gasim Hayder Ahmed ; Jagaba, Ahmad Hussaini ; Noor, Azmatullah ; Kumar, Vicky ; Almahbashi, Najib Mohammed Yahya ; Saeed, Anwar Ameen Hezam ; Saleh Al-dhawi, Baker Nasser</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c331t-7861880fa16f5c97a4173db6bb89e295e689f2011caaa9249127dabeef8235e93</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2021</creationdate><topic>Agricultural production</topic><topic>Air pollution</topic><topic>Alternative energy sources</topic><topic>Anaerobic digestion</topic><topic>Bagasse</topic><topic>Biogas</topic><topic>Biomass energy</topic><topic>Carbon</topic><topic>Carbon/nitrogen ratio</topic><topic>Caustic soda</topic><topic>Cellulose</topic><topic>Combustion</topic><topic>Digestibility</topic><topic>Electric utilities</topic><topic>Emissions</topic><topic>Energy recovery</topic><topic>Fourier transforms</topic><topic>Greenhouse gases</topic><topic>Inoculum</topic><topic>Lignin</topic><topic>Methane</topic><topic>Methods</topic><topic>Moisture content</topic><topic>Nitrogen</topic><topic>Oil refineries</topic><topic>Organic wastes</topic><topic>Petroleum industry</topic><topic>Pollution effects</topic><topic>Raw materials</topic><topic>Refineries</topic><topic>Refinery wastes</topic><topic>Refuse as fuel</topic><topic>Sludge</topic><topic>Sludge digestion</topic><topic>Sodium hydroxide</topic><topic>Substrates</topic><topic>Sugarcane</topic><topic>Technology</topic><topic>Volatile solids</topic><topic>Waste management</topic><topic>Wastewater treatment</topic><topic>Wastewater treatment plants</topic><topic>Water treatment</topic><topic>Yield</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Ghaleb, Aiban Abdulhakim Saeed</creatorcontrib><creatorcontrib>Kutty, Shamsul Rahman Mohamed</creatorcontrib><creatorcontrib>Salih, Gasim Hayder Ahmed</creatorcontrib><creatorcontrib>Jagaba, Ahmad Hussaini</creatorcontrib><creatorcontrib>Noor, Azmatullah</creatorcontrib><creatorcontrib>Kumar, Vicky</creatorcontrib><creatorcontrib>Almahbashi, Najib Mohammed Yahya</creatorcontrib><creatorcontrib>Saeed, Anwar Ameen Hezam</creatorcontrib><creatorcontrib>Saleh Al-dhawi, Baker Nasser</creatorcontrib><collection>CrossRef</collection><collection>ProQuest Central (Alumni Edition)</collection><collection>ProQuest Central UK/Ireland</collection><collection>ProQuest Central Essentials</collection><collection>ProQuest Central</collection><collection>ProQuest One Community College</collection><collection>ProQuest Central Korea</collection><collection>Publicly Available Content 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>ProQuest Central China</collection><jtitle>Water (Basel)</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Ghaleb, Aiban Abdulhakim Saeed</au><au>Kutty, Shamsul Rahman Mohamed</au><au>Salih, Gasim Hayder Ahmed</au><au>Jagaba, Ahmad Hussaini</au><au>Noor, Azmatullah</au><au>Kumar, Vicky</au><au>Almahbashi, Najib Mohammed Yahya</au><au>Saeed, Anwar Ameen Hezam</au><au>Saleh Al-dhawi, Baker Nasser</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Sugarcane Bagasse as a Co-Substrate with Oil-Refinery Biological Sludge for Biogas Production Using Batch Mesophilic Anaerobic Co-Digestion Technology: Effect of Carbon/Nitrogen Ratio</atitle><jtitle>Water (Basel)</jtitle><date>2021-03-01</date><risdate>2021</risdate><volume>13</volume><issue>5</issue><spage>590</spage><pages>590-</pages><issn>2073-4441</issn><eissn>2073-4441</eissn><abstract>Man-made organic waste leads to the rapid proliferation of pollution around the globe. Effective bio-waste management can help to reduce the adverse effects of organic waste while contributing to the circular economy at the same time. The toxic oily-biological sludge generated from oil refineries’ wastewater treatment plants is a potential source for biogas energy recovery via anaerobic digestion. However, the oily-biological sludge’s carbon/nitrogen (C/N) ratio is lower than the ideal 20–30 ratio required by anaerobic digestion technology for biogas production. Sugarcane bagasse can be digested as a high C/N co-substrate while the oily-biological sludge acts as a substrate and inoculum to improve biogas production. In this study, the best C/N with co-substrate volatile solids (VS)/inoculum VS ratios for the co-digestion process of mixtures were determined empirically through batch experiments at temperatures of 35–37 °C, pH (6–8) and 60 rpm mixing. The raw materials were pre-treated mechanically and thermo-chemically to further enhance the digestibility. The best condition for the sugarcane bagasse delignification process was 1% (w/v) sodium hydroxide, 1:10 solid-liquid ratio, at 100 °C, and 150 rpm for 1 h. The results from a 33-day batch anaerobic digestion experiment indicate that the production of biogas and methane yield were concurrent with the increasing C/N and co-substrate VS/inoculum VS ratios. The total biogas yields from C/N 20.0 with co-substrate VS/inoculum VS 0.06 and C/N 30.0 with co-substrate VS/inoculum VS 0.18 ratios were 2777.0 and 9268.0 mL, respectively, including a methane yield of 980.0 and 3009.3 mL, respectively. The biogas and methane yield from C/N 30.0 were higher than the biogas and methane yields from C/N 20.0 by 70.04 and 67.44%, respectively. The highest biogas and methane yields corresponded with the highest C/N with co-substrate VS/inoculum VS ratios (30.0 and 0.18), being 200.6 mL/g VSremoved and 65.1 mL CH4/g VSremoved, respectively.</abstract><cop>Basel</cop><pub>MDPI AG</pub><doi>10.3390/w13050590</doi><orcidid>https://orcid.org/0000-0003-0728-7676</orcidid><orcidid>https://orcid.org/0000-0002-0241-8764</orcidid><orcidid>https://orcid.org/0000-0002-8624-8394</orcidid><orcidid>https://orcid.org/0000-0001-6095-5739</orcidid><orcidid>https://orcid.org/0000-0002-6022-4749</orcidid><orcidid>https://orcid.org/0000-0002-3304-3790</orcidid><orcidid>https://orcid.org/0000-0002-2677-0367</orcidid><oa>free_for_read</oa></addata></record> |
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subjects | Agricultural production Air pollution Alternative energy sources Anaerobic digestion Bagasse Biogas Biomass energy Carbon Carbon/nitrogen ratio Caustic soda Cellulose Combustion Digestibility Electric utilities Emissions Energy recovery Fourier transforms Greenhouse gases Inoculum Lignin Methane Methods Moisture content Nitrogen Oil refineries Organic wastes Petroleum industry Pollution effects Raw materials Refineries Refinery wastes Refuse as fuel Sludge Sludge digestion Sodium hydroxide Substrates Sugarcane Technology Volatile solids Waste management Wastewater treatment Wastewater treatment plants Water treatment Yield |
title | Sugarcane Bagasse as a Co-Substrate with Oil-Refinery Biological Sludge for Biogas Production Using Batch Mesophilic Anaerobic Co-Digestion Technology: Effect of Carbon/Nitrogen Ratio |
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