Study on hydro-liquefaction kinetics of thermal dissolution soluble fraction from Shenfu sub-bituminous coal
•TDSF is almost completely liquefied at 380°C with high yield of oil+gas.•The model of hydro-liquefaction of TDSF includes series and parallel reactions.•The regressive reaction is ruled out in the model.•TDSF to PA and PA to oil+gas are the main reactions.•Oil+gas are mainly formed from the reactio...
Gespeichert in:
Veröffentlicht in: | Fuel (Guildford) 2017-07, Vol.200, p.576-582 |
---|---|
Hauptverfasser: | , , , , , , , , , |
Format: | Artikel |
Sprache: | eng |
Schlagworte: | |
Online-Zugang: | Volltext |
Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
container_end_page | 582 |
---|---|
container_issue | |
container_start_page | 576 |
container_title | Fuel (Guildford) |
container_volume | 200 |
creator | Shui, Hengfu Xu, Haiyan Zhou, Yan Shui, Tao Pan, Chunxiu Wang, Zhicai Lei, Zhiping Ren, Shibiao Kang, Shigang Xu, Chunbao (Charles) |
description | •TDSF is almost completely liquefied at 380°C with high yield of oil+gas.•The model of hydro-liquefaction of TDSF includes series and parallel reactions.•The regressive reaction is ruled out in the model.•TDSF to PA and PA to oil+gas are the main reactions.•Oil+gas are mainly formed from the reaction of PA to oil+gas.
Thermal dissolution (TD) of coal and hydro-liquefaction of the thermal dissolution soluble fraction (TDSF) with a high activity catalyst is one of effective high efficient hydro-liquefaction of coal techniques. In this study, a Chinese Shenfu (SF) sub-bituminous coal was thermally dissolved, and the TDSF obtained was further hydro-liquefied with Ni–Mo-S/Al2O3 catalyst. Based on the hydro-liquefaction results, a model including series and parallel reactions was established for the hydro-liquefaction of TDSF catalyzed by Ni–Mo-S/Al2O3, and the regressive reactions were ruled out in the model. From the kinetic parameters calculated, it suggested that the regressive reactions including the char formation reactions were negligible in the hydro-liquefaction of TDSF catalyzed by Ni–Mo-S/Al2O3. The reactions of TDSF to preasphaltene and preasphaltene to oil+gas predominated the formation of oil+gas. Ni–Mo-S/Al2O3 could decrease the activation energy of preasphaltene to oil+gas reaction, thus promoting the formation of oil and gas in the catalytic hydro-liquefaction of TDSF. |
doi_str_mv | 10.1016/j.fuel.2017.03.048 |
format | Article |
fullrecord | <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_journals_2006794241</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><els_id>S0016236117303241</els_id><sourcerecordid>2006794241</sourcerecordid><originalsourceid>FETCH-LOGICAL-c365t-82e96c36c31793ad44c04762a65d0d150256bb716cbbbf4fbac388b7e3c00b8c3</originalsourceid><addsrcrecordid>eNp9kE1LxDAQhoMouK7-AU8Bz62Tpk264EUWv2DBw-o5NGnCprbNmjTC_ntTd8-eZph53_l4ELolkBMg7L7LTdR9XgDhOdAcyvoMLUjNacZJRc_RApIqKygjl-gqhA4AeF2VC9Rvp9gesBvx7tB6l_X2O2rTqMmm0pcd9WRVwM7gaaf90PS4tSG4Pv7150T2Ght_MhjvBrzd6dFEHKLMpJ3iYEcXA1au6a_RhWn6oG9OcYk-n58-1q_Z5v3lbf24yRRl1ZTVhV6xlCpK-Io2bVkqKDkrGla10JIKiopJyQlTUkpTGtkoWteSa6oAZK3oEt0d5-69S--ESXQu-jGtFAUA46uyKElSFUeV8i4Er43Yezs0_iAIiJmq6MRMVcxUBVCRqCbTw9Gk0_0_VnsRlNWj0q31Wk2idfY_-y8KxILf</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>2006794241</pqid></control><display><type>article</type><title>Study on hydro-liquefaction kinetics of thermal dissolution soluble fraction from Shenfu sub-bituminous coal</title><source>Elsevier ScienceDirect Journals</source><creator>Shui, Hengfu ; Xu, Haiyan ; Zhou, Yan ; Shui, Tao ; Pan, Chunxiu ; Wang, Zhicai ; Lei, Zhiping ; Ren, Shibiao ; Kang, Shigang ; Xu, Chunbao (Charles)</creator><creatorcontrib>Shui, Hengfu ; Xu, Haiyan ; Zhou, Yan ; Shui, Tao ; Pan, Chunxiu ; Wang, Zhicai ; Lei, Zhiping ; Ren, Shibiao ; Kang, Shigang ; Xu, Chunbao (Charles)</creatorcontrib><description>•TDSF is almost completely liquefied at 380°C with high yield of oil+gas.