Separation of solvent and deasphalted oil for solvent deasphalting process

Due to the depletion of conventional oil resources and increasing prices, various technologies for utilizing unconventional oil and low-value crude residues, which have not been fully exploited, are currently being explored. The exploitation of unconventional oil and low-value crude residues require...

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Published in:	Fuel processing technology Vol. 119; pp. 204 - 210
Main Authors:	Lee, Jung Moo, Shin, Sangcheol, Ahn, Seonju, Chun, Jeong Hwan, Lee, Ki Bong, Mun, Sungyong, Jeon, Sang Goo, Nho, Nam Sun
Format:	Journal Article
Language:	English
Published:	Amsterdam Elsevier 01-03-2014
Subjects:	Applied sciences Crude oil Crude oil, natural gas and petroleum products Energy Exact sciences and technology Fuels Hexanes Pentanes Processing of crude oil and oils from shales and tar sands. Processes. Equipment. Refinery and treatment units Recovery Residues Separation Solvents Upgrading Solvent deasphalting Organic solvent Deasphalting Separation Hydrocarbon Deasphalted oil Hexane Pentane Recovery
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Abstract	Due to the depletion of conventional oil resources and increasing prices, various technologies for utilizing unconventional oil and low-value crude residues, which have not been fully exploited, are currently being explored. The exploitation of unconventional oil and low-value crude residues requires upgrading processes such as carbon rejection and hydrogen addition. Among many existing upgrading processes, solvent deasphalting (SDA), a technology for removing asphaltene-rich pitch and producing higher-value deasphalted oil ( DAO) by using paraffinic solvents, is promising because it offers the advantages of low installation cost and flexibility in terms of the control of the quality of pitch and DAO. The SDA process requires a considerable amount of expensive solvent. Thus, solvent recovery, an energy-intensive process, is required for improved efficiency. In this paper, DAO/solvent separation experiments were carried out using two solvents, pentane and hexane, to investigate the effect of operating conditions such as temperature, pressure, and DAO/solvent ratio on the process. The DAO/pentane separation was superior to the DAO/hexane separation under similar conditions. Regardless of the solvent type, solvent recovery was increased as the DAO/solvent ratio in the feed was decreased. Solvent recovery was strongly influenced by variations in temperature but was relatively insensitive to changes in pressure.
AbstractList	Due to the depletion of conventional oil resources and increasing prices, various technologies for utilizing unconventional oil and low-value crude residues, which have not been fully exploited, are currently being explored. The exploitation of unconventional oil and low-value crude residues requires upgrading processes such as carbon rejection and hydrogen addition. Among many existing upgrading processes, solvent deasphalting (SDA), a technology for removing asphaltene-rich pitch and producing higher-value deasphalted oil (DAO) by using paraffinic solvents, is promising because it offers the advantages of low installation cost and flexibility in terms of the control of the quality of pitch and DAO. The SDA process requires a considerable amount of expensive solvent. Thus, solvent recovery, an energy-intensive process, is required for improved efficiency. In this paper, DAO/solvent separation experiments were carried out using two solvents, pentane and hexane, to investigate the effect of operating conditions such as temperature, pressure, and DAO/solvent ratio on the process. The DAO/pentane separation was superior to the DAO/hexane separation under similar conditions. Regardless of the solvent type, solvent recovery was increased as the DAO/solvent ratio in the feed was decreased. Solvent recovery was strongly influenced by variations in temperature but was relatively insensitive to changes in pressure.
Author	NAM SUN NHO JEONG HWAN CHUN SANG GOO JEON SUNGYONG MUN SEONJU AHN JUNG MOO LEE SANGCHEOL SHIN KI BONG LEE JEONG GEOL NA
Author_xml	– sequence: 1 givenname: Jung Moo surname: Lee fullname: Lee, Jung Moo – sequence: 2 givenname: Sangcheol surname: Shin fullname: Shin, Sangcheol – sequence: 3 givenname: Seonju surname: Ahn fullname: Ahn, Seonju – sequence: 4 givenname: Jeong Hwan surname: Chun fullname: Chun, Jeong Hwan – sequence: 5 givenname: Ki Bong surname: Lee fullname: Lee, Ki Bong – sequence: 6 givenname: Sungyong surname: Mun fullname: Mun, Sungyong – sequence: 7 givenname: Sang Goo surname: Jeon fullname: Jeon, Sang Goo – sequence: 9 givenname: Nam Sun surname: Nho fullname: Nho, Nam Sun
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Keywords	Solvent deasphalting Organic solvent Deasphalting Separation Hydrocarbon Deasphalted oil Hexane Pentane Recovery
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SubjectTerms	Applied sciences Crude oil Crude oil, natural gas and petroleum products Energy Exact sciences and technology Fuels Hexanes Pentanes Processing of crude oil and oils from shales and tar sands. Processes. Equipment. Refinery and treatment units Recovery Residues Separation Solvents Upgrading
Title	Separation of solvent and deasphalted oil for solvent deasphalting process
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