Techno-economic modeling of an integrated biomethane-biomethanol production process via biomass gasification, electrolysis, biomethanation, and catalytic methanol synthesis
Biological methanation (biomethanation) of syngas obtained from biomass gasification offers the opportunity to employ a low-pressure, low-temperature process to produce storable bio-derived substitute natural gas (bSNG), although its economic viability is limited by high energy and biomass costs. Re...
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description | Biological methanation (biomethanation) of syngas obtained from biomass gasification offers the opportunity to employ a low-pressure, low-temperature process to produce storable bio-derived substitute natural gas (bSNG), although its economic viability is limited by high energy and biomass costs. Research on syngas biomethanation techno-economic performance is limited and novel biomass-to-biomethane process configurations are required in order to assess opportunities for the enhancement of its efficiency and economic feasibility. In this study, we carried out the techno-economic modeling of two processes comprising integrated biomass gasification, electrolysis, and syngas biomethanation with combined heat and power recovery in order to assess and compare their fuel yields, energy efficiency, carbon efficiency, and bSNG minimum selling price (MSP). The first process operates standalone biomethanation (SAB) of syngas and can produce approximately 38,000 Nm
3
of bSNG per day, with a total plant efficiency of 50.6%. The second process (integrated biomethane-biomethanol, IBB) exploits the unconverted carbon stream from the biomethanation process to recover energy and synthesize methanol via direct catalytic CO
2
hydrogenation. In addition to the same bSNG output, the IBB process can produce 10 t/day of biomethanol, at a 99% purity. The IBB process shows little global energy efficiency gains in comparison with SAB (51.7%) due to the large increase in electrolytic hydrogen demand, but it shows a substantial improvement in biomass-to-fuel carbon efficiency (33 vs. 26%). The SAB and IBB processes generate a bSNG MSP of 2.38 €/Nm
3
and 3.68 €/Nm
3
, respectively. Hydrogenation of unconverted carbon in biomass-to-biomethane processes comes with high additional capital and operating costs due to the large-scale electrolysis plants required. Consequently, in both processes, the market price gap of the bSNG produced is 0.13 €/kWh
bSNG
(SAB) and 0.25 €/kWh
bSNG
(IBB) even under the most optimistic cost scenarios considered, and it is primarily influenced by the cost of surplus electricity utilized in electrolysis, while the selling price of biomethanol exerts a very limited influence on process economics. Intensive subsidization would be required in order to sustain the decentralized production of bSNG through both processes. Despite their limited economic competitiveness, both processes have a size comparable with existing renewable gas production plants in terms of bSN |
doi_str_mv | 10.1007/s13399-020-01178-y |
format | Article |
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3
of bSNG per day, with a total plant efficiency of 50.6%. The second process (integrated biomethane-biomethanol, IBB) exploits the unconverted carbon stream from the biomethanation process to recover energy and synthesize methanol via direct catalytic CO
2
hydrogenation. In addition to the same bSNG output, the IBB process can produce 10 t/day of biomethanol, at a 99% purity. The IBB process shows little global energy efficiency gains in comparison with SAB (51.7%) due to the large increase in electrolytic hydrogen demand, but it shows a substantial improvement in biomass-to-fuel carbon efficiency (33 vs. 26%). The SAB and IBB processes generate a bSNG MSP of 2.38 €/Nm
3
and 3.68 €/Nm
3
, respectively. Hydrogenation of unconverted carbon in biomass-to-biomethane processes comes with high additional capital and operating costs due to the large-scale electrolysis plants required. Consequently, in both processes, the market price gap of the bSNG produced is 0.13 €/kWh
bSNG
(SAB) and 0.25 €/kWh
bSNG
