KR102309267B1 - 탄화수소 공급원료를 증기 분해기 단위에서 분해하는 방법 - Google Patents
탄화수소 공급원료를 증기 분해기 단위에서 분해하는 방법 Download PDFInfo
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- KR102309267B1 KR102309267B1 KR1020157037149A KR20157037149A KR102309267B1 KR 102309267 B1 KR102309267 B1 KR 102309267B1 KR 1020157037149 A KR1020157037149 A KR 1020157037149A KR 20157037149 A KR20157037149 A KR 20157037149A KR 102309267 B1 KR102309267 B1 KR 102309267B1
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- aromatics
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Classifications
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G51/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only
- C10G51/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural serial stages only
- C10G51/023—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural serial stages only only thermal cracking steps
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G69/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process
- C10G69/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only
- C10G69/06—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only including at least one step of thermal cracking in the absence of hydrogen
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G51/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
- C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
- C10G65/10—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only cracking steps
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G67/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only
- C10G67/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only
- C10G67/04—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only including solvent extraction as the refining step in the absence of hydrogen
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G9/00—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G9/34—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts
- C10G9/36—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts with heated gases or vapours
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/20—C2-C4 olefins
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/30—Aromatics
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
- Y02P30/40—Ethylene production
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- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
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| EP13174784.2 | 2013-07-02 | ||
| EP13174784 | 2013-07-02 | ||
| PCT/EP2014/063852 WO2015000844A1 (en) | 2013-07-02 | 2014-06-30 | Method for cracking a hydrocarbon feedstock in a steam cracker unit |
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| KR20160025530A KR20160025530A (ko) | 2016-03-08 |
| KR102309267B1 true KR102309267B1 (ko) | 2021-10-07 |
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| SG (1) | SG11201508917XA (enExample) |
| WO (1) | WO2015000844A1 (enExample) |
Families Citing this family (24)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10167434B2 (en) | 2014-02-25 | 2019-01-01 | Saudi Basic Industries Corporation | Integrated hydrocracking process |
| RU2705590C9 (ru) * | 2014-11-06 | 2019-12-19 | Бипи Европа Се | Способ и устройство для гидроконверсии углеводородов |
| EP3484980A1 (en) * | 2016-07-13 | 2019-05-22 | SABIC Global Technologies B.V. | A process which does simultaneous dehydrochlorination and hydrocracking of pyrolysis oils from mixed plastic pyrolysis while achieving selective hydrodealkylation of c9+ aromatics |
| EP3516012B1 (en) * | 2016-09-22 | 2021-01-06 | SABIC Global Technologies B.V. | An integrated process configuration and apparatus involving the steps of pyrolysis, hydrocracking, hydrodealkylation and steam cracking |
| US10619112B2 (en) | 2016-11-21 | 2020-04-14 | Saudi Arabian Oil Company | Process and system for conversion of crude oil to petrochemicals and fuel products integrating vacuum gas oil hydrotreating and steam cracking |
| US10472579B2 (en) * | 2016-11-21 | 2019-11-12 | Saudi Arabian Oil Company | Process and system for conversion of crude oil to petrochemicals and fuel products integrating vacuum gas oil hydrocracking and steam cracking |
