Thermal plasma-aided chemical looping carbon dioxide dissociation for fuel production from aluminium particles
[Display omitted] •A novel thermal plasma chemical looping for syngas production was developed.•Integration of the process with solar energy was demonstrated.•Aluminium/aluminium oxide pair was chosen as an oxygen carrier in the process.•Syngas quality > 3 was achieved at temperature of 1273 K in...
Gespeichert in:
| Veröffentlicht in: | Energy conversion and management 2022-04, Vol.257, p.115413, Article 115413 |
|---|---|
| Hauptverfasser: | , , , , |
| Format: | Artikel |
| Sprache: | eng |
| Schlagworte: | |
| Online-Zugang: | Volltext |
| Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
| container_end_page | |
|---|---|
| container_issue | |
| container_start_page | 115413 |
| container_title | Energy conversion and management |
| container_volume | 257 |
| creator | Sarafraz, M.M. Christo, F.C. Tran, N.N. Fulcheri, L. Hessel, V. |
| description | [Display omitted]
•A novel thermal plasma chemical looping for syngas production was developed.•Integration of the process with solar energy was demonstrated.•Aluminium/aluminium oxide pair was chosen as an oxygen carrier in the process.•Syngas quality > 3 was achieved at temperature of 1273 K in the fuel reactor.•Photovoltaic renewable energy share of 39.9% was achieved for the process.
In the present article, a new thermal plasma-aided process is proposed and analysed that utilises alumina/aluminium particles to dissociate steam/carbon dioxide blends into high-quality synthetic fuel. The proposed system utilises two reactors namely a synthetic fuel reactor and a thermal plasma particle regenerator following the chemical looping gasification principle. In the former, the gas blend reacts with aluminium particles to produce hydrogen-enriched synthetic fuel and alumina. While in the latter, the alumina is dissociated into oxygen and reduced aluminium. Using thermochemical equilibrium analysis, it was identified that the proposed system can offer a self-sustaining factor of up to 0.18, thermodynamic and exergy efficiency of 0.38 and 0.68, respectively. The system was integrated with photovoltaic energy and a solar share of ≤ 0.5 (with low-capacity battery storage ≤ 4 MWh) and > 0.5 (with high-capacity battery storage |
| doi_str_mv | 10.1016/j.enconman.2022.115413 |
| format | Article |
| fullrecord | <record><control><sourceid>proquest_hal_p</sourceid><recordid>TN_cdi_hal_primary_oai_HAL_hal_03909328v1</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><els_id>S0196890422002096</els_id><sourcerecordid>2649104140</sourcerecordid><originalsourceid>FETCH-LOGICAL-c422t-4eff56ef8d0c2afd7b8b518d1b13d6f97095d80e63f5310539d2b13b655a64aa3</originalsourceid><addsrcrecordid>eNqFkU9r3DAQxUVIIZu0XyEYcurB25Fkaa1bl5BkCwu9bM9irD9dLba1lezQfvtqcZNrTwNvfu8xwyPknsKaApVfTms3mjgOOK4ZMLamVDSUX5EVbTeqZoxtrskKqJJ1q6C5Ibc5nwCAC5ArMh6OLg3YV-ce84A1ButsZY5uCKaofYznMP6sDKYujpUN8XcBysw5moBTKKKPqfKzKxEp2tksWopDhf08hDHMQ3XGNAXTu_yRfPDYZ_fp37wjP56fDo-7ev_95dvjdl-bhrGpbpz3QjrfWjAMvd10bSdoa2lHuZVebUAJ24KT3AtOQXBlWVl1UgiUDSK_I5-X3CP2-pzCgOmPjhj0brvXFw24AsVZ-0oL-7Cw5f5fs8uTPsU5jeU8zWSjKDS0gULJhTIp5pycf4-loC896JN-60FfetBLD8X4dTG68u9rcElnEwrpbEjOTNrG8L-Iv6sklbM</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>2649104140</pqid></control><display><type>article</type><title>Thermal plasma-aided chemical looping carbon dioxide dissociation for fuel production from aluminium particles</title><source>Access via ScienceDirect (Elsevier)</source><creator>Sarafraz, M.M. ; Christo, F.C. ; Tran, N.N. ; Fulcheri, L. ; Hessel, V.</creator><creatorcontrib>Sarafraz, M.M. ; Christo, F.C. ; Tran, N.N. ; Fulcheri, L. ; Hessel, V.</creatorcontrib><description>[Display omitted]
•A novel thermal plasma chemical looping for syngas production was developed.•Integration of the process with solar energy was demonstrated.•Aluminium/aluminium oxide pair was chosen as an oxygen carrier in the process.•Syngas quality > 3 was achieved at temperature of 1273 K in the fuel reactor.•Photovoltaic renewable energy share of 39.9% was achieved for the process.