(IBB) even under the most optimistic cost scenarios considered, and it is primarily influenced by the cost of surplus electricity utilized in electrolysis, while the selling price of biomethanol exerts a very limited influence on process economics. Intensive subsidization would be required in order to sustain the decentralized production of bSNG through both processes. Despite their limited economic competitiveness, both processes have a size comparable with existing renewable gas production plants in terms of bSNG production capacity and the IBB process is of a size adequate for the supply of biomethanol to a decentralized biorenewable supply chain.</description><identifier>ISSN: 2190-6815</identifier><identifier>EISSN: 2190-6823</identifier><identifier>DOI: 10.1007/s13399-020-01178-y</identifier><language>eng</language><publisher>Berlin/Heidelberg: Springer Berlin Heidelberg</publisher><subject>Biogas ; Biomass ; Biomass energy production ; Biotechnology ; Carbon ; Cogeneration ; Economic models ; Electrolysis ; Energy ; Energy costs ; Energy efficiency ; Feasibility studies ; Fuels ; Gasification ; Heat recovery ; Hydrogenation ; Low pressure ; Low temperature ; Methanation ; Methanol ; Modelling ; Operating costs ; Original Article ; Renewable and Green Energy ; Substitute natural gas ; Supply chains ; Synthesis gas</subject><ispartof>Biomass conversion and biorefinery, 2023-01, Vol.13 (2), p.977-998</ispartof><rights>The Author(s) 2020. corrected publication 2021</rights><rights>The Author(s) 2020. corrected publication 2021. This work is published under http://creativecommons.org/licenses/by/4.0/ (the “License”). Notwithstanding the ProQuest Terms and Conditions, you may use this content in accordance with the terms of the License.</rights><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c363t-c1bcf935be223395260ed6bf733d4362ab101a58888f1b46c84ef8a3297d118b3</citedby><cites>FETCH-LOGICAL-c363t-c1bcf935be223395260ed6bf733d4362ab101a58888f1b46c84ef8a3297d118b3</cites><orcidid>0000-0002-7035-5187</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://link.springer.com/content/pdf/10.1007/s13399-020-01178-y$$EPDF$$P50$$Gspringer$$Hfree_for_read</linktopdf><linktohtml>$$Uhttps://link.springer.com/10.1007/s13399-020-01178-y$$EHTML$$P50$$Gspringer$$Hfree_for_read</linktohtml><link.rule.ids>314,780,784,27924,27925,41488,42557,51319</link.rule.ids></links><search><creatorcontrib>Menin, Lorenzo</creatorcontrib><creatorcontrib>Benedetti, Vittoria</creatorcontrib><creatorcontrib>Patuzzi, Francesco</creatorcontrib><creatorcontrib>Baratieri, Marco</creatorcontrib><title>Techno-economic modeling of an integrated biomethane-biomethanol production process via biomass gasification, electrolysis, biomethanation, and catalytic methanol synthesis</title><title>Biomass conversion and biorefinery</title><addtitle>Biomass Conv. Bioref</addtitle><description>Biological methanation (biomethanation) of syngas obtained from biomass gasification offers the opportunity to employ a low-pressure, low-temperature process to produce storable bio-derived substitute natural gas (bSNG), although its economic viability is limited by high energy and biomass costs. Research on syngas biomethanation techno-economic performance is limited and novel biomass-to-biomethane process configurations are required in order to assess opportunities for the enhancement of its efficiency and economic feasibility. In this study, we carried out the techno-economic modeling of two processes comprising integrated biomass gasification, electrolysis, and syngas biomethanation with combined heat and power recovery in order to assess and compare their fuel yields, energy efficiency, carbon efficiency, and bSNG minimum selling price (MSP). The first process operates standalone biomethanation (SAB) of syngas and can produce approximately 38,000 Nm
3
of bSNG per day, with a total plant efficiency of 50.6%. The second process (integrated biomethane-biomethanol, IBB) exploits the unconverted carbon stream from the biomethanation process to recover energy and synthesize methanol via direct catalytic CO
2
hydrogenation. In addition to the same bSNG output, the IBB process can produce 10 t/day of biomethanol, at a 99% purity. The IBB process shows little global energy efficiency gains in comparison with SAB (51.7%) due to the large increase in electrolytic hydrogen demand, but it shows a substantial improvement in biomass-to-fuel carbon efficiency (33 vs. 26%). The SAB and IBB processes generate a bSNG MSP of 2.38 €/Nm
3
and 3.68 €/Nm
3