| US11066611B2 (en) | 2016-11-21 | 2021-07-20 | Saudi Arabian Oil Company | System for conversion of crude oil to petrochemicals and fuel products integrating vacuum gas oil hydrotreating and steam cracking |
| US10472574B2 (en) * | 2016-11-21 | 2019-11-12 | Saudi Arabian Oil Company | Process and system for conversion of crude oil to petrochemicals and fuel products integrating delayed coking of vacuum residue |
| US10487275B2 (en) * | 2016-11-21 | 2019-11-26 | Saudi Arabian Oil Company | Process and system for conversion of crude oil to petrochemicals and fuel products integrating vacuum residue conditioning and base oil production |
| US10407630B2 (en) * | 2016-11-21 | 2019-09-10 | Saudi Arabian Oil Company | Process and system for conversion of crude oil to petrochemicals and fuel products integrating solvent deasphalting of vacuum residue |
| US10472580B2 (en) * | 2016-11-21 | 2019-11-12 | Saudi Arabian Oil Company | Process and system for conversion of crude oil to petrochemicals and fuel products integrating steam cracking and conversion of naphtha into chemical rich reformate |
| US10870807B2 (en) | 2016-11-21 | 2020-12-22 | Saudi Arabian Oil Company | 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 |
| 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 |
| US10487276B2 (en) * | 2016-11-21 | 2019-11-26 | Saudi Arabian Oil Company | Process and system for conversion of crude oil to petrochemicals and fuel products integrating vacuum residue hydroprocessing |
| EP3592828B1 (en) | 2017-03-09 | 2021-11-03 | SABIC Global Technologies B.V. | Integration of catalytic cracking process with crude conversion to chemicals process |
| US10899979B2 (en) * | 2017-08-15 | 2021-01-26 | Sabic Global Technologies, B.V. | Light olefin production via an integrated steam cracking and hydrocracking process |
| MY204513A (en) * | 2017-12-29 | 2024-08-31 | Lummus Technology Inc | Conversion of heavy fuel oil to chemicals |
| DE112019004677T5 (de) | 2018-09-19 | 2021-12-30 | Sabic Global Technologies B.V. | AUF ZEOLITHEN GETRÄGERTE BIMETALLISCHE KATALYSATOREN ZUR SELEKTIVEN UMWANDLUNG VON n-BUTAN IN ETHAN |
| WO2020061011A1 (en) | 2018-09-19 | 2020-03-26 | Sabic Global Technologies, B.V. | Selective hydrogenolysis integrated with mtbe production |
| US11827857B2 (en) | 2019-01-29 | 2023-11-28 | Sabic Global Technologies B.V. | Conversion of heavy ends of crude oil or whole crude oil to high value chemicals using a combination of thermal hydroprocessing, hydrotreating with steam crackers under high severity conditions to maximize ethylene, propylene, butenes and benzene |
| EP3918033A1 (en) | 2019-01-29 | 2021-12-08 | SABIC Global Technologies B.V. | Methods and systems for upgrading crude oils, heavy oils, and residues |
| 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 |
| US11384299B2 (en) | 2019-12-19 | 2022-07-12 | Saudi Arabian Oil Company | Systems and processes for upgrading and converting crude oil to petrochemicals through steam cracking |
| CN117625245A (zh) * | 2022-08-17 | 2024-03-01 | 中国石油化工股份有限公司 | 一种劣质催化柴油制备mtbe化工产品的系统及方法 |
Family Cites Families (29)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3172834A (en) * | 1965-03-09 | Process for manufacturing gasoline by blending the hydrocracked gasoline with the dehydrogenated and alkyl- ated products obtained from the hy- drocracking stage | ||
| US2326553A (en) * | 1939-08-26 | 1943-08-10 | Standard Oil Dev Co | Conversion of hydrocarbons |
| US3023158A (en) * | 1960-03-21 | 1962-02-27 | Universal Oil Prod Co | Increasing the yield of gasoline boiling range product from heavy petroleum stocks |
| US3268436A (en) * | 1964-02-25 | 1966-08-23 | Exxon Research Engineering Co | Paraffinic jet fuel by hydrocracking wax |
| US3256176A (en) | 1964-10-21 | 1966-06-14 | Phillips Petroleum Co | Hydrocracking heavy hydrocarbons to gasoline and distillate |
| US3433848A (en) | 1966-08-10 | 1969-03-18 | Texaco Inc | Method of controlling selectivity in an aromatic hydrocarbon dealkylation process |