•The model of hydro-liquefaction of TDSF includes series and parallel reactions.•The regressive reaction is ruled out in the model.•TDSF to PA and PA to oil+gas are the main reactions.•Oil+gas are mainly formed from the reaction of PA to oil+gas.
Thermal dissolution (TD) of coal and hydro-liquefaction of the thermal dissolution soluble fraction (TDSF) with a high activity catalyst is one of effective high efficient hydro-liquefaction of coal techniques. In this study, a Chinese Shenfu (SF) sub-bituminous coal was thermally dissolved, and the TDSF obtained was further hydro-liquefied with Ni–Mo-S/Al2O3 catalyst. Based on the hydro-liquefaction results, a model including series and parallel reactions was established for the hydro-liquefaction of TDSF catalyzed by Ni–Mo-S/Al2O3, and the regressive reactions were ruled out in the model. From the kinetic parameters calculated, it suggested that the regressive reactions including the char formation reactions were negligible in the hydro-liquefaction of TDSF catalyzed by Ni–Mo-S/Al2O3. The reactions of TDSF to preasphaltene and preasphaltene to oil+gas predominated the formation of oil+gas. Ni–Mo-S/Al2O3 could decrease the activation energy of preasphaltene to oil+gas reaction, thus promoting the formation of oil and gas in the catalytic hydro-liquefaction of TDSF.</description><identifier>ISSN: 0016-2361</identifier><identifier>EISSN: 1873-7153</identifier><identifier>DOI: 10.1016/j.fuel.2017.03.048</identifier><language>eng</language><publisher>Kidlington: Elsevier Ltd</publisher><subject>Aluminum oxide ; Bituminous coal ; Catalysis ; Catalyst ; Catalysts ; Char formation ; Chemical reactions ; Coal ; Dissolution ; Hydro-liquefaction kinetics ; Kinetics ; Liquefaction ; Molybdenum ; Natural gas ; Oil ; Reaction kinetics ; Thermal dissolution soluble fraction</subject><ispartof>Fuel (Guildford), 2017-07, Vol.200, p.576-582</ispartof><rights>2017 Elsevier Ltd</rights><rights>Copyright Elsevier BV Jul 15, 2017</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c365t-82e96c36c31793ad44c04762a65d0d150256bb716cbbbf4fbac388b7e3c00b8c3</citedby><cites>FETCH-LOGICAL-c365t-82e96c36c31793ad44c04762a65d0d150256bb716cbbbf4fbac388b7e3c00b8c3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/S0016236117303241$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,776,780,3537,27901,27902,65306</link.rule.ids></links><search><creatorcontrib>Shui, Hengfu</creatorcontrib><creatorcontrib>Xu, Haiyan</creatorcontrib><creatorcontrib>Zhou, Yan</creatorcontrib><creatorcontrib>Shui, Tao</creatorcontrib><creatorcontrib>Pan, Chunxiu</creatorcontrib><creatorcontrib>Wang, Zhicai</creatorcontrib><creatorcontrib>Lei, Zhiping</creatorcontrib><creatorcontrib>Ren, Shibiao</creatorcontrib><creatorcontrib>Kang, Shigang</creatorcontrib><creatorcontrib>Xu, Chunbao (Charles)</creatorcontrib><title>Study on hydro-liquefaction kinetics of thermal dissolution soluble fraction from Shenfu sub-bituminous coal</title><title>Fuel (Guildford)</title><description>•TDSF is almost completely liquefied at 380°C with high yield of oil+gas.•The model of hydro-liquefaction of TDSF includes series and parallel reactions.•The regressive reaction is ruled out in the model.•TDSF to PA and PA to oil+gas are the main reactions.•Oil+gas are mainly formed from the reaction of PA to oil+gas.
