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EXPERIMENTAL VERIFICATION FOR PROCESS MODELING OF COKING HEATER INNER TUBE
The flow and reaction processes of vacuum residue were simulated in an electric heated tube for coking heater. The vacuum residue was pumped into the tube, and heated up to about 500°C to carry out thermal conversion. Gaseous products were measured by gas meter and analyzed by gas chromatography. Th...
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Published in: | Petroleum science and technology 2002-01, Vol.20 (5-6), p.613-620 |
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creator | Xiao, Jiazhi Wang, Lanjuan Chen, Qinglin Song, Antai |
description | The flow and reaction processes of vacuum residue were simulated in an electric heated tube for coking heater. The vacuum residue was pumped into the tube, and heated up to about 500°C to carry out thermal conversion. Gaseous products were measured by gas meter and analyzed by gas chromatography. The liquid products were first quenched and collected by a specially designed sampling tube, and then analyzed by liquid chromatography. Therefore, the conversion fraction of every narrow fraction was obtained experimentally. Both flow and reaction processes were simulated using a dynamic model, the simulated conversion at exit of the tube is near to the experimental data under three dynamic conditions. This indicates that the model for flow and reaction processes used in this paper is reasonable. |
doi_str_mv | 10.1081/LFT-120003584 |
format | article |
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The vacuum residue was pumped into the tube, and heated up to about 500°C to carry out thermal conversion. Gaseous products were measured by gas meter and analyzed by gas chromatography. The liquid products were first quenched and collected by a specially designed sampling tube, and then analyzed by liquid chromatography. Therefore, the conversion fraction of every narrow fraction was obtained experimentally. Both flow and reaction processes were simulated using a dynamic model, the simulated conversion at exit of the tube is near to the experimental data under three dynamic conditions. This indicates that the model for flow and reaction processes used in this paper is reasonable.</description><identifier>ISSN: 1091-6466</identifier><identifier>EISSN: 1532-2459</identifier><identifier>DOI: 10.1081/LFT-120003584</identifier><language>eng</language><publisher>Colchester: Taylor & Francis Group</publisher><subject>Applied sciences ; Coking ; Computer simulation ; Conversion ; Crude oil, natural gas and petroleum products ; Energy ; Exact sciences and technology ; Fuels ; Heaters ; Heaters (tube) ; Heating equipment ; Processing of crude oil and oils from shales and tar sands. Processes. Equipment. 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The vacuum residue was pumped into the tube, and heated up to about 500°C to carry out thermal conversion. Gaseous products were measured by gas meter and analyzed by gas chromatography. The liquid products were first quenched and collected by a specially designed sampling tube, and then analyzed by liquid chromatography. Therefore, the conversion fraction of every narrow fraction was obtained experimentally. Both flow and reaction processes were simulated using a dynamic model, the simulated conversion at exit of the tube is near to the experimental data under three dynamic conditions. This indicates that the model for flow and reaction processes used in this paper is reasonable.</description><subject>Applied sciences</subject><subject>Coking</subject><subject>Computer simulation</subject><subject>Conversion</subject><subject>Crude oil, natural gas and petroleum products</subject><subject>Energy</subject><subject>Exact sciences and technology</subject><subject>Fuels</subject><subject>Heaters</subject><subject>Heaters (tube)</subject><subject>Heating equipment</subject><subject>Processing of crude oil and oils from shales and tar sands. Processes. Equipment. 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Refinery and treatment units</topic><topic>Residues</topic><topic>Tubes</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Xiao, Jiazhi</creatorcontrib><creatorcontrib>Wang, Lanjuan</creatorcontrib><creatorcontrib>Chen, Qinglin</creatorcontrib><creatorcontrib>Song, Antai</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Oceanic Abstracts</collection><collection>ASFA: Aquatic Sciences and Fisheries Abstracts</collection><collection>Aquatic Science & Fisheries Abstracts (ASFA) 2: Ocean Technology, Policy & Non-Living Resources</collection><collection>Aquatic Science & Fisheries Abstracts (ASFA) Professional</collection><collection>Technology Research Database</collection><collection>Engineering Research Database</collection><collection>Civil Engineering Abstracts</collection><jtitle>Petroleum science and technology</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Xiao, Jiazhi</au><au>Wang, Lanjuan</au><au>Chen, Qinglin</au><au>Song, Antai</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>EXPERIMENTAL VERIFICATION FOR PROCESS MODELING OF COKING HEATER INNER TUBE</atitle><jtitle>Petroleum science and technology</jtitle><date>2002-01-01</date><risdate>2002</risdate><volume>20</volume><issue>5-6</issue><spage>613</spage><epage>620</epage><pages>613-620</pages><issn>1091-6466</issn><eissn>1532-2459</eissn><abstract>The flow and reaction processes of vacuum residue were simulated in an electric heated tube for coking heater. 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source | Taylor and Francis Science and Technology Collection |
subjects | Applied sciences Coking Computer simulation Conversion Crude oil, natural gas and petroleum products Energy Exact sciences and technology Fuels Heaters Heaters (tube) Heating equipment Processing of crude oil and oils from shales and tar sands. Processes. Equipment. Refinery and treatment units Residues Tubes |
title | EXPERIMENTAL VERIFICATION FOR PROCESS MODELING OF COKING HEATER INNER TUBE |
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