, respectively. Hydrogenation of unconverted carbon in biomass-to-biomethane processes comes with high additional capital and operating costs due to the large-scale electrolysis plants required. Consequently, in both processes, the market price gap of the bSNG produced is 0.13 €/kWh
bSNG
(SAB) and 0.25 €/kWh
bSNG
(IBB) even under the most optimistic cost scenarios considered, and it is primarily influenced by the cost of surplus electricity utilized in electrolysis, while the selling price of biomethanol exerts a very limited influence on process economics. Intensive subsidization would be required in order to sustain the decentralized production of bSNG through both processes. Despite their limited economic competitiveness, both processes have a size comparable with existing renewable gas production plants in terms of bSNG production capacity and the IBB process is of a size adequate for the supply of biomethanol to a decentralized biorenewable supply chain.</description><subject>Biogas</subject><subject>Biomass</subject><subject>Biomass energy production</subject><subject>Biotechnology</subject><subject>Carbon</subject><subject>Cogeneration</subject><subject>Economic models</subject><subject>Electrolysis</subject><subject>Energy</subject><subject>Energy costs</subject><subject>Energy efficiency</subject><subject>Feasibility studies</subject><subject>Fuels</subject><subject>Gasification</subject><subject>Heat recovery</subject><subject>Hydrogenation</subject><subject>Low pressure</subject><subject>Low temperature</subject><subject>Methanation</subject><subject>Methanol</subject><subject>Modelling</subject><subject>Operating costs</subject><subject>Original Article</subject><subject>Renewable and Green Energy</subject><subject>Substitute natural gas</subject><subject>Supply chains</subject><subject>Synthesis gas</subject><issn>2190-6815</issn><issn>2190-6823</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2023</creationdate><recordtype>article</recordtype><sourceid>C6C</sourceid><recordid>eNp9kctOAyEYhSdGE5vaF3BF4rYol85taRpvSRM3dU0Y5p8pzRQqUJN5Jx9SplPrTjachO-cHzhJckvJPSUkf_CU87LEhBFMKM0L3F8kE0ZLgrOC8cuzpul1MvN-SwhhPOcFJ5Pkew1qYywGZY3daYV2toZOmxbZBkmDtAnQOhmgRpW2OwgbaQCfpe3Q3tn6oIK2ZpAKvEdfWh5pGXUrvW60kgMwR9CBCs52vdd-_pd4OpWmRpGUXR-Gm_xO8L0JG4iOm-SqkZ2H2WmfJh_PT-vlK169v7wtH1dY8YwHrGilmpKnFTAWfyZlGYE6q5qc83rBMyYrSqhMi7gaWi0yVSygKSRnZV5TWlR8mtyNufFBnwfwQWztwZk4UrA8S0kZc4tIsZFSznrvoBF7p3fS9YISMRQjxmJELEYcixF9NPHR5CNsWnB_0f-4fgDXaJY9</recordid><startdate>20230101</startdate><enddate>20230101</enddate><creator>Menin, Lorenzo</creator><creator>Benedetti, Vittoria</creator><creator>Patuzzi, Francesco</creator><creator>Baratieri, Marco</creator><general>Springer Berlin Heidelberg</general><general>Springer Nature B.V</general><scope>C6C</scope><scope>AAYXX</scope><scope>CITATION</scope><orcidid>https://orcid.org/0000-0002-7035-5187</orcidid></search><sort><creationdate>20230101</creationdate><title>Techno-economic modeling of an integrated biomethane-biomethanol production process via biomass gasification, electrolysis, biomethanation, and catalytic methanol synthesis</title><author>Menin, Lorenzo ; Benedetti, Vittoria ; Patuzzi, Francesco ; Baratieri, Marco</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c363t-c1bcf935be223395260ed6bf733d4362ab101a58888f1b46c84ef8a3297d118b3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2023</creationdate><topic>Biogas</topic><topic>Biomass</topic><topic>Biomass energy production</topic><topic>Biotechnology</topic><topic>Carbon</topic><topic>Cogeneration</topic><topic>Economic models</topic><topic>Electrolysis</topic><topic>Energy</topic><topic>Energy costs</topic><topic>Energy efficiency</topic><topic>Feasibility studies</topic><topic>Fuels</topic><topic>Gasification</topic><topic>Heat recovery</topic><topic>Hydrogenation</topic><topic>Low pressure</topic><topic>Low temperature</topic><topic>Methanation</topic><topic>Methanol</topic><topic>Modelling</topic><topic>Operating costs</topic><topic>Original Article</topic><topic>Renewable and Green Energy</topic><topic>Substitute natural gas</topic><topic>Supply chains</topic><topic>Synthesis gas</topic><toplevel>online_resources</toplevel><creatorcontrib>Menin, Lorenzo</creatorcontrib><creatorcontrib>Benedetti, Vittoria</creatorcontrib><creatorcontrib>Patuzzi, Francesco</creatorcontrib><creatorcontrib>Baratieri, Marco</creatorcontrib><collection>Springer