Experimental Study on Homogeneous Catalytic Upgrading of Heavy Oil

Four catalyst precursors were prepared to assess the performance on the upgrading process of heavy oil. It has been showed that viscosity of Lukeqin heavy oil was decreased significantly, which revealed a viscosity reduction ratio of up to 99.28% with a catalyst precursor concentration of 0.12 wt %,...

Ausführliche Beschreibung

Gespeichert in:
Bibliographische Detailangaben
Veröffentlicht in:Petroleum chemistry 2017-12, Vol.57 (12), p.1018-1023
Hauptverfasser: Tang, X. D., Chen, X. D., Li, J. J., Deng, L. Y., Liang, G. J.
Format: Artikel
Sprache:eng
Schlagworte:
Online-Zugang:Volltext
Tags: Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
container_end_page 1023
container_issue 12
container_start_page 1018
container_title Petroleum chemistry
container_volume 57
creator Tang, X. D.
Chen, X. D.
Li, J. J.
Deng, L. Y.
Liang, G. J.
description Four catalyst precursors were prepared to assess the performance on the upgrading process of heavy oil. It has been showed that viscosity of Lukeqin heavy oil was decreased significantly, which revealed a viscosity reduction ratio of up to 99.28% with a catalyst precursor concentration of 0.12 wt %, reaction temperature of 365°С and reaction time of 40 min. Analysis of the oil after upgrading showed an obviously change in the composition of hydrocarbon components. The increase of light fractions after reaction improved the properties of heavy oil which is benefit to the pipeline transportation and downstream refining. Meanwhile, the mechanism of upgrading was also investigated. This work proved that heavy oil can be effectively upgraded with the catalyst precursor of petroleum acid iron.
doi_str_mv 10.1134/S0965544117120143
format Article
fullrecord <record><control><sourceid>gale_proqu</sourceid><recordid>TN_cdi_proquest_journals_2002508292</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><galeid>A529948047</galeid><sourcerecordid>A529948047</sourcerecordid><originalsourceid>FETCH-LOGICAL-c392t-e5ce6311ba0af35e4aadf7e1b4e84334a57cbefb4a9c84234e8bbcfb72f846993</originalsourceid><addsrcrecordid>eNp1kE1Lw0AQhhdRsH78AG8LnlP3M8kea6lWKPRQew6bzWxISXfjJhXz790SwYPIHAbmfZ-Z4UXogZI5pVw87YhKpRSC0owyQgW_QDMqpUxSxtUlmp3l5Kxfo5u-PxASfYLP0PPqq4PQHMENusW74VSN2Du89kdfgwN_6vFSR2kcGoP3XR101bgae4vXoD9HvG3aO3RlddvD_U-_RfuX1ftynWy2r2_LxSYxXLEhAWkg5ZSWmmjLJQitK5sBLQXkgnOhZWZKsKXQyuSC8TguS2PLjNlcpErxW_Q47e2C_zhBPxQHfwouniwYIUySnCkWXfPJVesWisZZPwRtYlVwbIx3YJs4X0imlMiJyCJAJ8AE3_cBbNHFPHQYC0qKc7bFn2wjwyamj15XQ_h95X_oG-4Deo4</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>2002508292</pqid></control><display><type>article</type><title>Experimental Study on Homogeneous Catalytic Upgrading of Heavy Oil</title><source>Business Source Complete</source><source>SpringerLink Journals - AutoHoldings</source><creator>Tang, X. D. ; Chen, X. D. ; Li, J. J. ; Deng, L. Y. ; Liang, G. J.</creator><creatorcontrib>Tang, X. D. ; Chen, X. D. ; Li, J. J. ; Deng, L. Y. ; Liang, G. J.</creatorcontrib><description>Four catalyst precursors were prepared to assess the performance on the upgrading process of heavy oil. It has been showed that viscosity of Lukeqin heavy oil was decreased significantly, which revealed a viscosity reduction ratio of up to 99.28% with a catalyst precursor concentration of 0.12 wt %, reaction temperature of 365°С and reaction time of 40 min. Analysis of the oil after upgrading showed an obviously change in the composition of hydrocarbon components. The increase of light fractions after reaction improved the properties of heavy oil which is benefit to the pipeline transportation and downstream refining. Meanwhile, the mechanism of upgrading was also investigated. This work proved that heavy oil can be effectively upgraded with the catalyst precursor of petroleum acid iron.