JP2017509745A5 - - Google Patents
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- JP2017509745A5 JP2017509745A5 JP2016553574A JP2016553574A JP2017509745A5 JP 2017509745 A5 JP2017509745 A5 JP 2017509745A5 JP 2016553574 A JP2016553574 A JP 2016553574A JP 2016553574 A JP2016553574 A JP 2016553574A JP 2017509745 A5 JP2017509745 A5 JP 2017509745A5
- Authority
- JP
- Japan
- Prior art keywords
- process according
- stream
- gas stream
- ring
- pressure
- 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
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- 238000000034 method Methods 0.000 claims description 41
- 150000002430 hydrocarbons Chemical class 0.000 claims description 40
- 229930195733 hydrocarbon Natural products 0.000 claims description 37
- 239000007789 gas Substances 0.000 claims description 28
- 239000004215 Carbon black (E152) Substances 0.000 claims description 19
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 claims description 14
- 238000004517 catalytic hydrocracking Methods 0.000 claims description 13
- 239000001257 hydrogen Substances 0.000 claims description 12
- 229910052739 hydrogen Inorganic materials 0.000 claims description 12
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 11
- 238000009835 boiling Methods 0.000 claims description 11
- 239000003921 oil Substances 0.000 claims description 10
- 238000006356 dehydrogenation reaction Methods 0.000 claims description 9
- 239000003054 catalyst Substances 0.000 claims description 8
- 238000006243 chemical reaction Methods 0.000 claims description 7
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 claims description 7
- 239000001294 propane Substances 0.000 claims description 7
- 238000004821 distillation Methods 0.000 claims description 6
- 238000004230 steam cracking Methods 0.000 claims description 6
- 239000007788 liquid Substances 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 5
- 239000012188 paraffin wax Substances 0.000 claims description 4
- 238000000926 separation method Methods 0.000 claims description 4
- 238000007142 ring opening reaction Methods 0.000 claims 9
- 150000001491 aromatic compounds Chemical class 0.000 claims 4
- 239000001273 butane Substances 0.000 claims 4
- HOWJQLVNDUGZBI-UHFFFAOYSA-N butane;propane Chemical compound CCC.CCCC HOWJQLVNDUGZBI-UHFFFAOYSA-N 0.000 claims 4
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims 4
- 239000002994 raw material Substances 0.000 claims 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims 3
- 238000000605 extraction Methods 0.000 claims 3
- 125000000217 alkyl group Chemical group 0.000 claims 2
- 239000010724 circulating oil Substances 0.000 claims 2
- 239000010779 crude oil Substances 0.000 claims 2
- 238000003385 ring cleavage reaction Methods 0.000 claims 2
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 claims 1
- 230000003197 catalytic effect Effects 0.000 claims 1
- 239000007795 chemical reaction product Substances 0.000 claims 1
- 239000000571 coke Substances 0.000 claims 1
- 230000018044 dehydration Effects 0.000 claims 1
- 238000006297 dehydration reaction Methods 0.000 claims 1
- 238000005984 hydrogenation reaction Methods 0.000 claims 1
- 239000003350 kerosene Substances 0.000 claims 1
- 239000002808 molecular sieve Substances 0.000 claims 1
- 239000000047 product Substances 0.000 claims 1
- 238000002407 reforming Methods 0.000 claims 1
- 239000003079 shale oil Substances 0.000 claims 1
- 239000002002 slurry Substances 0.000 claims 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims 1
- 238000000638 solvent extraction Methods 0.000 claims 1
- 238000004227 thermal cracking Methods 0.000 claims 1
- 239000001993 wax Substances 0.000 claims 1
- 239000008096 xylene Substances 0.000 claims 1
- 125000004432 carbon atom Chemical group C* 0.000 description 15
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 8
- 239000002283 diesel fuel Substances 0.000 description 3
- 238000005292 vacuum distillation Methods 0.000 description 3
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 2
- 238000004523 catalytic cracking Methods 0.000 description 2
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 2
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 description 2
- 125000004178 (C1-C4) alkyl group Chemical group 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 239000010426 asphalt Substances 0.000 description 1
- 125000004429 atom Chemical group 0.000 description 1
- 125000002619 bicyclic group Chemical group 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 229930195734 saturated hydrocarbon Natural products 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP14156629 | 2014-02-25 | ||
| EP14156629.9 | 2014-02-25 | ||
| PCT/EP2014/079193 WO2015128036A1 (en) | 2014-02-25 | 2014-12-23 | Process for upgrading refinery heavy hydrocarbons to petrochemicals |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| JP2017509745A JP2017509745A (ja) | 2017-04-06 |
| JP2017509745A5 true JP2017509745A5 (enExample) | 2017-11-30 |
| JP6574432B2 JP6574432B2 (ja) | 2019-09-11 |
Family
ID=50156658
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2016553574A Expired - Fee Related JP6574432B2 (ja) | 2014-02-25 | 2014-12-23 | 製油所重質炭化水素の石油化学製品へのアップグレードプロセス |
Country Status (9)
| Country | Link |
|---|---|
| US (1) | US20160362618A1 (enExample) |
| EP (1) | EP3110918B1 (enExample) |
| JP (1) | JP6574432B2 (enExample) |
| KR (1) | KR102387828B1 (enExample) |
| CN (1) | CN106103663B (enExample) |
| EA (1) | EA032758B1 (enExample) |
| ES (1) | ES2703209T3 (enExample) |
| SG (1) | SG11201606012PA (enExample) |
| WO (1) | WO2015128036A1 (enExample) |
Families Citing this family (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105505451B (zh) * | 2016-01-04 | 2017-07-11 | 北京神雾环境能源科技集团股份有限公司 | 焦油裂解的装置以及进行焦油裂解的方法 |
| CN108884397B (zh) * | 2016-02-05 | 2021-08-31 | 沙特基础全球技术有限公司 | 具有改善的产品产率的将原油转化为石油化学品的方法和装置 |
| US20180142167A1 (en) * | 2016-11-21 | 2018-05-24 | Saudi Arabian Oil Company | Process and system for conversion of crude oil to chemicals and fuel products integrating steam cracking and fluid catalytic cracking |
| US10968399B2 (en) | 2017-04-07 | 2021-04-06 | Citgo Petroleum Corporation | Online coke removal in a heater pass |
| FR3098824B1 (fr) | 2019-07-17 | 2021-09-03 | Ifp Energies Now | Procede de production d’olefines comprenant un hydrotraitement, un desasphaltage, un hydrocraquage et un vapocraquage |
| US12122963B2 (en) | 2019-07-31 | 2024-10-22 | Sabic Global Technologies B.V. | Naphtha catalytic cracking process |
| US11046899B2 (en) | 2019-10-03 | 2021-06-29 | Saudi Arabian Oil Company | Two stage hydrodearylation systems and processes to convert heavy aromatics into gasoline blending components and chemical grade aromatics |
| KR20220117899A (ko) * | 2019-12-23 | 2022-08-24 | 셰브런 유.에스.에이.인크. | 정제 fcc 장치를 통한 플라스틱 폐기물의 폴리프로필렌으로의 순환 경제 |
| US10961470B1 (en) | 2020-04-23 | 2021-03-30 | Saudi Arabian Oil Company | Thermal hydrodealkylation of hydrocracking feedstock to mitigate HPNA formation |
| CN114426879B (zh) * | 2020-10-15 | 2023-08-08 | 中国石油化工股份有限公司 | 含烃混合物的利用系统和方法 |
| US11578276B2 (en) * | 2021-07-01 | 2023-02-14 | Saudi Arabian Oil Company | Two stage catalytic process for pyrolysis oil upgrading to BTX |
| US11377400B1 (en) * | 2021-07-01 | 2022-07-05 | Saudi Arabian Oil Company | Three stage catalytic process for pyrolysis oil upgrading to xylenes |
| CN118440739B (zh) * | 2023-02-03 | 2025-07-01 | 中国石油化工股份有限公司 | 一种焦化和加氢裂化联合生产化工原料的方法 |
Family Cites Families (23)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3268436A (en) * | 1964-02-25 | 1966-08-23 | Exxon Research Engineering Co | Paraffinic jet fuel by hydrocracking wax |
