Pyrolysis Products Formation Characteristics and Kinetics of Heavy Oil Base Cracked Oil
In this study, the pyrolysis products formation and kinetics of base cracked oil were studied by a TG-FTIR device, which can provide a reference basis for heavy oil and gas reaction and industrial application. The results exhibited that the saturated fraction was mainly composed of chain alkanes and...
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Veröffentlicht in: | Journal of the Chemical Society of Pakistan 2024-12, Vol.46 (6), p.508-508 |
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container_title | Journal of the Chemical Society of Pakistan |
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creator | Ruiyuan Tang, Ruiyuan Tang Yuru Gao, Yuru Gao Yani Li, Yani Li Lixia He, Lixia He Peixuan Sun, Peixuan Sun Zhibing Shen and Juntao Zhang, Zhibing Shen and Juntao Zhang |
description | In this study, the pyrolysis products formation and kinetics of base cracked oil were studied by a TG-FTIR device, which can provide a reference basis for heavy oil and gas reaction and industrial application. The results exhibited that the saturated fraction was mainly composed of chain alkanes and cycloalkanes. The aromatic fraction mainly contains polycyclic aromatic hydrocarbons and alkyl substituted aromatic hydrocarbons. The resin fraction is mainly multi-cyclic aromatic hydrocarbons. As the fraction becomes heavier, the initial and termination cracking temperature of saturate, aromatic, the amount of carbon residue gradually increases and coking intensifies. The pyrolysis products of chemical group were mainly methane, ethylene, C2+ hydrocarbons, and light aromatics, and the main contributing components for the generation of low carbon olefins are the saturated and aromatic fractions. The correlation coefficients R2 of the linear equations and fitting results were close to 1, and thus proving that the selected model was reasonable. The saturate fraction had the lowest activation energy of 78.82 kJ∙mol-1, while the aromatic, resin, and asphaltene have activation energies of 103.46 kJ∙mol-1, 108.87 kJ∙mol-1, and 110.56 kJ∙mol-1, respectively. |
doi_str_mv | 10.52568/001616/JCSP/46.06.2024 |
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The results exhibited that the saturated fraction was mainly composed of chain alkanes and cycloalkanes. The aromatic fraction mainly contains polycyclic aromatic hydrocarbons and alkyl substituted aromatic hydrocarbons. The resin fraction is mainly multi-cyclic aromatic hydrocarbons. As the fraction becomes heavier, the initial and termination cracking temperature of saturate, aromatic, the amount of carbon residue gradually increases and coking intensifies. The pyrolysis products of chemical group were mainly methane, ethylene, C2+ hydrocarbons, and light aromatics, and the main contributing components for the generation of low carbon olefins are the saturated and aromatic fractions. The correlation coefficients R2 of the linear equations and fitting results were close to 1, and thus proving that the selected model was reasonable. The saturate fraction had the lowest activation energy of 78.82 kJ∙mol-1, while the aromatic, resin, and asphaltene have activation energies of 103.46 kJ∙mol-1, 108.87 kJ∙mol-1, and 110.56 kJ∙mol-1, respectively.</description><identifier>ISSN: 0253-5106</identifier><identifier>DOI: 10.52568/001616/JCSP/46.06.2024</identifier><language>eng</language><publisher>Knowledge Bylanes</publisher><subject>Butadiene ; Oil sands ; Olefins ; Petroleum chemicals ; Petroleum mining ; Pyrolysis</subject><ispartof>Journal of the Chemical Society of Pakistan, 2024-12, Vol.46 (6), p.508-508</ispartof><rights>COPYRIGHT 2024 Knowledge Bylanes</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,776,780,27901,27902</link.rule.ids></links><search><creatorcontrib>Ruiyuan Tang, Ruiyuan Tang</creatorcontrib><creatorcontrib>Yuru Gao, Yuru Gao</creatorcontrib><creatorcontrib>Yani Li, Yani Li</creatorcontrib><creatorcontrib>Lixia He, Lixia He</creatorcontrib><creatorcontrib>Peixuan Sun, Peixuan Sun</creatorcontrib><creatorcontrib>Zhibing Shen and Juntao Zhang, Zhibing Shen and Juntao Zhang</creatorcontrib><title>Pyrolysis Products Formation Characteristics and Kinetics of Heavy Oil Base Cracked Oil</title><title>Journal of the Chemical Society of Pakistan</title><description>In this study, the pyrolysis products formation and kinetics of base cracked oil were studied by a TG-FTIR device, which can provide a reference basis for heavy oil and gas reaction and industrial application. The results exhibited that the saturated fraction was mainly composed of chain alkanes and cycloalkanes. The aromatic fraction mainly contains polycyclic aromatic hydrocarbons and alkyl substituted aromatic hydrocarbons. The resin fraction is mainly multi-cyclic aromatic hydrocarbons. As the fraction becomes heavier, the initial and termination cracking temperature of saturate, aromatic, the amount of carbon residue gradually increases and coking intensifies. The pyrolysis products of chemical group were mainly methane, ethylene, C2+ hydrocarbons, and light aromatics, and the main contributing components for the generation of low carbon olefins are the saturated and aromatic fractions. The correlation coefficients R2 of the linear equations and fitting results were close to 1, and thus proving that the selected model was reasonable. The saturate fraction had the lowest activation energy of 78.82 kJ∙mol-1, while the aromatic, resin, and asphaltene have activation energies of 103.46 kJ∙mol-1, 108.87 kJ∙mol-1, and 110.56 kJ∙mol-1, respectively.