FR2754826B1 - Procede d'hydrocraquage doux de coupes petrolieres avec un catalyseur contenant au moins deux zeolithes y desaluminees - Google Patents
Procede d'hydrocraquage doux de coupes petrolieres avec un catalyseur contenant au moins deux zeolithes y desalumineesInfo
- Publication number
- FR2754826B1 FR2754826B1 FR9612958A FR9612958A FR2754826B1 FR 2754826 B1 FR2754826 B1 FR 2754826B1 FR 9612958 A FR9612958 A FR 9612958A FR 9612958 A FR9612958 A FR 9612958A FR 2754826 B1 FR2754826 B1 FR 2754826B1
- Authority
- FR
- France
- Prior art keywords
- desaluminated
- zeoliths
- catalyst containing
- oil cuttings
- soft hydrocracking
- 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.)
- Expired - Lifetime
Links
- 239000003054 catalyst Substances 0.000 title 1
- 238000004517 catalytic hydrocracking Methods 0.000 title 1
- 238000000034 method Methods 0.000 title 1
Classifications
-
- 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
- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
- C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
- C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
- C10G45/12—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing crystalline alumino-silicates, e.g. molecular sieves
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/80—Mixtures of different zeolites
-
- 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
- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
- C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
- C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
- C10G45/06—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
- C10G45/08—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof in combination with chromium, molybdenum, or tungsten metals, or compounds thereof
-
- 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
- C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
- C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
- C10G47/10—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
- C10G47/12—Inorganic carriers
- C10G47/16—Crystalline alumino-silicate carriers
-
- 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
- C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
- C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
- C10G47/10—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
- C10G47/12—Inorganic carriers
- C10G47/16—Crystalline alumino-silicate carriers
- C10G47/20—Crystalline alumino-silicate carriers the catalyst containing other metals or compounds thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/10—After treatment, characterised by the effect to be obtained
- B01J2229/16—After treatment, characterised by the effect to be obtained to increase the Si/Al ratio; Dealumination
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/10—After treatment, characterised by the effect to be obtained
- B01J2229/26—After treatment, characterised by the effect to be obtained to stabilize the total catalyst structure
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/30—After treatment, characterised by the means used
- B01J2229/42—Addition of matrix or binder particles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
- B01J29/084—Y-type faujasite
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/40—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively
-
- 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/4006—Temperature
-
- 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/4012—Pressure
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Crystallography & Structural Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Materials Engineering (AREA)
- Catalysts (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Priority Applications (8)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR9612958A FR2754826B1 (fr) | 1996-10-22 | 1996-10-22 | Procede d'hydrocraquage doux de coupes petrolieres avec un catalyseur contenant au moins deux zeolithes y desaluminees |
| ES97402445T ES2175301T3 (es) | 1996-10-22 | 1997-10-16 | Procedimiento para la hidroconversion suave de fracciones petroleras con un catalizador que comprende al menos dos zeolitas y desaluminadas. |
| EP97402445A EP0838516B1 (fr) | 1996-10-22 | 1997-10-16 | Procédé d'hydrocraquage doux de coupes pétrolières avec un catalyseur contenant au moins deux zeolithes y desaluminées |
| DE69711804T DE69711804T2 (de) | 1996-10-22 | 1997-10-16 | Mildes hydrokracken von Erdölfraktionen unter Verwendung eines zwei dealuminierte Y-Zeolithen enthaltende Katalysators |
