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Investigation of the co-processing technology of crude oil and coal and its deployment
The effect of process conditions on the co-processing technology of crude oil and coal was investigated. Crude oil/coal matching performance, swelling degree, crude oil/coal slurry viscosity-temperature characteristics and process parameters were obtained via the laboratory scale and pilot scale stu...
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Published in: | Polish journal of chemical technology 2022-12, Vol.24 (4), p.39-50 |
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creator | Li, Suan Liu, Qi Deng, Qingyu Ye, Hang Zhou, Xuejie Qiao, Aijun |
description | The effect of process conditions on the co-processing technology of crude oil and coal was investigated. Crude oil/coal matching performance, swelling degree, crude oil/coal slurry viscosity-temperature characteristics and process parameters were obtained via the laboratory scale and pilot scale studies. The optimum reaction temperature of the co-processing was 445~450
C, the pressure was 19 MPa, the catalyst addition was 3 wt.%, the reaction time was 2 h, and the ratio of hydrogen to crude oil was 1500 (V/V). Furthermore, the co-processing technology including catalyst and corresponding equipment based on the slurry bed hydrogenation were developed. By using this co-processing technology, the feed ratio of crude oil and coal can be 1:1, the coal conversion rate can be over 99%, the light oil (oil and aromatics) yield was over 70%, and the end products were gasoline, diesel, jet fuel, aromatics and LPG. The product quality meets the Euro V standard, whilst aromatics accounted for 48% of the light oil. So it was proved to be feasible to co-refine crude oil and coal at a ratio of 1:1. What’s more, the slurry bed hydrogenation plant and its equipment were tested for long-term operation, and it has been proved that this co-processing technology could be deployed as large-scale industrial application. |
doi_str_mv | 10.2478/pjct-2022-0027 |
format | article |
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C, the pressure was 19 MPa, the catalyst addition was 3 wt.%, the reaction time was 2 h, and the ratio of hydrogen to crude oil was 1500 (V/V). Furthermore, the co-processing technology including catalyst and corresponding equipment based on the slurry bed hydrogenation were developed. By using this co-processing technology, the feed ratio of crude oil and coal can be 1:1, the coal conversion rate can be over 99%, the light oil (oil and aromatics) yield was over 70%, and the end products were gasoline, diesel, jet fuel, aromatics and LPG. The product quality meets the Euro V standard, whilst aromatics accounted for 48% of the light oil. So it was proved to be feasible to co-refine crude oil and coal at a ratio of 1:1. What’s more, the slurry bed hydrogenation plant and its equipment were tested for long-term operation, and it has been proved that this co-processing technology could be deployed as large-scale industrial application.</description><identifier>ISSN: 1899-4741</identifier><identifier>ISSN: 1509-8117</identifier><identifier>EISSN: 1899-4741</identifier><identifier>DOI: 10.2478/pjct-2022-0027</identifier><language>eng</language><publisher>Szczecin: Sciendo</publisher><subject>Catalysts ; Coal ; Crude oil ; Diesel fuels ; Hydrogenation ; industrial application ; Industrial applications ; Jet engine fuels ; process development ; Process parameters ; Reaction time ; Slurries ; the co-processing technology</subject><ispartof>Polish journal of chemical technology, 2022-12, Vol.24 (4), p.39-50</ispartof><rights>2022. This work is published under http://creativecommons.org/licenses/by/4.0 (the “License”). Notwithstanding the ProQuest Terms and Conditions, you may use this content in accordance with the terms of the License.</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><cites>FETCH-LOGICAL-c380t-8a5695fa5b2ba4a0e2f3bff63e002177171bccb15c2ef11eff4bd3c175d9f11f3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.proquest.com/docview/2758222255?pq-origsite=primo$$EHTML$$P50$$Gproquest$$Hfree_for_read</linktohtml><link.rule.ids>314,777,781,25734,27905,27906,36993,44571</link.rule.ids></links><search><creatorcontrib>Li, Suan</creatorcontrib><creatorcontrib>Liu, Qi</creatorcontrib><creatorcontrib>Deng, Qingyu</creatorcontrib><creatorcontrib>Ye, Hang</creatorcontrib><creatorcontrib>Zhou, Xuejie</creatorcontrib><creatorcontrib>Qiao, Aijun</creatorcontrib><title>Investigation of the co-processing technology of crude oil and coal and its deployment</title><title>Polish journal of chemical technology</title><description>The effect of process conditions on the co-processing technology of crude oil and coal was investigated. Crude oil/coal matching performance, swelling degree, crude oil/coal slurry viscosity-temperature characteristics and process parameters were obtained via the laboratory scale and pilot scale studies. The optimum reaction temperature of the co-processing was 445~450
C, the pressure was 19 MPa, the catalyst addition was 3 wt.%, the reaction time was 2 h, and the ratio of hydrogen to crude oil was 1500 (V/V). Furthermore, the co-processing technology including catalyst and corresponding equipment based on the slurry bed hydrogenation were developed. By using this co-processing technology, the feed ratio of crude oil and coal can be 1:1, the coal conversion rate can be over 99%, the light oil (oil and aromatics) yield was over 70%, and the end products were gasoline, diesel, jet fuel, aromatics and LPG. The product quality meets the Euro V standard, whilst aromatics accounted for 48% of the light oil. So it was proved to be feasible to co-refine crude oil and coal at a ratio of 1:1. 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C, the pressure was 19 MPa, the catalyst addition was 3 wt.%, the reaction time was 2 h, and the ratio of hydrogen to crude oil was 1500 (V/V). Furthermore, the co-processing technology including catalyst and corresponding equipment based on the slurry bed hydrogenation were developed. By using this co-processing technology, the feed ratio of crude oil and coal can be 1:1, the coal conversion rate can be over 99%, the light oil (oil and aromatics) yield was over 70%, and the end products were gasoline, diesel, jet fuel, aromatics and LPG. The product quality meets the Euro V standard, whilst aromatics accounted for 48% of the light oil. So it was proved to be feasible to co-refine crude oil and coal at a ratio of 1:1. What’s more, the slurry bed hydrogenation plant and its equipment were tested for long-term operation, and it has been proved that this co-processing technology could be deployed as large-scale industrial application.</abstract><cop>Szczecin</cop><pub>Sciendo</pub><doi>10.2478/pjct-2022-0027</doi><tpages>12</tpages><oa>free_for_read</oa></addata></record> |
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subjects | Catalysts Coal Crude oil Diesel fuels Hydrogenation industrial application Industrial applications Jet engine fuels process development Process parameters Reaction time Slurries the co-processing technology |
title | Investigation of the co-processing technology of crude oil and coal and its deployment |
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