JP2019520443A5 - - Google Patents
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- Publication number
- JP2019520443A5 JP2019520443A5 JP2018559704A JP2018559704A JP2019520443A5 JP 2019520443 A5 JP2019520443 A5 JP 2019520443A5 JP 2018559704 A JP2018559704 A JP 2018559704A JP 2018559704 A JP2018559704 A JP 2018559704A JP 2019520443 A5 JP2019520443 A5 JP 2019520443A5
- Authority
- JP
- Japan
- Prior art keywords
- boiling fraction
- low
- boiling
- fraction
- crude oil
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000009835 boiling Methods 0.000 claims description 59
- 238000000034 method Methods 0.000 claims description 41
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 16
- 239000010779 crude oil Substances 0.000 claims description 16
- 239000001257 hydrogen Substances 0.000 claims description 16
- 229910052739 hydrogen Inorganic materials 0.000 claims description 16
- 239000000203 mixture Substances 0.000 claims description 16
- 239000003054 catalyst Substances 0.000 claims description 10
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 6
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 6
- 150000001336 alkenes Chemical class 0.000 claims description 5
- 239000007788 liquid Substances 0.000 claims description 5
- 238000000926 separation method Methods 0.000 claims description 5
- 238000004230 steam cracking Methods 0.000 claims description 5
- 239000002184 metal Substances 0.000 claims description 4
- 229910052751 metal Inorganic materials 0.000 claims description 4
- 239000012876 carrier material Substances 0.000 claims description 3
- 238000004821 distillation Methods 0.000 claims description 3
- 238000000197 pyrolysis Methods 0.000 claims description 3
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 claims description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 2
- 125000003118 aryl group Chemical group 0.000 claims description 2
- 238000006243 chemical reaction Methods 0.000 claims description 2
- 230000005484 gravity Effects 0.000 claims description 2
- 229910052750 molybdenum Inorganic materials 0.000 claims description 2
- 229910052759 nickel Inorganic materials 0.000 claims description 2
- 238000004064 recycling Methods 0.000 claims description 2
- 229910052721 tungsten Inorganic materials 0.000 claims description 2
- 238000011144 upstream manufacturing Methods 0.000 claims description 2
- 239000008096 xylene Substances 0.000 claims description 2
- 210000003918 fraction a Anatomy 0.000 claims 2
- 238000000354 decomposition reaction Methods 0.000 claims 1
- 239000012530 fluid Substances 0.000 claims 1
- 239000000463 material Substances 0.000 claims 1
- 238000001816 cooling Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US201662336055P | 2016-05-13 | 2016-05-13 | |
| US62/336,055 | 2016-05-13 | ||
| PCT/US2017/031670 WO2017196791A1 (en) | 2016-05-13 | 2017-05-09 | Conversion of crude oil to petrochemicals |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| JP2019520443A JP2019520443A (ja) | 2019-07-18 |
| JP2019520443A5 true JP2019520443A5 (enExample) | 2020-06-25 |
| JP6895994B2 JP6895994B2 (ja) | 2021-06-30 |
Family
ID=58745389
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2018559704A Active JP6895994B2 (ja) | 2016-05-13 | 2017-05-09 | 原油の石油化学製品への転化 |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US10563141B2 (enExample) |
| EP (1) | EP3455335B1 (enExample) |
| JP (1) | JP6895994B2 (enExample) |
| KR (1) | KR102335299B1 (enExample) |
| CN (1) | CN109153926B (enExample) |
| SA (1) | SA518400414B1 (enExample) |
| SG (1) | SG11201810050SA (enExample) |
| WO (1) | WO2017196791A1 (enExample) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR102800554B1 (ko) * | 2019-03-15 | 2025-04-24 | 루머스 테크놀로지 엘엘씨 | 올레핀 제조를 위한 구성 |
| US11807818B2 (en) * | 2021-01-07 | 2023-11-07 | Saudi Arabian Oil Company | Integrated FCC and aromatic recovery complex to boost BTX and light olefin production |
| US11230676B1 (en) | 2021-01-12 | 2022-01-25 | Saudi Arabian Oil Company | Processes for producing petrochemical products from crude oil |
Family Cites Families (40)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4934527B1 (enExample) | 1969-04-25 | 1974-09-14 | ||
| US3856659A (en) | 1972-12-19 | 1974-12-24 | Mobil Oil Corp | Multiple reactor fcc system relying upon a dual cracking catalyst composition |
| US4134824A (en) | 1977-06-07 | 1979-01-16 | Union Carbide Corporation | Integrated process for the partial oxidation-thermal cracking of crude oil feedstocks |
| US4264435A (en) | 1978-04-05 | 1981-04-28 | The Dow Chemical Company | Crude oil cracking using partial combustion gases |
| JPS59159887A (ja) | 1983-03-03 | 1984-09-10 | Mitsubishi Heavy Ind Ltd | 炭化水素からオレフインを製造するための熱分解法 |
| US4992160A (en) | 1983-05-02 | 1991-02-12 | Uop | Conversion of crude oil feeds by catalytic cracking |
| JPS601138A (ja) | 1983-06-17 | 1985-01-07 | Mitsubishi Heavy Ind Ltd | 炭化水素からオレフイン、および芳香族炭化水素を選択的に製造するための熱分解法 |
| JPS6011584A (ja) | 1983-06-30 | 1985-01-21 | Mitsubishi Heavy Ind Ltd | 炭化水素から石油化学製品を選択的に製造するための熱分解法 |
| JPS60219292A (ja) | 1984-04-13 | 1985-11-01 | Mitsubishi Heavy Ind Ltd | 石油化学製品の選択的製造法 |
| US4830728A (en) | 1986-09-03 | 1989-05-16 | Mobil Oil Corporation | Upgrading naphtha in a multiple riser fluid catalytic cracking operation employing a catalyst mixture |
| JP3580518B2 (ja) | 1996-06-05 | 2004-10-27 | 新日本石油株式会社 | 重質油の流動接触分解法 |
| US5904837A (en) | 1996-10-07 | 1999-05-18 | Nippon Oil Co., Ltd. | Process for fluid catalytic cracking of oils |
| US6033555A (en) | 1997-06-10 | 2000-03-07 | Exxon Chemical Patents Inc. | Sequential catalytic and thermal cracking for enhanced ethylene yield |
| US6210562B1 (en) | 1997-10-15 | 2001-04-03 | China Petrochemical Corporation | Process for production of ethylene and propylene by catalytic pyrolysis of heavy hydrocarbons |
| US6656346B2 (en) | 2001-06-07 | 2003-12-02 | King Fahd University Of Petroleum And Minerals | Fluid catalytic cracking process for heavy oil |
| US6743961B2 (en) | 2002-08-26 | 2004-06-01 | Equistar Chemicals, Lp | Olefin production utilizing whole crude oil |
| US7019187B2 (en) | 2002-09-16 | 2006-03-28 | Equistar Chemicals, Lp | Olefin production utilizing whole crude oil and mild catalytic cracking |
| US6979757B2 (en) | 2003-07-10 | 2005-12-27 | Equistar Chemicals, Lp | Olefin production utilizing whole crude oil and mild controlled cavitation assisted cracking |
| US7247765B2 (en) | 2004-05-21 | 2007-07-24 | Exxonmobil Chemical Patents Inc. | Cracking hydrocarbon feedstock containing resid utilizing partial condensation of vapor phase from vapor/liquid separation to mitigate fouling in a flash/separation vessel |