| US08/955,623 US5954947A (en) | 1996-10-22 | 1997-10-22 | Process for mild hydrocracking of petroleum cuts using a catalyst containing at least two dealuminated Y zeolites |
| JP28975997A JP3994237B2 (ja) | 1996-10-22 | 1997-10-22 | 脱アルミニウム化された少なくとも2つのゼオライトyを含む触媒を用いる石油留分の温和な水素化クラッキング方法 |
| KR1019970054126A KR100504448B1 (ko) | 1996-10-22 | 1997-10-22 | 탈알루미네이트화된2이상의y제올라이트를포함하는촉매를사용한석유유분의온화한수소분해증류방법 |
| BR9705240A BR9705240A (pt) | 1996-10-22 | 1997-10-22 | Processo de hidrocraqueamento doce de cortes petrolíferos com um catalisador que contém pelo menos dois zeólitos y desaluminados |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR9612958A FR2754826B1 (fr) | 1996-10-22 | 1996-10-22 | Procede d'hydrocraquage doux de coupes petrolieres avec un catalyseur contenant au moins deux zeolithes y desaluminees |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| FR2754826A1 FR2754826A1 (fr) | 1998-04-24 |
| FR2754826B1 true FR2754826B1 (fr) | 1998-12-11 |
Family
ID=9496974
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| FR9612958A Expired - Lifetime FR2754826B1 (fr) | 1996-10-22 | 1996-10-22 | Procede d'hydrocraquage doux de coupes petrolieres avec un catalyseur contenant au moins deux zeolithes y desaluminees |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US5954947A (enExample) |
| EP (1) | EP0838516B1 (enExample) |
| JP (1) | JP3994237B2 (enExample) |
| KR (1) | KR100504448B1 (enExample) |
| BR (1) | BR9705240A (enExample) |
| DE (1) | DE69711804T2 (enExample) |
| ES (1) | ES2175301T3 (enExample) |
| FR (1) | FR2754826B1 (enExample) |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2777290B1 (fr) * | 1998-04-09 | 2000-05-12 | Inst Francais Du Petrole | Procede d'amelioration de l'indice de cetane d'une coupe gasoil |
| CN1096296C (zh) | 1998-11-13 | 2002-12-18 | 中国石油化工集团公司 | 一种生产中间馏分油的加氢裂化催化剂及其制备 |
| US20020144928A1 (en) * | 2001-01-29 | 2002-10-10 | Bronshtein Alexander P. | Energy efficient process for converting refinery and petroleum-based waste to standard fuels |
| US7611689B2 (en) * | 2004-09-24 | 2009-11-03 | Shell Oil Company | Faujasite zeolite, its preparation and use in hydrocracking |
| CN101468317B (zh) * | 2007-12-25 | 2011-01-19 | 中国石油化工股份有限公司 | 一种加氢裂化催化剂及其制备方法 |
| US20090272674A1 (en) * | 2008-04-30 | 2009-11-05 | Ying Zheng | Nano zeolite containing hydrotreating catalyst and method of preparation |
| JP5940935B2 (ja) * | 2012-08-17 | 2016-06-29 | 日揮触媒化成株式会社 | 炭化水素接触分解用触媒 |
| US10603657B2 (en) | 2016-04-11 | 2020-03-31 | Saudi Arabian Oil Company | Nano-sized zeolite supported catalysts and methods for their production |
| US11084992B2 (en) | 2016-06-02 | 2021-08-10 | Saudi Arabian Oil Company | Systems and methods for upgrading heavy oils |
| US10301556B2 (en) | 2016-08-24 | 2019-05-28 | Saudi Arabian Oil Company | Systems and methods for the conversion of feedstock hydrocarbons to petrochemical products |
| US10689587B2 (en) | 2017-04-26 | 2020-06-23 | Saudi Arabian Oil Company | Systems and processes for conversion of crude oil |
| JP2020527638A (ja) | 2017-07-17 | 2020-09-10 | サウジ アラビアン オイル カンパニーSaudi Arabian Oil Company | 油アップグレードに続く蒸気分解により重質油を処理するためのシステムおよび方法 |
Family Cites Families (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA964255A (en) * | 1970-12-23 | 1975-03-11 | Geoffrey E. Dolbear | Cracking catalyst containing nickel and magnesium exchanged zeolites |
| US3830725A (en) * | 1970-12-23 | 1974-08-20 | Grace W R & Co | Cracking hydrocarbons with catalysts containing nickel and magnesium exchanged zeolites |
| CA1046484A (en) * | 1976-04-12 | 1979-01-16 | Elroy M. Gladrow | Hydrocarbon conversion catalyst containing a co oxidation promoter |
| US4097410A (en) * | 1976-06-23 | 1978-06-27 | Exxon Research & Engineering Co. | Hydrocarbon conversion catalyst containing a CO oxidation promoter |
| US4477336A (en) * | 1982-03-02 | 1984-10-16 | Harshaw/Filtrol Partnership | Acid dealuminated Y-zeolite and cracking process employing the same |
| EP0287718B1 (en) * | 1987-04-21 | 1991-03-06 | Uop | Middle distillate - producing hydrocracking catalyst |
| US4661239A (en) * | 1985-07-02 | 1987-04-28 | Uop Inc. | Middle distillate producing hydrocracking process |
| KR900004505B1 (ko) * | 1987-04-27 | 1990-06-28 | 유오피 인코오포레이티드 | 중간유분을 생성하는 수소화 크래킹 촉매 |
| US4925546A (en) * | 1989-09-12 | 1990-05-15 | Amoco Corporation | Hydrocracking process |
| US5275720A (en) * | 1990-11-30 | 1994-01-04 | Union Oil Company Of California | Gasoline hydrocracking catalyst and process |
| CA2143893C (en) * | 1994-03-07 | 2000-11-14 | Nicolaas Van Dijk | