JP2020500966A5 - - Google Patents
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- JP2020500966A5 JP2020500966A5 JP2019527360A JP2019527360A JP2020500966A5 JP 2020500966 A5 JP2020500966 A5 JP 2020500966A5 JP 2019527360 A JP2019527360 A JP 2019527360A JP 2019527360 A JP2019527360 A JP 2019527360A JP 2020500966 A5 JP2020500966 A5 JP 2020500966A5
- Authority
- JP
- Japan
- Prior art keywords
- fraction
- region
- naphtha
- stream
- 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.)
- Withdrawn
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- 239000003921 oil Substances 0.000 claims 23
- 150000001491 aromatic compounds Chemical class 0.000 claims 19
- 239000007789 gas Substances 0.000 claims 19
- 238000000605 extraction Methods 0.000 claims 16
- 238000004519 manufacturing process Methods 0.000 claims 11
- 238000000034 method Methods 0.000 claims 11
- 238000000197 pyrolysis Methods 0.000 claims 11
- 150000001336 alkenes Chemical class 0.000 claims 9
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 claims 8
- 238000001833 catalytic reforming Methods 0.000 claims 8
- 238000000354 decomposition reaction Methods 0.000 claims 8
- 238000005984 hydrogenation reaction Methods 0.000 claims 8
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims 8
- 239000007788 liquid Substances 0.000 claims 6
- 239000012188 paraffin wax Substances 0.000 claims 6
- 239000000203 mixture Substances 0.000 claims 5
- 239000002994 raw material Substances 0.000 claims 5
- 238000002407 reforming Methods 0.000 claims 5
- 238000004821 distillation Methods 0.000 claims 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims 4
- 239000003348 petrochemical agent Substances 0.000 claims 4
- 238000000926 separation method Methods 0.000 claims 4
- 239000000126 substance Substances 0.000 claims 4
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 claims 3
- IAQRGUVFOMOMEM-UHFFFAOYSA-N butene Natural products CC=CC IAQRGUVFOMOMEM-UHFFFAOYSA-N 0.000 claims 3
- 238000005336 cracking Methods 0.000 claims 3
- 239000010779 crude oil Substances 0.000 claims 3
- 239000000295 fuel oil Substances 0.000 claims 3
- 238000005649 metathesis reaction Methods 0.000 claims 3
- 230000007935 neutral effect Effects 0.000 claims 3
- 238000011084 recovery Methods 0.000 claims 3
- 238000011069 regeneration method Methods 0.000 claims 3
- 238000004230 steam cracking Methods 0.000 claims 3
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims 2
- 239000005977 Ethylene Substances 0.000 claims 2
- 239000002283 diesel fuel Substances 0.000 claims 2
- 238000009826 distribution Methods 0.000 claims 2
- -1 ethylene, propylene Chemical group 0.000 claims 2
- 239000012530 fluid Substances 0.000 claims 2
- 239000000446 fuel Substances 0.000 claims 2
- 239000000463 material Substances 0.000 claims 2
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 claims 2
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 claims 2
- 230000008929 regeneration Effects 0.000 claims 2
- 238000005292 vacuum distillation Methods 0.000 claims 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 2
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 claims 1
- 125000003118 aryl group Chemical group 0.000 claims 1
- 230000001588 bifunctional effect Effects 0.000 claims 1
- 239000003054 catalyst Substances 0.000 claims 1
- 230000003197 catalytic effect Effects 0.000 claims 1
- 238000007385 chemical modification Methods 0.000 claims 1
- 150000001875 compounds Chemical class 0.000 claims 1
- 125000004122 cyclic group Chemical group 0.000 claims 1
- 230000006837 decompression Effects 0.000 claims 1
- 238000007599 discharging Methods 0.000 claims 1
- 238000004231 fluid catalytic cracking Methods 0.000 claims 1
- 239000002737 fuel gas Substances 0.000 claims 1
- 238000012986 modification Methods 0.000 claims 1
- 230000004048 modification Effects 0.000 claims 1
- 238000002360 preparation method Methods 0.000 claims 1
- 238000007670 refining Methods 0.000 claims 1
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 claims 1
- 238000005979 thermal decomposition reaction Methods 0.000 claims 1
Images
Applications Claiming Priority (11)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US201662424883P | 2016-11-21 | 2016-11-21 | |
| US62/424,883 | 2016-11-21 | ||
| US201762450058P | 2017-01-24 | 2017-01-24 | |
| US201762450018P | 2017-01-24 | 2017-01-24 | |
| US201762450060P | 2017-01-24 | 2017-01-24 | |
| US62/450,060 | 2017-01-24 | ||
| US62/450,058 | 2017-01-24 | ||
| US62/450,018 | 2017-01-24 | ||
| US15/710,799 | 2017-09-20 | ||
| US15/710,799 US20180142167A1 (en) | 2016-11-21 | 2017-09-20 | Process and system for conversion of crude oil to chemicals and fuel products integrating steam cracking and fluid catalytic cracking |
| PCT/US2017/062614 WO2018094353A1 (en) | 2016-11-21 | 2017-11-20 | Process and system for conversion of crude oil to petrochemicals and fuel products integrating steam cracking, fluid catalytic cracking, and conversion of naphtha into chemical rich reformate |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2020500966A JP2020500966A (ja) | 2020-01-16 |
| JP2020500966A5 true JP2020500966A5 (enExample) | 2021-01-07 |
Family
ID=62145873
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2019527360A Withdrawn JP2020500966A (ja) | 2016-11-21 | 2017-11-20 | 水蒸気分解、流動接触分解、及びナフサから濃化学物質改質油への転化を統合した、原油を石油化学製品及び燃料製品に転化するためのプロセス及びシステム |
Country Status (5)
| Country | Link |
|---|---|
| EP (1) | EP3541894B1 (enExample) |
| JP (1) | JP2020500966A (enExample) |
| KR (1) | KR20190086707A (enExample) |
| CN (1) | CN110214170B (enExample) |
| WO (1) | WO2018094353A1 (enExample) |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11279891B2 (en) * | 2020-03-05 | 2022-03-22 | Saudi Arabian Oil Company | Systems and processes for direct crude oil upgrading to hydrogen and chemicals |
| EP4243974A1 (en) * | 2020-11-13 | 2023-09-20 | Shell Internationale Research Maatschappij B.V. | Methods for replacing a spent catalyst of a reactor train of an operating hydroprocessing system |
| CN112500891A (zh) * | 2020-12-23 | 2021-03-16 | 北京石油化工工程研究院 | 一种重油的加工方法及系统 |
| CN116554927B (zh) * | 2022-01-28 | 2024-10-11 | 中国石油化工股份有限公司 | 一种重油生产低碳烯烃和芳烃的方法及系统 |
| CN114674780B (zh) * | 2022-03-16 | 2025-02-11 | 中国石油化工股份有限公司 | 一种轻质原油的调配方法 |
| US11820950B1 (en) | 2022-06-16 | 2023-11-21 | Saudi Arabian Oil Company | Conversion of whole crude to value added petrochemicals in an integrated reactor process |
| US11866663B1 (en) * | 2023-02-02 | 2024-01-09 | Saudi Arabian Oil Company | Multi-zone catalytic cracking of crude oils |
| US11939539B1 (en) * | 2023-06-09 | 2024-03-26 | Saudi Arabian Oil Company | Multi-zone catalytic cracking of crude oils |
| CN119912975B (zh) * | 2023-10-30 | 2025-11-14 | 中国石油化工股份有限公司 | 一种生产全化工品的原油加工方法及系统 |
| FR3160184A1 (fr) | 2024-03-14 | 2025-09-19 | IFP Energies Nouvelles | Procédé de production de bases pour la pétrochimie comprenant un craquage catalytique fluide, un oligocraquage, un hydrocraquage en lit fixe, un reformage catalytique et un vapocraquage |
| FR3160183A1 (fr) | 2024-03-14 | 2025-09-19 | IFP Energies Nouvelles | Procédé de production de bases pour la pétrochimie comprenant un craquage catalytique fluide, une oligomérisation, un hydrocraquage en lit fixe, un reformage catalytique et un vapocraquage |
| FR3160185A1 (fr) | 2024-03-14 | 2025-09-19 | IFP Energies Nouvelles | Procédé de production de bases pour la pétrochimie comprenant un craquage catalytique fluide, un hydrocraquage en lit fixe, un reformage catalytique et un vapocraquage |
Family Cites Families (19)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3702292A (en) * | 1970-03-10 | 1972-11-07 | Du Pont | Composite hydrocarbon refinery apparatus and process arrangement |
| CN1031646C (zh) | 1992-10-22 | 1996-04-24 | 中国石油化工总公司 | 石油烃的催化转化方法 |
| US6538169B1 (en) | 2000-11-13 | 2003-03-25 | Uop Llc | FCC process with improved yield of light olefins |
| US20020195373A1 (en) | 2001-06-07 | 2002-12-26 | Takashi Ino | Heavy oil fluid catalytic cracking process |
| US6656346B2 (en) | 2001-06-07 | 2003-12-02 | King Fahd University Of Petroleum And Minerals | Fluid catalytic cracking process for heavy oil |
| US8558036B2 (en) | 2010-11-15 | 2013-10-15 | Saudi Arabian Oil Company | Dual phase catalysts system for mixed olefin hydrations |
| US8629080B2 (en) | 2011-03-21 | 2014-01-14 | Saudi Arabian Oil Company | Hydrated niobium oxide nanoparticle containing catalysts for olefin hydration |
| US8999013B2 (en) | 2011-11-01 | 2015-04-07 | Saudi Arabian Oil Company | Method for contemporaneously dimerizing and hydrating a feed having butene |
| KR101876612B1 (ko) | 2011-12-05 | 2018-07-09 | 사우디 아라비안 오일 컴퍼니 | 친수성 멤브레인 통합형 올레핀 수화 공정 |
| US9187388B2 (en) | 2012-09-05 | 2015-11-17 | Saudi Arabian Oil Company | Olefin hydration process using oscillatory baffled reactor |
| US10155707B2 (en) | 2012-09-05 | 2018-12-18 | Saudi Arabian Oil Company | Olefin hydration process using oscillatory baffled reactor |
| CN105308159B (zh) * | 2013-07-02 | 2018-06-22 | 沙特基础工业公司 | 用于将原油转化成具有改进的乙烯产率的石化品的方法和设施 |
| KR102308545B1 (ko) * | 2013-07-02 | 2021-10-05 | 사우디 베이식 인더스트리즈 코포레이션 | 탄화수소 공급원료로부터 방향족 화합물 및 경질 올레핀을 생산하는 방법 |
| EP3017029B1 (en) * | 2013-07-02 | 2018-07-18 | Saudi Basic Industries Corporation | Process and installation for the conversion of crude oil to petrochemicals having an improved propylene yield |
| WO2015000850A1 (en) * | 2013-07-02 | 2015-01-08 | Saudi Basic Industries Corporation | Process and installation for the conversion of crude oil to petrochemicals having an improved btx yield |
| KR102325584B1 (ko) * | 2013-07-02 | 2021-11-15 | 사우디 베이식 인더스트리즈 코포레이션 | 정제소 중질 잔사유를 석유화학물질로 업그레이드하는 방법 |
| US20150148572A1 (en) | 2013-11-27 | 2015-05-28 | Saudi Arabian Oil Company | Process for the Dimerization/Oligomerization of Mixed Butenes Over an Ion-Exchange Resin Catalyst |
| US9447346B2 (en) | 2013-12-11 | 2016-09-20 | Saudi Arabian Oil Company | Two-step process for production of RON-enhanced mixed butanols and diisobutenes |
| US9732018B2 (en) | 2014-02-11 | 2017-08-15 | Saudi Arabian Oil Company | Process for production of mixed butanols and diisobutenes as fuel blending components |
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2017
- 2017-11-20 WO PCT/US2017/062614 patent/WO2018094353A1/en not_active Ceased
- 2017-11-20 JP JP2019527360A patent/JP2020500966A/ja not_active Withdrawn
- 2017-11-20 CN CN201780078195.3A patent/CN110214170B/zh not_active Expired - Fee Related
- 2017-11-20 KR KR1020197017067A patent/KR20190086707A/ko not_active Withdrawn
- 2017-11-20 EP EP17812154.7A patent/EP3541894B1/en active Active