| US7790018B2 (en) | 2005-05-11 | 2010-09-07 | Saudia Arabian Oil Company | Methods for making higher value products from sulfur containing crude oil |
| US7374664B2 (en) | 2005-09-02 | 2008-05-20 | Equistar Chemicals, Lp | Olefin production utilizing whole crude oil feedstock |
| CN101292013B (zh) * | 2005-10-20 | 2012-10-24 | 埃克森美孚化学专利公司 | 烃残油处理和减粘裂化蒸汽裂化器的原料 |
| US8696888B2 (en) | 2005-10-20 | 2014-04-15 | Exxonmobil Chemical Patents Inc. | Hydrocarbon resid processing |
| US7396449B2 (en) | 2006-03-01 | 2008-07-08 | Equistar Chemicals, Lp | Olefin production utilizing condensate feedstock |
| US7550642B2 (en) | 2006-10-20 | 2009-06-23 | Equistar Chemicals, Lp | Olefin production utilizing whole crude oil/condensate feedstock with enhanced distillate production |
| US20080277314A1 (en) | 2007-05-08 | 2008-11-13 | Halsey Richard B | Olefin production utilizing whole crude oil/condensate feedstock and hydrotreating |
| US20080283445A1 (en) | 2007-05-16 | 2008-11-20 | Powers Donald H | Hydrocarbon thermal cracking using atmospheric residuum |
| US7404889B1 (en) | 2007-06-27 | 2008-07-29 | Equistar Chemicals, Lp | Hydrocarbon thermal cracking using atmospheric distillation |
| US7858834B2 (en) | 2007-08-17 | 2010-12-28 | Equistar Chemicals, Lp | Olefin production utilizing a feed containing condensate and crude oil |
| US20090050523A1 (en) | 2007-08-20 | 2009-02-26 | Halsey Richard B | Olefin production utilizing whole crude oil/condensate feedstock and selective hydrocracking |
| US7744747B2 (en) | 2008-01-02 | 2010-06-29 | Equistar Chemicals, Lp | Olefin production utilizing whole crude oil/condensate feedstock with a partitioned vaporization unit |
| CN102041080A (zh) * | 2009-10-16 | 2011-05-04 | 中国石油化工股份有限公司 | 加氢裂化与生产乙烯裂解原料的综合方法 |
| JP6151716B2 (ja) | 2012-01-27 | 2017-06-21 | サウジ アラビアン オイル カンパニー | 原油の直接処理のための水素処理および蒸気熱分解統合プロセス |
| CN109897660A (zh) * | 2012-01-27 | 2019-06-18 | 沙特阿拉伯石油公司 | 用于直接加工原油的整合的溶剂脱沥青、加氢处理以及水蒸气热解方法 |
| CN104334694B (zh) * | 2012-03-20 | 2016-06-29 | 沙特阿拉伯石油公司 | 由原油生产石油化学产品的集成加氢处理、蒸汽热解和催化裂化工艺 |
| JP6081571B2 (ja) * | 2012-03-20 | 2017-02-15 | サウジ アラビアン オイル カンパニー | 軽質オレフィン及びコークスを生成させる、統合された、原油の水素化処理及び水蒸気熱分解 |
| KR102061187B1 (ko) | 2012-03-20 | 2019-12-31 | 사우디 아라비안 오일 컴퍼니 | 원유의 처리를 위한 통합된 수소화공정 및 유체 촉매 크래킹 방법 |
| EP2828362B1 (en) | 2012-03-20 | 2020-12-30 | Saudi Arabian Oil Company | Integrated slurry hydroprocessing and steam pyrolysis of crude oil to produce petrochemicals |
| SG11201502991RA (en) | 2012-10-19 | 2015-06-29 | Saudi Arabian Oil Co | Process for high severity catalytic cracking of crude oil |
| EP3110925B1 (en) | 2014-02-25 | 2018-12-05 | Saudi Basic Industries Corporation | An integrated hydrocracking process |
-
2017
- 2017-05-05 US US15/588,024 patent/US10563141B2/en active Active
- 2017-05-09 CN CN201780029295.7A patent/CN109153926B/zh active Active
- 2017-05-09 JP JP2018559704A patent/JP6895994B2/ja active Active
- 2017-05-09 SG SG11201810050SA patent/SG11201810050SA/en unknown
- 2017-05-09 WO PCT/US2017/031670 patent/WO2017196791A1/en not_active Ceased
- 2017-05-09 EP EP17725006.5A patent/EP3455335B1/en active Active
- 2017-05-09 KR KR1020187035759A patent/KR102335299B1/ko active Active
-
2018
- 2018-11-11 SA SA518400414A patent/SA518400414B1/ar unknown
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