Thermal dissolution (TD) of coal and hydro-liquefaction of the thermal dissolution soluble fraction (TDSF) with a high activity catalyst is one of effective high efficient hydro-liquefaction of coal techniques. In this study, a Chinese Shenfu (SF) sub-bituminous coal was thermally dissolved, and the TDSF obtained was further hydro-liquefied with Ni–Mo-S/Al2O3 catalyst. Based on the hydro-liquefaction results, a model including series and parallel reactions was established for the hydro-liquefaction of TDSF catalyzed by Ni–Mo-S/Al2O3, and the regressive reactions were ruled out in the model. From the kinetic parameters calculated, it suggested that the regressive reactions including the char formation reactions were negligible in the hydro-liquefaction of TDSF catalyzed by Ni–Mo-S/Al2O3. The reactions of TDSF to preasphaltene and preasphaltene to oil+gas predominated the formation of oil+gas. Ni–Mo-S/Al2O3 could decrease the activation energy of preasphaltene to oil+gas reaction, thus promoting the formation of oil and gas in the catalytic hydro-liquefaction of TDSF.</description><subject>Aluminum oxide</subject><subject>Bituminous coal</subject><subject>Catalysis</subject><subject>Catalyst</subject><subject>Catalysts</subject><subject>Char formation</subject><subject>Chemical reactions</subject><subject>Coal</subject><subject>Dissolution</subject><subject>Hydro-liquefaction kinetics</subject><subject>Kinetics</subject><subject>Liquefaction</subject><subject>Molybdenum</subject><subject>Natural gas</subject><subject>Oil</subject><subject>Reaction kinetics</subject><subject>Thermal dissolution soluble fraction</subject><issn>0016-2361</issn><issn>1873-7153</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2017</creationdate><recordtype>article</recordtype><recordid>eNp9kE1LxDAQhoMouK7-AU8Bz62Tpk264EUWv2DBw-o5NGnCprbNmjTC_ntTd8-eZph53_l4ELolkBMg7L7LTdR9XgDhOdAcyvoMLUjNacZJRc_RApIqKygjl-gqhA4AeF2VC9Rvp9gesBvx7tB6l_X2O2rTqMmm0pcd9WRVwM7gaaf90PS4tSG4Pv7150T2Ght_MhjvBrzd6dFEHKLMpJ3iYEcXA1au6a_RhWn6oG9OcYk-n58-1q_Z5v3lbf24yRRl1ZTVhV6xlCpK-Io2bVkqKDkrGla10JIKiopJyQlTUkpTGtkoWteSa6oAZK3oEt0d5-69S--ESXQu-jGtFAUA46uyKElSFUeV8i4Er43Yezs0_iAIiJmq6MRMVcxUBVCRqCbTw9Gk0_0_VnsRlNWj0q31Wk2idfY_-y8KxILf</recordid><startdate>20170715</startdate><enddate>20170715</enddate><creator>Shui, Hengfu</creator><creator>Xu, Haiyan</creator><creator>Zhou, Yan</creator><creator>Shui, Tao</creator><creator>Pan, Chunxiu</creator><creator>Wang, Zhicai</creator><creator>Lei, Zhiping</creator><creator>Ren, Shibiao</creator><creator>Kang, Shigang</creator><creator>Xu, Chunbao (Charles)</creator><general>Elsevier Ltd</general><general>Elsevier BV</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7QF</scope><scope>7QO</scope><scope>7QQ</scope><scope>7SC</scope><scope>7SE</scope><scope>7SP</scope><scope>7SR</scope><scope>7T7</scope><scope>7TA</scope><scope>7TB</scope><scope>7U5</scope><scope>8BQ</scope><scope>8FD</scope><scope>C1K</scope><scope>F28</scope><scope>FR3</scope><scope>H8D</scope><scope>H8G</scope><scope>JG9</scope><scope>JQ2</scope><scope>KR7</scope><scope>L7M</scope><scope>L~C</scope><scope>L~D</scope><scope>P64</scope></search><sort><creationdate>20170715</creationdate><title>Study on hydro-liquefaction kinetics of thermal dissolution soluble fraction from Shenfu sub-bituminous coal</title><author>Shui, Hengfu ; Xu, Haiyan ; Zhou, Yan ; Shui, Tao ; Pan, Chunxiu ; Wang, Zhicai ; Lei, Zhiping ; Ren, Shibiao ; Kang, Shigang ; Xu, Chunbao (Charles)</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c365t-82e96c36c31793ad44c04762a65d0d150256bb716cbbbf4fbac388b7e3c00b8c3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2017</creationdate><topic>Aluminum oxide</topic><topic>Bituminous coal</topic><topic>Catalysis</topic><topic>Catalyst</topic><topic>Catalysts</topic><topic>Char formation</topic><topic>Chemical reactions</topic><topic>Coal</topic><topic>Dissolution</topic><topic>Hydro-liquefaction kinetics</topic><topic>Kinetics</topic><topic>Liquefaction</topic><topic>Molybdenum</topic><topic>Natural gas</topic><topic>Oil</topic><topic>Reaction kinetics</topic><topic>Thermal dissolution soluble fraction</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Shui, Hengfu</creatorcontrib><creatorcontrib>Xu, Haiyan</creatorcontrib><creatorcontrib>Zhou, Yan</creatorcontrib><creatorcontrib>Shui, Tao</creatorcontrib><creatorcontrib>Pan, Chunxiu</creatorcontrib><creatorcontrib>Wang, Zhicai</creatorcontrib><creatorcontrib>Lei, Zhiping</creatorcontrib><creatorcontrib>Ren, Shibiao</creatorcontrib><creatorcontrib>Kang, Shigang</creatorcontrib><creatorcontrib>Xu, Chunbao (Charles)</creatorcontrib><collection>CrossRef</collection><collection>Aluminium Industry Abstracts</collection><collection>Biotechnology Research Abstracts</collection><collection>Ceramic Abstracts</collection><collection>Computer and Information Systems Abstracts</collection><collection>Corrosion Abstracts</collection><collection>Electronics & Communications Abstracts</collection><collection>Engineered Materials Abstracts</collection><collection>Industrial and Applied Microbiology Abstracts (Microbiology A)</collection><collection>Materials Business File</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>ANTE: Abstracts in New Technology & Engineering</collection><collection>Engineering Research Database</collection><collection>Aerospace Database</collection><collection>Copper Technical Reference Library</collection><collection>Materials Research Database</collection><collection>ProQuest Computer Science Collection</collection><collection>Civil Engineering Abstracts</collection><collection>Advanced Technologies Database with Aerospace</collection><collection>Computer and Information Systems Abstracts Academic</collection><collection>Computer and Information Systems Abstracts Professional</collection><collection>Biotechnology and BioEngineering Abstracts</collection><jtitle>Fuel (Guildford)</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Shui, Hengfu</au><au>Xu, Haiyan</au><au>Zhou, Yan</au><au>Shui, Tao</au><au>Pan, Chunxiu</au><au>Wang, Zhicai</au><au>Lei, Zhiping</au><au>Ren, Shibiao</au><au>Kang, Shigang</au><au>Xu, Chunbao (Charles)</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Study on hydro-liquefaction kinetics of thermal dissolution soluble fraction from Shenfu sub-bituminous coal</atitle><jtitle>Fuel (Guildford)</jtitle><date>2017-07-15</date><risdate>2017</risdate><volume>200</volume><spage>576</spage><epage>582</epage><pages>576-582</pages><issn>0016-2361</issn><eissn>1873-7153</eissn><abstract>•TDSF is almost completely liquefied at 380°C with high yield of oil+gas.•The model of hydro-liquefaction of TDSF includes series and parallel reactions.•The regressive reaction is ruled out in the model.•TDSF to PA and PA to oil+gas are the main reactions.•Oil+gas are mainly formed from the reaction of PA to oil+gas.
