CN103333714A - 包括具有四个和/或五个碳原子的烯烃的进料的直接转化方法，用于伴有汽油副产品生产的丙烯生产 - Google Patents
包括具有四个和/或五个碳原子的烯烃的进料的直接转化方法，用于伴有汽油副产品生产的丙烯生产 Download PDFInfo
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- CN103333714A CN103333714A CN2013102381291A CN201310238129A CN103333714A CN 103333714 A CN103333714 A CN 103333714A CN 2013102381291 A CN2013102381291 A CN 2013102381291A CN 201310238129 A CN201310238129 A CN 201310238129A CN 103333714 A CN103333714 A CN 103333714A
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Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
- C07C2/02—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons
- C07C2/04—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation
- C07C2/06—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation of alkenes, i.e. acyclic hydrocarbons having only one carbon-to-carbon double bond
- C07C2/08—Catalytic processes
- C07C2/10—Catalytic processes with metal oxides
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C11/00—Aliphatic unsaturated hydrocarbons
- C07C11/02—Alkenes
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C11/00—Aliphatic unsaturated hydrocarbons
- C07C11/02—Alkenes
- C07C11/06—Propene
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C4/00—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
- C07C4/02—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by cracking a single hydrocarbon or a mixture of individually defined hydrocarbons or a normally gaseous hydrocarbon fraction
- C07C4/06—Catalytic processes
-
- 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
- C10G50/00—Production of liquid hydrocarbon mixtures from lower carbon number hydrocarbons, e.g. by oligomerisation
-
- 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
- C10G69/12—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 polymerisation or alkylation step
-
- 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
- C10G69/12—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 polymerisation or alkylation step
- C10G69/126—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 polymerisation or alkylation step polymerisation, e.g. oligomerisation
-
- 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
- C10G2400/02—Gasoline
-
- 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
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR0413680A FR2879620B1 (fr) | 2004-12-21 | 2004-12-21 | Procede de conversion directe d'une charge comprenant des olefines a quatre et/ou cinq atomes de carbone, pour la production de propylene avec une co-production d'essence |
| FR0413680 | 2004-12-21 |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNA2005800437597A Division CN101084291A (zh) | 2004-12-21 | 2005-12-13 | 包括具有四个和/或五个碳原子的烯烃的进料的直接转化方法，用于伴有汽油副产品生产的丙烯生产 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103333714A true CN103333714A (zh) | 2013-10-02 |
Family
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Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNA2005800437597A Pending CN101084291A (zh) | 2004-12-21 | 2005-12-13 | 包括具有四个和/或五个碳原子的烯烃的进料的直接转化方法，用于伴有汽油副产品生产的丙烯生产 |
| CN2013102381291A Pending CN103333714A (zh) | 2004-12-21 | 2005-12-13 | 包括具有四个和/或五个碳原子的烯烃的进料的直接转化方法，用于伴有汽油副产品生产的丙烯生产 |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNA2005800437597A Pending CN101084291A (zh) | 2004-12-21 | 2005-12-13 | 包括具有四个和/或五个碳原子的烯烃的进料的直接转化方法，用于伴有汽油副产品生产的丙烯生产 |
Country Status (7)
| Country | Link |
|---|---|
| US (1) | US9193922B2 (enExample) |
| JP (1) | JP5140819B2 (enExample) |
| CN (2) | CN101084291A (enExample) |
| DE (1) | DE112005003177B4 (enExample) |
| FR (1) | FR2879620B1 (enExample) |
| GB (1) | GB2437203B (enExample) |
| WO (1) | WO2006067305A1 (enExample) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2020192490A1 (zh) | 2019-03-22 | 2020-10-01 | 中国石油化工股份有限公司 | 一种多产丙烯的催化转化方法和系统 |