In the present article, a new thermal plasma-aided process is proposed and analysed that utilises alumina/aluminium particles to dissociate steam/carbon dioxide blends into high-quality synthetic fuel. The proposed system utilises two reactors namely a synthetic fuel reactor and a thermal plasma particle regenerator following the chemical looping gasification principle. In the former, the gas blend reacts with aluminium particles to produce hydrogen-enriched synthetic fuel and alumina. While in the latter, the alumina is dissociated into oxygen and reduced aluminium. Using thermochemical equilibrium analysis, it was identified that the proposed system can offer a self-sustaining factor of up to 0.18, thermodynamic and exergy efficiency of 0.38 and 0.68, respectively. The system was integrated with photovoltaic energy and a solar share of ≤ 0.5 (with low-capacity battery storage ≤ 4 MWh) and > 0.5 (with high-capacity battery storage < 5 MWh) was obtained at photovoltaic capacity ∼ 3–5 MW. The thermodynamic conditions of 1273 K < T < 1573 under lean oxygen conditions and T > 6373 K were identified for the fuel and plasma reactors, respectively. The calculated syngas quality was > 2 for the selected thermodynamic conditions. The integration of the system with photovoltaic energy showed that the installed capacity of photovoltaic panels and battery storage are intertwined representing a trade-off trend. The optimum storage capacity of 4–6 MWh and photovoltaic installation capacity of 3–5 MWe was calculated for the localised production scale of 775 tonnes/year. The proposed system offers resiliency against the continuous operation in both centralised and decentralised arrangements. Based on this proof of concept, the viability of the thermal plasma-aided process for remote small-scale applications was discussed by benchmarking how it can meet the requirements well known for remote gas-to-liquid compact plants, producing gasoline out of syngas.</description><identifier>ISSN: 0196-8904</identifier><identifier>EISSN: 1879-2227</identifier><identifier>DOI: 10.1016/j.enconman.2022.115413</identifier><language>eng</language><publisher>Oxford: Elsevier Ltd</publisher><subject>Aluminum ; Aluminum oxide ; Carbon dioxide ; Energy storage ; Engineering Sciences ; Equilibrium analysis ; Exergy ; Fuel production ; Gasification ; Gasoline ; Hydrogen enrichment ; Mathematical analysis ; Nuclear fuels ; Oxygen ; Photovoltaics ; Plasma ; Reactors ; Reduction ; Renewable energy ; Solar energy ; Steam ; Storage capacity ; Synthesis gas ; Synthetic fuels ; Thermal plasma ; Thermal plasmas ; Thermodynamics</subject><ispartof>Energy conversion and management, 2022-04, Vol.257, p.115413, Article 115413</ispartof><rights>2022 Elsevier Ltd</rights><rights>Copyright Elsevier Science Ltd. Apr 1, 2022</rights><rights>Distributed under a Creative Commons Attribution 4.0 International License</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c422t-4eff56ef8d0c2afd7b8b518d1b13d6f97095d80e63f5310539d2b13b655a64aa3</citedby><cites>FETCH-LOGICAL-c422t-4eff56ef8d0c2afd7b8b518d1b13d6f97095d80e63f5310539d2b13b655a64aa3</cites><orcidid>0000-0002-3843-431X</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.enconman.2022.115413$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>230,314,780,784,885,3550,27924,27925,45995</link.rule.ids><backlink>$$Uhttps://hal.science/hal-03909328$$DView record in HAL$$Hfree_for_read</backlink></links><search><creatorcontrib>Sarafraz, M.M.</creatorcontrib><creatorcontrib>Christo, F.C.</creatorcontrib><creatorcontrib>Tran, N.N.</creatorcontrib><creatorcontrib>Fulcheri, L.</creatorcontrib><creatorcontrib>Hessel, V.</creatorcontrib><title>Thermal plasma-aided chemical looping carbon dioxide dissociation for fuel production from aluminium particles</title><title>Energy conversion and management</title><description>[Display omitted]
•A novel thermal plasma chemical looping for syngas production was developed.•Integration of the process with solar energy was demonstrated.•Aluminium/aluminium oxide pair was chosen as an oxygen carrier in the process.•Syngas quality > 3 was achieved at temperature of 1273 K in the fuel reactor.•Photovoltaic renewable energy share of 39.9% was achieved for the process.