| US3505205A (en) * | 1968-04-23 | 1970-04-07 | Gulf Research Development Co | Production of lpg by low temperature hydrocracking |
| GB1250615A (enExample) * | 1968-05-02 | 1971-10-20 | ||
| US3617482A (en) * | 1969-11-10 | 1971-11-02 | Chevron Res | Process for the production of lubricating oils |
| BE793036A (fr) * | 1971-12-21 | 1973-04-16 | Pierrefitte Auby Sa | Procede de craquage sous pression d'hydrogene pour la production d'olefines |
| GB1504776A (en) * | 1975-08-14 | 1978-03-22 | Davy Powergas Ltd | Hydrocracking c3 or higher hydrocarbon feedstock |
| FR2364879A1 (fr) * | 1976-09-16 | 1978-04-14 | Inst Francais Du Petrole | Procede de fabrication d'hydrocarbures olefiniques a deux et trois atomes de carbone par molecule |
| 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 |
| US4430103A (en) * | 1982-02-24 | 1984-02-07 | Phillips Petroleum Company | Cryogenic recovery of LPG from natural gas |
| FI852865A7 (fi) | 1984-07-25 | 1986-01-26 | Air Prod & Chem | Parannettu katalyytti hiilivetyjen dehydrausta varten. |
| FI860203A7 (fi) | 1985-01-22 | 1986-07-23 | Air Prod & Chem | Hiilivetyjen dehydroisomerointi. |
| US4789457A (en) | 1985-06-03 | 1988-12-06 | Mobil Oil Corporation | Production of high octane gasoline by hydrocracking catalytic cracking products |
| US4827072A (en) | 1986-06-06 | 1989-05-02 | Uop Inc. | Dehydrogenation catalyst composition and hydrocarbon dehydrogenation process |
| US4926005A (en) | 1989-05-17 | 1990-05-15 | Phillips Petroleum Company | Dehydrogenation process |
| EP0584879B1 (en) | 1992-08-25 | 1997-10-29 | Shell Internationale Researchmaatschappij B.V. | Process for the preparation of lower olefins |
| CA2104044C (en) * | 1992-08-25 | 2004-11-02 | Johan W. Gosselink | Process for the preparation of lower olefins |
| US5880325A (en) | 1993-09-07 | 1999-03-09 | Exxon Research And Engineering Company | Aromatics extraction from hydrocarbon oil using tetramethylene sulfoxide |
| US6217746B1 (en) * | 1999-08-16 | 2001-04-17 | Uop Llc | Two stage hydrocracking process |
| EP1370628A1 (en) * | 2001-03-20 | 2003-12-17 | Uop Llc | Two stage hydrocracking process |
| CN100389179C (zh) * | 2005-04-29 | 2008-05-21 | 中国石油化工股份有限公司 | 一种最大量生产化工原料的加氢裂化方法 |
| US7622623B2 (en) | 2005-09-02 | 2009-11-24 | Sud-Chemie Inc. | Catalytically inactive heat generator and improved dehydrogenation process |
| US7951745B2 (en) | 2008-01-03 | 2011-05-31 | Wilmington Trust Fsb | Catalyst for hydrocracking hydrocarbons containing polynuclear aromatic compounds |
| DE102009012265A1 (de) | 2009-03-11 | 2010-09-23 | Uhde Gmbh | Verfahren zur Gewinnung von Reinaromaten aus aromatenhaltigen Kohlenwasserstofffraktionen |
| WO2012135111A2 (en) | 2011-03-31 | 2012-10-04 | Uop Llc | Aromatics recovery by extractive distillation |
-
2014
- 2014-06-30 CN CN201480034023.2A patent/CN105358660B/zh active Active
- 2014-06-30 WO PCT/EP2014/063852 patent/WO2015000844A1/en not_active Ceased
- 2014-06-30 EP EP14733660.6A patent/EP3017022B1/en active Active
- 2014-06-30 ES ES14733660.6T patent/ES2671782T3/es active Active
- 2014-06-30 KR KR1020157037149A patent/KR102309267B1/ko active Active
- 2014-06-30 EA EA201690117A patent/EA030932B1/ru not_active IP Right Cessation
- 2014-06-30 US US14/902,153 patent/US20160137933A1/en not_active Abandoned
- 2014-06-30 SG SG11201508917XA patent/SG11201508917XA/en unknown
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2019
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Also Published As
| Publication number | Publication date |
|---|---|
| JP2016526594A (ja) | 2016-09-05 |
| KR20160025530A (ko) | 2016-03-08 |
| JP6360554B2 (ja) | 2018-07-18 |
| SG11201508917XA (en) | 2016-01-28 |
| EA201690117A1 (ru) | 2016-06-30 |
| CN105358660A (zh) | 2016-02-24 |
| EP3017022B1 (en) | 2018-03-07 |
| US20160137933A1 (en) | 2016-05-19 |
| EP3017022A1 (en) | 2016-05-11 |
| EA030932B1 (ru) | 2018-10-31 |
| US20190322952A1 (en) | 2019-10-24 |
| WO2015000844A1 (en) | 2015-01-08 |
| CN105358660B (zh) | 2018-06-29 |
| ES2671782T3 (es) | 2018-06-08 |
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