Families Citing this family (32)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2892126B1 (fr) * | 2005-10-19 | 2010-04-30 | Inst Francais Du Petrole | Procede de conversion directe d'une charge comprenant des olefines a quatre, et/ou cinq atomes de carbone, pour la production de propylene avec une co-production d'essence desulfuree |
| FR2905122B1 (fr) * | 2006-08-24 | 2009-07-24 | Inst Francais Du Petrole | Procede de production de propylene en presence d'un catalyseur macroporeux se presentant sous forme de billes spheriques |
| JP5023637B2 (ja) * | 2006-09-27 | 2012-09-12 | 三菱化学株式会社 | プロピレンの製造方法 |
| FR2942796B1 (fr) * | 2009-03-09 | 2011-05-27 | Inst Francais Du Petrole | Procede de conversion directe d'une charge comprenant des olefines a quatre et/ou cinq atomes de carbone pour la production de propylene |
| EP2404980A1 (en) * | 2010-07-08 | 2012-01-11 | Total Raffinage Marketing | Hydrocarbon feedstock average molecular weight increase |
| KR20140019318A (ko) | 2010-12-28 | 2014-02-14 | 토탈 라피나쥬 마케팅 | 니트릴 함유 탄화수소 공급원료, 이의 제조방법 및 용도 |
| CN102517073B (zh) * | 2011-12-09 | 2014-07-23 | 大庆华科股份有限公司 | 一种裂解碳五分离工艺中采用精馏和加氢耦合脱除碳四的方法 |
| FR2984916B1 (fr) * | 2011-12-23 | 2014-01-17 | IFP Energies Nouvelles | Procede ameliore de conversion d'une charge lourde en distillat moyen faisant appel a un pretraitement en amont de l'unite de craquage catalytique |
| WO2013104614A1 (en) | 2012-01-09 | 2013-07-18 | Total Raffinage Marketing | Method for the conversion of low boiling point olefin containing hydrocarbon feedstock |
| FR2986799B1 (fr) * | 2012-02-15 | 2015-02-06 | IFP Energies Nouvelles | Procede de conversion d'une charge lourde, mettant en oeuvre une unite de craquage catalytique et une etape d'hydrogenation selective de l'essence issue du craquage catalytique |
| US10508064B2 (en) * | 2012-11-12 | 2019-12-17 | Uop Llc | Process for oligomerizing gasoline without further upgrading |
| US9522375B2 (en) | 2012-11-12 | 2016-12-20 | Uop Llc | Apparatus for fluid catalytic cracking oligomerate |
| US9663415B2 (en) | 2012-11-12 | 2017-05-30 | Uop Llc | Process for making diesel by oligomerization of gasoline |
| US9567267B2 (en) * | 2012-11-12 | 2017-02-14 | Uop Llc | Process for oligomerizing light olefins including pentenes |
| US9434891B2 (en) | 2012-11-12 | 2016-09-06 | Uop Llc | Apparatus for recovering oligomerate |
| US9914673B2 (en) | 2012-11-12 | 2018-03-13 | Uop Llc | Process for oligomerizing light olefins |
| US9522373B2 (en) | 2012-11-12 | 2016-12-20 | Uop Llc | Apparatus for oligomerizing light olefins |
| US9441173B2 (en) | 2012-11-12 | 2016-09-13 | Uop Llc | Process for making diesel by oligomerization |
| US9644159B2 (en) | 2012-11-12 | 2017-05-09 | Uop Llc | Composition of oligomerate |
| US9278893B2 (en) | 2012-11-12 | 2016-03-08 | Uop Llc | Process for making gasoline by oligomerization |
| US9834492B2 (en) * | 2012-11-12 | 2017-12-05 | Uop Llc | Process for fluid catalytic cracking oligomerate |
| US9670425B2 (en) | 2013-12-17 | 2017-06-06 | Uop Llc | Process for oligomerizing and cracking to make propylene and aromatics |
| US9732285B2 (en) | 2013-12-17 | 2017-08-15 | Uop Llc | Process for oligomerization of gasoline to make diesel |
| JP2015218312A (ja) * | 2014-05-20 | 2015-12-07 | Ｊｘ日鉱日石エネルギー株式会社 | オレフィンを含む炭化水素混合物の脱硫方法 |
| US10544068B2 (en) | 2016-08-16 | 2020-01-28 | Iran Polymer And Petrochemical Institute | Catalytic process for producing olefins |
| US10745328B2 (en) * | 2018-03-27 | 2020-08-18 | Phillips 66 Company | Catalytic activation and oligomerization of isopentane-enriched mixtures |
| US10774017B2 (en) * | 2018-03-27 | 2020-09-15 | Phillips 66 Company | Catalytic activation of isopentane-enriched mixtures |
| US10815438B2 (en) * | 2018-03-27 | 2020-10-27 | Phillips 66 Company | Catalytic activation and alkylation of isopentane-enriched mixtures |
| WO2020058904A1 (en) | 2018-09-20 | 2020-03-26 | Sabic Global Technologies B.V. | A process for producing light olefins (ethylene + propylene) and btx using a mixed paraffinic c 4 feed |
| US10870808B2 (en) * | 2019-04-24 | 2020-12-22 | Phillips 66 Company | Isomerization and catalytic activation of pentane-enriched hydrocarbon mixtures |