In the present article, a new thermal plasma-aided process is proposed and analysed that utilises alumina/aluminium particles to dissociate steam/carbon dioxide blends into high-quality synthetic fuel. The proposed system utilises two reactors namely a synthetic fuel reactor and a thermal plasma particle regenerator following the chemical looping gasification principle. In the former, the gas blend reacts with aluminium particles to produce hydrogen-enriched synthetic fuel and alumina. While in the latter, the alumina is dissociated into oxygen and reduced aluminium. Using thermochemical equilibrium analysis, it was identified that the proposed system can offer a self-sustaining factor of up to 0.18, thermodynamic and exergy efficiency of 0.38 and 0.68, respectively. The system was integrated with photovoltaic energy and a solar share of ≤ 0.5 (with low-capacity battery storage ≤ 4 MWh) and > 0.5 (with high-capacity battery storage < 5 MWh) was obtained at photovoltaic capacity ∼ 3–5 MW. The thermodynamic conditions of 1273 K < T < 1573 under lean oxygen conditions and T > 6373 K were identified for the fuel and plasma reactors, respectively. The calculated syngas quality was > 2 for the selected thermodynamic conditions. The integration of the system with photovoltaic energy showed that the installed capacity of photovoltaic panels and battery storage are intertwined representing a trade-off trend. The optimum storage capacity of 4–6 MWh and photovoltaic installation capacity of 3–5 MWe was calculated for the localised production scale of 775 tonnes/year. The proposed system offers resiliency against the continuous operation in both centralised and decentralised arrangements. Based on this proof of concept, the viability of the thermal plasma-aided process for remote small-scale applications was discussed by benchmarking how it can meet the requirements well known for remote gas-to-liquid compact plants, producing gasoline out of syngas.</description><subject>Aluminum</subject><subject>Aluminum oxide</subject><subject>Carbon dioxide</subject><subject>Energy storage</subject><subject>Engineering Sciences</subject><subject>Equilibrium analysis</subject><subject>Exergy</subject><subject>Fuel production</subject><subject>Gasification</subject><subject>Gasoline</subject><subject>Hydrogen enrichment</subject><subject>Mathematical analysis</subject><subject>Nuclear fuels</subject><subject>Oxygen</subject><subject>Photovoltaics</subject><subject>Plasma</subject><subject>Reactors</subject><subject>Reduction</subject><subject>Renewable energy</subject><subject>Solar energy</subject><subject>Steam</subject><subject>Storage capacity</subject><subject>Synthesis gas</subject><subject>Synthetic fuels</subject><subject>Thermal plasma</subject><subject>Thermal plasmas</subject><subject>Thermodynamics</subject><issn>0196-8904</issn><issn>1879-2227</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2022</creationdate><recordtype>article</recordtype><recordid>eNqFkU9r3DAQxUVIIZu0XyEYcurB25Fkaa1bl5BkCwu9bM9irD9dLba1lezQfvtqcZNrTwNvfu8xwyPknsKaApVfTms3mjgOOK4ZMLamVDSUX5EVbTeqZoxtrskKqJJ1q6C5Ibc5nwCAC5ArMh6OLg3YV-ce84A1ButsZY5uCKaofYznMP6sDKYujpUN8XcBysw5moBTKKKPqfKzKxEp2tksWopDhf08hDHMQ3XGNAXTu_yRfPDYZ_fp37wjP56fDo-7ev_95dvjdl-bhrGpbpz3QjrfWjAMvd10bSdoa2lHuZVebUAJ24KT3AtOQXBlWVl1UgiUDSK_I5-X3CP2-pzCgOmPjhj0brvXFw24AsVZ-0oL-7Cw5f5fs8uTPsU5jeU8zWSjKDS0gULJhTIp5pycf4-loC896JN-60FfetBLD8X4dTG68u9rcElnEwrpbEjOTNrG8L-Iv6sklbM</recordid><startdate>20220401</startdate><enddate>20220401</enddate><creator>Sarafraz, M.M.