JP2020512417A5 - - Google Patents
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- JP2020512417A5 JP2020512417A5 JP2019527447A JP2019527447A JP2020512417A5 JP 2020512417 A5 JP2020512417 A5 JP 2020512417A5 JP 2019527447 A JP2019527447 A JP 2019527447A JP 2019527447 A JP2019527447 A JP 2019527447A JP 2020512417 A5 JP2020512417 A5 JP 2020512417A5
- Authority
- JP
- Japan
- Prior art keywords
- fraction
- region
- naphtha
- fcc
- stream
- 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.)
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- 238000004231 fluid catalytic cracking Methods 0.000 claims 25
- 238000000605 extraction Methods 0.000 claims 21
- 150000001491 aromatic compounds Chemical class 0.000 claims 20
- 239000007789 gas Substances 0.000 claims 19
- 239000003921 oil Substances 0.000 claims 19
- 238000004519 manufacturing process Methods 0.000 claims 11
- 150000001336 alkenes Chemical class 0.000 claims 10
- 238000005984 hydrogenation reaction Methods 0.000 claims 9
- 238000000034 method Methods 0.000 claims 9
- 238000000354 decomposition reaction Methods 0.000 claims 8
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims 8
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 claims 6
- 238000000197 pyrolysis Methods 0.000 claims 6
- 239000002994 raw material Substances 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
- 238000000926 separation method Methods 0.000 claims 4
- 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
- 239000003348 petrochemical agent Substances 0.000 claims 3
- 238000011084 recovery Methods 0.000 claims 3
- 238000005979 thermal decomposition reaction Methods 0.000 claims 3
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 claims 2
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 claims 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims 2
- 239000005977 Ethylene Substances 0.000 claims 2
- IAQRGUVFOMOMEM-UHFFFAOYSA-N butene Natural products CC=CC IAQRGUVFOMOMEM-UHFFFAOYSA-N 0.000 claims 2
- 150000001875 compounds Chemical class 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
- 239000000446 fuel Substances 0.000 claims 2
- 239000007788 liquid Substances 0.000 claims 2
- 239000000203 mixture Substances 0.000 claims 2
- 230000007935 neutral effect Effects 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
- 238000005292 vacuum distillation Methods 0.000 claims 2
- 125000003118 aryl group Chemical group 0.000 claims 1
- 230000006837 decompression Effects 0.000 claims 1
- 238000007599 discharging Methods 0.000 claims 1
- 239000012530 fluid Substances 0.000 claims 1
- 239000003205 fragrance Substances 0.000 claims 1
- 239000002737 fuel gas Substances 0.000 claims 1
- 239000012188 paraffin wax Substances 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
Applications Claiming Priority (9)
| 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 | |
| US62/450,058 | 2017-01-24 | ||
| US62/450,018 | 2017-01-24 | ||
| 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 |
| US15/710,799 | 2017-09-20 | ||
| PCT/US2017/062607 WO2018094351A1 (en) | 2016-11-21 | 2017-11-20 | Process and system for conversion of crude oil to petrochemicals and fuel products integrating steam cracking and fluid catalytic cracking |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2020512417A JP2020512417A (ja) | 2020-04-23 |
| JP2020512417A5 true JP2020512417A5 (https=) | 2021-01-07 |
Family
ID=62144318
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2019527447A Withdrawn JP2020512417A (ja) | 2016-11-21 | 2017-11-20 | 水蒸気分解及び流動接触分解を統合した、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 (6)
| Country | Link |
|---|---|
| US (3) | US20180142167A1 (https=) |
| EP (1) | EP3541899B1 (https=) |
| JP (1) | JP2020512417A (https=) |
| KR (1) | KR20190087477A (https=) |
| CN (1) | CN110088242B (https=) |
| WO (1) | WO2018094351A1 (https=) |
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| US9452955B2 (en) | 2013-03-14 | 2016-09-27 | Lummus Technology Inc. | Process for producing distillate fuels and anode grade coke from vacuum resid |
| EP2992070A2 (en) | 2013-05-02 | 2016-03-09 | Shell Internationale Research Maatschappij B.V. | Process for preparing a heavy base oil |
| CA2818322C (en) * | 2013-05-24 | 2015-03-10 | Expander Energy Inc. | Refinery process for heavy oil and bitumen |
| CN109593556A (zh) | 2013-07-02 | 2019-04-09 | 沙特基础工业公司 | 用于将原油转化成具有改进的丙烯产率的石化品的方法和设施 |
| ES2671782T3 (es) | 2013-07-02 | 2018-06-08 | Saudi Basic Industries Corporation | Método para craquear una materia prima hidrocarbonada en una unidad de craqueador a vapor |
| US9856425B2 (en) | 2013-07-02 | 2018-01-02 | Saudi Basic Industries Corporation | Method of producing aromatics and light olefins from a hydrocarbon feedstock |
| CN105308156B (zh) | 2013-07-02 | 2017-06-09 | 沙特基础工业公司 | 用于将原油转化成具有改进的btx产率的石化品的方法和设施 |
| SG11201508916TA (en) | 2013-07-02 | 2016-01-28 | Saudi Basic Ind Corp | Process for upgrading refinery heavy residues to petrochemicals |
| ES2725609T3 (es) * | 2013-07-02 | 2019-09-25 | Saudi Basic Ind Corp | Proceso e instalación para la conversión de crudo en productos petroquímicos que tienen un rendimiento de etileno mejorado |
| ITMI20131137A1 (it) * | 2013-07-05 | 2015-01-06 | Eni Spa | Procedimento per la raffinazione del greggio |
| 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 |
| FR3014897B1 (fr) | 2013-12-17 | 2017-04-07 | Ifp Energies Now | Nouveau procede integre de traitement de charges petrolieres pour la production de fiouls a basse teneur en soufre et en sediments |
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| RU2705590C9 (ru) | 2014-11-06 | 2019-12-19 | Бипи Европа Се | Способ и устройство для гидроконверсии углеводородов |
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-
2017
- 2017-09-20 US US15/710,799 patent/US20180142167A1/en not_active Abandoned
- 2017-11-17 US US15/817,146 patent/US10717941B2/en active Active
- 2017-11-20 KR KR1020197017068A patent/KR20190087477A/ko not_active Withdrawn
- 2017-11-20 CN CN201780078199.1A patent/CN110088242B/zh not_active Expired - Fee Related
- 2017-11-20 JP JP2019527447A patent/JP2020512417A/ja not_active Withdrawn
- 2017-11-20 EP EP17812153.9A patent/EP3541899B1/en active Active
- 2017-11-20 WO PCT/US2017/062607 patent/WO2018094351A1/en not_active Ceased
-
2019
- 2019-08-29 US US16/555,814 patent/US10913908B2/en active Active
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