| US10865168B2 (en) * | 2019-04-24 | 2020-12-15 | Phillips 66 Company | Isomerization, catalytic activation and oligomerization of pentane-enriched hydrocarbon mixtures |
| CN114456025B (zh) * | 2020-10-21 | 2024-05-28 | 中国石油化工股份有限公司 | 一种催化轻汽油生产乙烯丙烯的方法和系统 |
Family Cites Families (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2492365B1 (fr) * | 1980-10-16 | 1986-02-28 | Inst Francais Du Petrole | Procede de valorisation des coupes c4 olefiniques |
| DE3372474D1 (en) * | 1982-11-10 | 1987-08-20 | Montedipe Spa | Process for converting olefins having 4 to 12 carbon atoms into propylene |
| FR2603895B1 (fr) * | 1986-09-15 | 1989-09-01 | Inst Francais Du Petrole | Procede d'obtention de supercarburant a partir des butanes et/ou des coupes a quatre atomes de carbone issus d'un craquage ou d'un reformage catalytique |
| US4795844A (en) * | 1987-07-20 | 1989-01-03 | Uop Inc. | Process for conversion of light olefins to LPG and aromatics |
| FR2755958B1 (fr) * | 1996-11-19 | 1999-01-08 | Inst Francais Du Petrole | Zeolithe nu-86 desaluminee et son utilisation en conversion des hydrocarbures |
| US6049017A (en) * | 1998-04-13 | 2000-04-11 | Uop Llc | Enhanced light olefin production |
| IT1318527B1 (it) * | 2000-05-19 | 2003-08-27 | Enichem Spa | Procedimento per la produzione di propilene da correnti olefiniche. |
| FR2810991B1 (fr) * | 2000-06-28 | 2004-07-09 | Inst Francais Du Petrole | Procede pour l'hydrogenation de coupes contenant des hydrocarbures et notamment des molecules insaturees contenant au moins deux doubles liaisons ou au moins une triple liaison |
| EP1195424A1 (en) * | 2000-10-05 | 2002-04-10 | ATOFINA Research | A process for cracking an olefin-rich hydrocarbon feedstock |
| FR2837199B1 (fr) | 2002-03-15 | 2005-09-16 | Inst Francais Du Petrole | Procede de conversion en plusieurs etapes d'une charge comprenant des olefines a quatre, cinq atomes de carbone ou plus, en vue de produire du propylene |
| EP1388528B1 (de) * | 2002-08-06 | 2015-04-08 | Evonik Degussa GmbH | Verfahren zur Oligomerisierung von Isobuten in n-Buten-haltigen Kohlenwasserstoffströmen |
| US6867341B1 (en) | 2002-09-17 | 2005-03-15 | Uop Llc | Catalytic naphtha cracking catalyst and process |
| FR2859994B1 (fr) * | 2003-09-19 | 2005-10-28 | Inst Francais Du Petrole | Procede de conversion directe d'une charge comprenant des olefines a quatre, et/ou cinq atomes de carbone ou plus, pour la production de propylene |
-
2004
- 2004-12-21 FR FR0413680A patent/FR2879620B1/fr not_active Expired - Lifetime
-
2005
- 2005-12-13 CN CNA2005800437597A patent/CN101084291A/zh active Pending
- 2005-12-13 WO PCT/FR2005/003141 patent/WO2006067305A1/fr not_active Ceased
- 2005-12-13 US US11/722,300 patent/US9193922B2/en active Active
- 2005-12-13 DE DE112005003177.2T patent/DE112005003177B4/de not_active Expired - Fee Related
- 2005-12-13 CN CN2013102381291A patent/CN103333714A/zh active Pending
- 2005-12-13 GB GB0713207A patent/GB2437203B/en not_active Expired - Fee Related
- 2005-12-13 JP JP2007547561A patent/JP5140819B2/ja not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2020192490A1 (zh) | 2019-03-22 | 2020-10-01 | 中国石油化工股份有限公司 | 一种多产丙烯的催化转化方法和系统 |
| US12180148B2 (en) | 2019-03-22 | 2024-12-31 | China Petroleum & Chemical Corporation | Catalytic conversion process and system with increased propylene production |
Also Published As
| Publication number | Publication date |
|---|---|
| DE112005003177B4 (de) | 2016-03-10 |
| JP2008524421A (ja) | 2008-07-10 |
| US20100036182A1 (en) | 2010-02-11 |
| JP5140819B2 (ja) | 2013-02-13 |
| FR2879620A1 (fr) | 2006-06-23 |
| GB2437203A (en) | 2007-10-17 |
| DE112005003177T5 (de) | 2008-01-24 |
| US9193922B2 (en) | 2015-11-24 |
| FR2879620B1 (fr) | 2007-02-23 |
| WO2006067305A1 (fr) | 2006-06-29 |
| GB2437203B (en) | 2009-07-08 |
| CN101084291A (zh) | 2007-12-05 |
| GB0713207D0 (en) | 2007-08-15 |
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