</creator><creator>Christo, F.C.</creator><creator>Tran, N.N.</creator><creator>Fulcheri, L.</creator><creator>Hessel, V.</creator><general>Elsevier Ltd</general><general>Elsevier Science Ltd</general><general>Elsevier</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7ST</scope><scope>7TB</scope><scope>8FD</scope><scope>C1K</scope><scope>FR3</scope><scope>H8D</scope><scope>KR7</scope><scope>L7M</scope><scope>SOI</scope><scope>1XC</scope><orcidid>https://orcid.org/0000-0002-3843-431X</orcidid></search><sort><creationdate>20220401</creationdate><title>Thermal plasma-aided chemical looping carbon dioxide dissociation for fuel production from aluminium particles</title><author>Sarafraz, M.M. ; Christo, F.C. ; Tran, N.N. ; Fulcheri, L. ; Hessel, V.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c422t-4eff56ef8d0c2afd7b8b518d1b13d6f97095d80e63f5310539d2b13b655a64aa3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2022</creationdate><topic>Aluminum</topic><topic>Aluminum oxide</topic><topic>Carbon dioxide</topic><topic>Energy storage</topic><topic>Engineering Sciences</topic><topic>Equilibrium analysis</topic><topic>Exergy</topic><topic>Fuel production</topic><topic>Gasification</topic><topic>Gasoline</topic><topic>Hydrogen enrichment</topic><topic>Mathematical analysis</topic><topic>Nuclear fuels</topic><topic>Oxygen</topic><topic>Photovoltaics</topic><topic>Plasma</topic><topic>Reactors</topic><topic>Reduction</topic><topic>Renewable energy</topic><topic>Solar energy</topic><topic>Steam</topic><topic>Storage capacity</topic><topic>Synthesis gas</topic><topic>Synthetic fuels</topic><topic>Thermal plasma</topic><topic>Thermal plasmas</topic><topic>Thermodynamics</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Sarafraz, M.M.</creatorcontrib><creatorcontrib>Christo, F.C.</creatorcontrib><creatorcontrib>Tran, N.N.</creatorcontrib><creatorcontrib>Fulcheri, L.</creatorcontrib><creatorcontrib>Hessel, V.</creatorcontrib><collection>CrossRef</collection><collection>Environment Abstracts</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Engineering Research Database</collection><collection>Aerospace Database</collection><collection>Civil Engineering Abstracts</collection><collection>Advanced Technologies Database with Aerospace</collection><collection>Environment Abstracts</collection><collection>Hyper Article en Ligne (HAL)</collection><jtitle>Energy conversion and management</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Sarafraz, M.M.</au><au>Christo, F.C.</au><au>Tran, N.N.</au><au>Fulcheri, L.</au><au>Hessel, V.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Thermal plasma-aided chemical looping carbon dioxide dissociation for fuel production from aluminium particles</atitle><jtitle>Energy conversion and management</jtitle><date>2022-04-01</date><risdate>2022</risdate><volume>257</volume><spage>115413</spage><pages>115413-</pages><artnum>115413</artnum><issn>0196-8904</issn><eissn>1879-2227</eissn><abstract>[Display omitted]
•A novel thermal plasma chemical looping for syngas production was developed.•Integration of the process with solar energy was demonstrated.•Aluminium/aluminium oxide pair was chosen as an oxygen carrier in the process.•Syngas quality > 3 was achieved at temperature of 1273 K in the fuel reactor.•Photovoltaic renewable energy share of 39.9% was achieved for the process.