</description><identifier>ISSN: 0965-5441</identifier><identifier>EISSN: 1555-6239</identifier><identifier>DOI: 10.1134/S0965544117120143</identifier><language>eng</language><publisher>Moscow: Pleiades Publishing</publisher><subject>Catalysis ; Catalysts ; Chemistry ; Chemistry and Materials Science ; Energy (Physics) ; Industrial Chemistry/Chemical Engineering ; Reaction time ; Upgrading ; Viscosity</subject><ispartof>Petroleum chemistry, 2017-12, Vol.57 (12), p.1018-1023</ispartof><rights>Pleiades Publishing, Ltd. 2017</rights><rights>COPYRIGHT 2017 Springer</rights><rights>Copyright Springer Science &amp; Business Media 2017</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c392t-e5ce6311ba0af35e4aadf7e1b4e84334a57cbefb4a9c84234e8bbcfb72f846993</citedby><cites>FETCH-LOGICAL-c392t-e5ce6311ba0af35e4aadf7e1b4e84334a57cbefb4a9c84234e8bbcfb72f846993</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://link.springer.com/content/pdf/10.1134/S0965544117120143$$EPDF$$P50$$Gspringer$$H</linktopdf><linktohtml>$$Uhttps://link.springer.com/10.1134/S0965544117120143$$EHTML$$P50$$Gspringer$$H</linktohtml><link.rule.ids>314,780,784,27923,27924,41487,42556,51318</link.rule.ids></links><search><creatorcontrib>Tang, X. D.</creatorcontrib><creatorcontrib>Chen, X. D.</creatorcontrib><creatorcontrib>Li, J. J.</creatorcontrib><creatorcontrib>Deng, L. Y.</creatorcontrib><creatorcontrib>Liang, G. J.</creatorcontrib><title>Experimental Study on Homogeneous Catalytic Upgrading of Heavy Oil</title><title>Petroleum chemistry</title><addtitle>Pet. Chem</addtitle><description>Four catalyst precursors were prepared to assess the performance on the upgrading process of heavy oil. It has been showed that viscosity of Lukeqin heavy oil was decreased significantly, which revealed a viscosity reduction ratio of up to 99.28% with a catalyst precursor concentration of 0.12 wt %, reaction temperature of 365°С and reaction time of 40 min. Analysis of the oil after upgrading showed an obviously change in the composition of hydrocarbon components. The increase of light fractions after reaction improved the properties of heavy oil which is benefit to the pipeline transportation and downstream refining. Meanwhile, the mechanism of upgrading was also investigated. This work proved that heavy oil can be effectively upgraded with the catalyst precursor of petroleum acid iron.</description><subject>Catalysis</subject><subject>Catalysts</subject><subject>Chemistry</subject><subject>Chemistry and Materials Science</subject><subject>Energy (Physics)</subject><subject>Industrial Chemistry/Chemical Engineering</subject><subject>Reaction time</subject><subject>Upgrading</subject><subject>Viscosity</subject><issn>0965-5441</issn><issn>1555-6239</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2017</creationdate><recordtype>article</recordtype><recordid>eNp1kE1Lw0AQhhdRsH78AG8LnlP3M8kea6lWKPRQew6bzWxISXfjJhXz790SwYPIHAbmfZ-Z4UXogZI5pVw87YhKpRSC0owyQgW_QDMqpUxSxtUlmp3l5Kxfo5u-PxASfYLP0PPqq4PQHMENusW74VSN2Du89kdfgwN_6vFSR2kcGoP3XR101bgae4vXoD9HvG3aO3RlddvD_U-_RfuX1ftynWy2r2_LxSYxXLEhAWkg5ZSWmmjLJQitK5sBLQXkgnOhZWZKsKXQyuSC8TguS2PLjNlcpErxW_Q47e2C_zhBPxQHfwouniwYIUySnCkWXfPJVesWisZZPwRtYlVwbIx3YJs4X0imlMiJyCJAJ8AE3_cBbNHFPHQYC0qKc7bFn2wjwyamj15XQ_h95X_oG-4Deo4</recordid><startdate>20171201</startdate><enddate>20171201</enddate><creator>Tang, X. D.</creator><creator>Chen, X. D.</creator><creator>Li, J. J.</creator><creator>Deng, L. Y.</creator><creator>Liang, G. J.