Thermal dissolution (TD) of coal and hydro-liquefaction of the thermal dissolution soluble fraction (TDSF) with a high activity catalyst is one of effective high efficient hydro-liquefaction of coal techniques. In this study, a Chinese Shenfu (SF) sub-bituminous coal was thermally dissolved, and the TDSF obtained was further hydro-liquefied with Ni–Mo-S/Al2O3 catalyst. Based on the hydro-liquefaction results, a model including series and parallel reactions was established for the hydro-liquefaction of TDSF catalyzed by Ni–Mo-S/Al2O3, and the regressive reactions were ruled out in the model. From the kinetic parameters calculated, it suggested that the regressive reactions including the char formation reactions were negligible in the hydro-liquefaction of TDSF catalyzed by Ni–Mo-S/Al2O3. The reactions of TDSF to preasphaltene and preasphaltene to oil+gas predominated the formation of oil+gas. Ni–Mo-S/Al2O3 could decrease the activation energy of preasphaltene to oil+gas reaction, thus promoting the formation of oil and gas in the catalytic hydro-liquefaction of TDSF.</abstract><cop>Kidlington</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.fuel.2017.03.048</doi><tpages>7</tpages></addata></record> |
fulltext | fulltext |
identifier | ISSN: 0016-2361 |
ispartof | Fuel (Guildford), 2017-07, Vol.200, p.576-582 |
issn | 0016-2361 1873-7153 |
language | eng |
recordid | cdi_proquest_journals_2006794241 |
source | Elsevier ScienceDirect Journals |
subjects | Aluminum oxide Bituminous coal Catalysis Catalyst Catalysts Char formation Chemical reactions Coal Dissolution Hydro-liquefaction kinetics Kinetics Liquefaction Molybdenum Natural gas Oil Reaction kinetics Thermal dissolution soluble fraction |
title | Study on hydro-liquefaction kinetics of thermal dissolution soluble fraction from Shenfu sub-bituminous coal |
url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-02-01T08%3A41%3A17IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-proquest_cross&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Study%20on%20hydro-liquefaction%20kinetics%20of%20thermal%20dissolution%20soluble%20fraction%20from%20Shenfu%20sub-bituminous%20coal&rft.jtitle=Fuel%20(Guildford)&rft.au=Shui,%20Hengfu&rft.date=2017-07-15&rft.volume=200&rft.spage=576&rft.epage=582&rft.pages=576-582&rft.issn=0016-2361&rft.eissn=1873-7153&rft_id=info:doi/10.1016/j.fuel.2017.03.048&rft_dat=%3Cproquest_cross%3E2006794241%3C/proquest_cross%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_pqid=2006794241&rft_id=info:pmid/&rft_els_id=S0016236117303241&rfr_iscdi=true |