In the present article, a new thermal plasma-aided process is proposed and analysed that utilises alumina/aluminium particles to dissociate steam/carbon dioxide blends into high-quality synthetic fuel. The proposed system utilises two reactors namely a synthetic fuel reactor and a thermal plasma particle regenerator following the chemical looping gasification principle. In the former, the gas blend reacts with aluminium particles to produce hydrogen-enriched synthetic fuel and alumina. While in the latter, the alumina is dissociated into oxygen and reduced aluminium. Using thermochemical equilibrium analysis, it was identified that the proposed system can offer a self-sustaining factor of up to 0.18, thermodynamic and exergy efficiency of 0.38 and 0.68, respectively. The system was integrated with photovoltaic energy and a solar share of ≤ 0.5 (with low-capacity battery storage ≤ 4 MWh) and > 0.5 (with high-capacity battery storage < 5 MWh) was obtained at photovoltaic capacity ∼ 3–5 MW. The thermodynamic conditions of 1273 K < T < 1573 under lean oxygen conditions and T > 6373 K were identified for the fuel and plasma reactors, respectively. The calculated syngas quality was > 2 for the selected thermodynamic conditions. The integration of the system with photovoltaic energy showed that the installed capacity of photovoltaic panels and battery storage are intertwined representing a trade-off trend. The optimum storage capacity of 4–6 MWh and photovoltaic installation capacity of 3–5 MWe was calculated for the localised production scale of 775 tonnes/year. The proposed system offers resiliency against the continuous operation in both centralised and decentralised arrangements. Based on this proof of concept, the viability of the thermal plasma-aided process for remote small-scale applications was discussed by benchmarking how it can meet the requirements well known for remote gas-to-liquid compact plants, producing gasoline out of syngas.</abstract><cop>Oxford</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.enconman.2022.115413</doi><orcidid>https://orcid.org/0000-0002-3843-431X</orcidid><oa>free_for_read</oa></addata></record> |
| fulltext | fulltext |
| identifier | ISSN: 0196-8904 |
| ispartof | Energy conversion and management, 2022-04, Vol.257, p.115413, Article 115413 |
| issn | 0196-8904 1879-2227 |
| language | eng |
| recordid | cdi_hal_primary_oai_HAL_hal_03909328v1 |
| source | Access via ScienceDirect (Elsevier) |
| subjects | Aluminum Aluminum oxide Carbon dioxide Energy storage Engineering Sciences Equilibrium analysis Exergy Fuel production Gasification Gasoline Hydrogen enrichment Mathematical analysis Nuclear fuels Oxygen Photovoltaics Plasma Reactors Reduction Renewable energy Solar energy Steam Storage capacity Synthesis gas Synthetic fuels Thermal plasma Thermal plasmas Thermodynamics |
| title | Thermal plasma-aided chemical looping carbon dioxide dissociation for fuel production from aluminium particles |
| url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2024-12-22T13%3A18%3A21IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-proquest_hal_p&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Thermal%20plasma-aided%20chemical%20looping%20carbon%20dioxide%20dissociation%20for%20fuel%20production%20from%20aluminium%20particles&rft.jtitle=Energy%20conversion%20and%20management&rft.au=Sarafraz,%20M.M.&rft.date=2022-04-01&rft.volume=257&rft.spage=115413&rft.pages=115413-&rft.artnum=115413&rft.issn=0196-8904&rft.eissn=1879-2227&rft_id=info:doi/10.1016/j.enconman.2022.115413&rft_dat=%3Cproquest_hal_p%3E2649104140%3C/proquest_hal_p%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_pqid=2649104140&rft_id=info:pmid/&rft_els_id=S0196890422002096&rfr_iscdi=true |