</description><subject>Butadiene</subject><subject>Oil sands</subject><subject>Olefins</subject><subject>Petroleum chemicals</subject><subject>Petroleum mining</subject><subject>Pyrolysis</subject><issn>0253-5106</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2024</creationdate><recordtype>article</recordtype><recordid>eNptkE1LAzEQhnNQsNT-BgOet5187vZYF-tXoQUVjyGbTTS6u5FkFfbfu229CM4chnl532F4ELogMBdUyGIBQCSRi_vycbfgcg5yToHyEzQBKlgmCMgzNEvpHcaSNGeSTdDLboihGZJPeBdD_WX6hNchtrr3ocPlm47a9Db61HuTsO5q_OA7e1iCw7dWfw946xt8pZPF5Wj-sPVeOEenTjfJzn7nFD2vr5_K22yzvbkrV5vMECJ4ZnIJS8FdblhhRFEUUNVQWWIMZ0tJHaWScwraGMkrAE1yzt3SkppRIuuKsCm6PN591Y1VvnOhH59ofTJqVVAiJOM5H13zf1xj17b1JnTW-VH_E8iPARNDStE69Rl9q-OgCKgDbXWkrfa0FZcKpNrTZj_F_XMJ</recordid><startdate>20241231</startdate><enddate>20241231</enddate><creator>Ruiyuan Tang, Ruiyuan Tang</creator><creator>Yuru Gao, Yuru Gao</creator><creator>Yani Li, Yani Li</creator><creator>Lixia He, Lixia He</creator><creator>Peixuan Sun, Peixuan Sun</creator><creator>Zhibing Shen and Juntao Zhang, Zhibing Shen and Juntao Zhang</creator><general>Knowledge Bylanes</general><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>20241231</creationdate><title>Pyrolysis Products Formation Characteristics and Kinetics of Heavy Oil Base Cracked Oil</title><author>Ruiyuan Tang, Ruiyuan Tang ; Yuru Gao, Yuru Gao ; Yani Li, Yani Li ; Lixia He, Lixia He ; Peixuan Sun, Peixuan Sun ; Zhibing Shen and Juntao Zhang, Zhibing Shen and Juntao Zhang</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c1154-c760954f7c38c58880bd0be1cc43962f2264420acc64b00a1744f9e1d3216db13</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2024</creationdate><topic>Butadiene</topic><topic>Oil sands</topic><topic>Olefins</topic><topic>Petroleum chemicals</topic><topic>Petroleum mining</topic><topic>Pyrolysis</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Ruiyuan Tang, Ruiyuan Tang</creatorcontrib><creatorcontrib>Yuru Gao, Yuru Gao</creatorcontrib><creatorcontrib>Yani Li, Yani Li</creatorcontrib><creatorcontrib>Lixia He, Lixia He</creatorcontrib><creatorcontrib>Peixuan Sun, Peixuan Sun</creatorcontrib><creatorcontrib>Zhibing Shen and Juntao Zhang, Zhibing Shen and Juntao Zhang</creatorcontrib><collection>CrossRef</collection><jtitle>Journal of the Chemical Society of Pakistan</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Ruiyuan Tang, Ruiyuan Tang</au><au>Yuru Gao, Yuru Gao</au><au>Yani Li, Yani Li</au><au>Lixia He, Lixia He</au><au>Peixuan Sun, Peixuan Sun</au><au>Zhibing Shen and Juntao Zhang, Zhibing Shen and Juntao Zhang</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Pyrolysis Products Formation Characteristics and Kinetics of Heavy Oil Base Cracked Oil</atitle><jtitle>Journal of the Chemical Society of Pakistan</jtitle><date>2024-12-31</date><risdate>2024</risdate><volume>46</volume><issue>6</issue><spage>508</spage><epage>508</epage><pages>508-508</pages><issn>0253-5106</issn><abstract>In this study, the pyrolysis products formation and kinetics of base cracked oil were studied by a TG-FTIR device, which can provide a reference basis for heavy oil and gas reaction and industrial application. The results exhibited that the saturated fraction was mainly composed of chain alkanes and cycloalkanes. The aromatic fraction mainly contains polycyclic aromatic hydrocarbons and alkyl substituted aromatic hydrocarbons. The resin fraction is mainly multi-cyclic aromatic hydrocarbons. As the fraction becomes heavier, the initial and termination cracking temperature of saturate, aromatic, the amount of carbon residue gradually increases and coking intensifies. The pyrolysis products of chemical group were mainly methane, ethylene, C2+ hydrocarbons, and light aromatics, and the main contributing components for the generation of low carbon olefins are the saturated and aromatic fractions. The correlation coefficients R2 of the linear equations and fitting results were close to 1, and thus proving that the selected model was reasonable. The saturate fraction had the lowest activation energy of 78.82 kJ∙mol-1, while the aromatic, resin, and asphaltene have activation energies of 103.46 kJ∙mol-1, 108.87 kJ∙mol-1, and 110.56 kJ∙mol-1, respectively.</abstract><pub>Knowledge Bylanes</pub><doi>10.52568/001616/JCSP/46.06.2024</doi><tpages>1</tpages></addata></record> |
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subjects | Butadiene Oil sands Olefins Petroleum chemicals Petroleum mining Pyrolysis |
title | Pyrolysis Products Formation Characteristics and Kinetics of Heavy Oil Base Cracked Oil |
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