</creator><general>Pleiades Publishing</general><general>Springer</general><general>Springer Nature B.V</general><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>20171201</creationdate><title>Experimental Study on Homogeneous Catalytic Upgrading of Heavy Oil</title><author>Tang, X. D. ; Chen, X. D. ; Li, J. J. ; Deng, L. Y. ; Liang, G. J.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c392t-e5ce6311ba0af35e4aadf7e1b4e84334a57cbefb4a9c84234e8bbcfb72f846993</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2017</creationdate><topic>Catalysis</topic><topic>Catalysts</topic><topic>Chemistry</topic><topic>Chemistry and Materials Science</topic><topic>Energy (Physics)</topic><topic>Industrial Chemistry/Chemical Engineering</topic><topic>Reaction time</topic><topic>Upgrading</topic><topic>Viscosity</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Tang, X. D.</creatorcontrib><creatorcontrib>Chen, X. D.</creatorcontrib><creatorcontrib>Li, J. J.</creatorcontrib><creatorcontrib>Deng, L. Y.</creatorcontrib><creatorcontrib>Liang, G. J.</creatorcontrib><collection>CrossRef</collection><jtitle>Petroleum chemistry</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Tang, X. D.</au><au>Chen, X. D.</au><au>Li, J. J.</au><au>Deng, L. Y.</au><au>Liang, G. J.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Experimental Study on Homogeneous Catalytic Upgrading of Heavy Oil</atitle><jtitle>Petroleum chemistry</jtitle><stitle>Pet. Chem</stitle><date>2017-12-01</date><risdate>2017</risdate><volume>57</volume><issue>12</issue><spage>1018</spage><epage>1023</epage><pages>1018-1023</pages><issn>0965-5441</issn><eissn>1555-6239</eissn><abstract>Four catalyst precursors were prepared to assess the performance on the upgrading process of heavy oil. It has been showed that viscosity of Lukeqin heavy oil was decreased significantly, which revealed a viscosity reduction ratio of up to 99.28% with a catalyst precursor concentration of 0.12 wt %, reaction temperature of 365°С and reaction time of 40 min. Analysis of the oil after upgrading showed an obviously change in the composition of hydrocarbon components. The increase of light fractions after reaction improved the properties of heavy oil which is benefit to the pipeline transportation and downstream refining. Meanwhile, the mechanism of upgrading was also investigated. This work proved that heavy oil can be effectively upgraded with the catalyst precursor of petroleum acid iron.</abstract><cop>Moscow</cop><pub>Pleiades Publishing</pub><doi>10.1134/S0965544117120143</doi><tpages>6</tpages></addata></record>
fulltext fulltext
identifier ISSN: 0965-5441
ispartof Petroleum chemistry, 2017-12, Vol.57 (12), p.1018-1023
issn 0965-5441
1555-6239
language eng
recordid cdi_proquest_journals_2002508292
source Business Source Complete; SpringerLink Journals - AutoHoldings
subjects Catalysis
Catalysts
Chemistry
Chemistry and Materials Science
Energy (Physics)
Industrial Chemistry/Chemical Engineering
Reaction time
Upgrading
Viscosity
title Experimental Study on Homogeneous Catalytic Upgrading of Heavy Oil
url https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-12T03%3A52%3A44IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-gale_proqu&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Experimental%20Study%20on%20Homogeneous%20Catalytic%20Upgrading%20of%20Heavy%20Oil&rft.jtitle=Petroleum%20chemistry&rft.au=Tang,%20X.%20D.&rft.date=2017-12-01&rft.volume=57&rft.issue=12&rft.spage=1018&rft.epage=1023&rft.pages=1018-1023&rft.issn=0965-5441&rft.eissn=1555-6239&rft_id=info:doi/10.1134/S0965544117120143&rft_dat=%3Cgale_proqu%3EA529948047%3C/gale_proqu%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_pqid=2002508292&rft_id=info:pmid/&rft_galeid=A529948047&rfr_iscdi=true