| US3617507A (en) * | 1968-02-17 | 1971-11-02 | Basf Ag | Process for hydrocracking heavy hydrocarbons |
| US3617482A (en) * | 1969-11-10 | 1971-11-02 | Chevron Res | Process for the production of lubricating oils |
| US3726789A (en) * | 1971-04-05 | 1973-04-10 | Ashland Oil Inc | Hydrocarbon conversion process for the production of olefins and aromatics |
| GB1504776A (en) * | 1975-08-14 | 1978-03-22 | Davy Powergas Ltd | Hydrocracking c3 or higher hydrocarbon feedstock |
| US4137147A (en) * | 1976-09-16 | 1979-01-30 | Institut Francais Du Petrole | Process for manufacturing olefinic hydrocarbons with respectively two and three carbon atoms per molecule |
| US4418006A (en) * | 1980-07-21 | 1983-11-29 | Standard Oil Company (Indiana) | Hydrocarbon conversion catalyst system |
| US4458096A (en) * | 1983-05-26 | 1984-07-03 | Air Products And Chemicals, Inc. | Process for the production of ethylene and propylene |
| US4664777A (en) * | 1984-07-30 | 1987-05-12 | Exxon Research And Engineering Company | Process for improving octane by the conversion of fused multi-ring aromatics and hydroaromatics to lower molecular weight compounds |
| US4943366A (en) * | 1985-06-03 | 1990-07-24 | Mobil Oil Corporation | Production of high octane gasoline |
| CA2309093C (en) * | 1997-11-03 | 2009-05-05 | Mobil Oil Corporation | Low pressure naphtha hydrocracking process |
| US6133192A (en) * | 1998-12-29 | 2000-10-17 | Phillips Petroleum Company | Catalyst material, the preparation thereof and the use thereof in converting hydrocarbons |
| US7012038B2 (en) * | 2002-06-12 | 2006-03-14 | Engelhard Corporation | Paraffin dehydrogenation catalyst |
| KR100710542B1 (ko) * | 2005-06-21 | 2007-04-24 | 에스케이 주식회사 | 탄화수소 원료 혼합물로부터 경질 올레핀계 탄화수소의증산방법 |
| CA2541051C (en) * | 2005-09-20 | 2013-04-02 | Nova Chemicals Corporation | Aromatic saturation and ring opening process |
| EP1779929A1 (en) * | 2005-10-27 | 2007-05-02 | Süd-Chemie Ag | A catalyst composition for hydrocracking and process of mild hydrocracking and ring opening |
| KR101234448B1 (ko) * | 2005-11-14 | 2013-02-18 | 에스케이이노베이션 주식회사 | 탄화수소 혼합물로부터 방향족 탄화수소 및 액화석유가스를제조하는 공정 |
| WO2010116603A1 (ja) * | 2009-03-30 | 2010-10-14 | 財団法人石油産業活性化センター | アルキルベンゼン類の製造方法及びそれに用いる触媒 |
| US8481797B2 (en) * | 2010-10-01 | 2013-07-09 | Uop Llc | Processes for maximizing high-value aromatics production utilizing stabilized crude benzene withdrawal |
| ES2654404T3 (es) * | 2010-10-22 | 2018-02-13 | Sk Innovation Co., Ltd. | Método para producir compuestos aromáticos valiosos y parafinas ligeras a partir de aceites hidrocarbonáceos derivados del petróleo, carbón o madera |
| WO2012071137A1 (en) * | 2010-11-01 | 2012-05-31 | Shell Oil Company | Process for hydrocracking butane or naphtha in the presence of a combination of two zeolites |
| US9139782B2 (en) * | 2011-02-11 | 2015-09-22 | E I Du Pont De Nemours And Company | Targeted pretreatment and selective ring opening in liquid-full reactors |
| CN105473691B (zh) * | 2013-07-02 | 2019-03-15 | 沙特基础工业公司 | 从烃原料生产轻质烯烃和芳烃的方法 |
-
2014
- 2014-12-23 WO PCT/EP2014/079193 patent/WO2015128036A1/en not_active Ceased
- 2014-12-23 KR KR1020167026466A patent/KR102387828B1/ko active Active
- 2014-12-23 SG SG11201606012PA patent/SG11201606012PA/en unknown
- 2014-12-23 US US15/120,931 patent/US20160362618A1/en not_active Abandoned
- 2014-12-23 EA EA201691719A patent/EA032758B1/ru not_active IP Right Cessation
- 2014-12-23 JP JP2016553574A patent/JP6574432B2/ja not_active Expired - Fee Related
- 2014-12-23 CN CN201480076307.8A patent/CN106103663B/zh active Active
- 2014-12-23 EP EP14827222.2A patent/EP3110918B1/en active Active
- 2014-12-23 ES ES14827222T patent/ES2703209T3/es active Active
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