Nature OA Free Journals</collection><collection>CrossRef</collection><jtitle>Biomass conversion and biorefinery</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Menin, Lorenzo</au><au>Benedetti, Vittoria</au><au>Patuzzi, Francesco</au><au>Baratieri, Marco</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Techno-economic modeling of an integrated biomethane-biomethanol production process via biomass gasification, electrolysis, biomethanation, and catalytic methanol synthesis</atitle><jtitle>Biomass conversion and biorefinery</jtitle><stitle>Biomass Conv. Bioref</stitle><date>2023-01-01</date><risdate>2023</risdate><volume>13</volume><issue>2</issue><spage>977</spage><epage>998</epage><pages>977-998</pages><issn>2190-6815</issn><eissn>2190-6823</eissn><abstract>Biological methanation (biomethanation) of syngas obtained from biomass gasification offers the opportunity to employ a low-pressure, low-temperature process to produce storable bio-derived substitute natural gas (bSNG), although its economic viability is limited by high energy and biomass costs. Research on syngas biomethanation techno-economic performance is limited and novel biomass-to-biomethane process configurations are required in order to assess opportunities for the enhancement of its efficiency and economic feasibility. In this study, we carried out the techno-economic modeling of two processes comprising integrated biomass gasification, electrolysis, and syngas biomethanation with combined heat and power recovery in order to assess and compare their fuel yields, energy efficiency, carbon efficiency, and bSNG minimum selling price (MSP). The first process operates standalone biomethanation (SAB) of syngas and can produce approximately 38,000 Nm
3
of bSNG per day, with a total plant efficiency of 50.6%. The second process (integrated biomethane-biomethanol, IBB) exploits the unconverted carbon stream from the biomethanation process to recover energy and synthesize methanol via direct catalytic CO
2
hydrogenation. In addition to the same bSNG output, the IBB process can produce 10 t/day of biomethanol, at a 99% purity. The IBB process shows little global energy efficiency gains in comparison with SAB (51.7%) due to the large increase in electrolytic hydrogen demand, but it shows a substantial improvement in biomass-to-fuel carbon efficiency (33 vs. 26%). The SAB and IBB processes generate a bSNG MSP of 2.38 €/Nm
3
and 3.68 €/Nm
3
, respectively. Hydrogenation of unconverted carbon in biomass-to-biomethane processes comes with high additional capital and operating costs due to the large-scale electrolysis plants required. Consequently, in both processes, the market price gap of the bSNG produced is 0.13 €/kWh
bSNG
(SAB) and 0.25 €/kWh
bSNG
(IBB) even under the most optimistic cost scenarios considered, and it is primarily influenced by the cost of surplus electricity utilized in electrolysis, while the selling price of biomethanol exerts a very limited influence on process economics. Intensive subsidization would be required in order to sustain the decentralized production of bSNG through both processes. Despite their limited economic competitiveness, both processes have a size comparable with existing renewable gas production plants in terms of bSNG production capacity and the IBB process is of a size adequate for the supply of biomethanol to a decentralized biorenewable supply chain.</abstract><cop>Berlin/Heidelberg</cop><pub>Springer Berlin Heidelberg</pub><doi>10.1007/s13399-020-01178-y</doi><tpages>22</tpages><orcidid>https://orcid.org/0000-0002-7035-5187</orcidid><oa>free_for_read</oa></addata></record> |
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subjects | Biogas Biomass Biomass energy production Biotechnology Carbon Cogeneration Economic models Electrolysis Energy Energy costs Energy efficiency Feasibility studies Fuels Gasification Heat recovery Hydrogenation Low pressure Low temperature Methanation Methanol Modelling Operating costs Original Article Renewable and Green Energy Substitute natural gas Supply chains Synthesis gas |
title | Techno-economic modeling of an integrated biomethane-biomethanol production process via biomass gasification, electrolysis, biomethanation, and catalytic methanol synthesis |
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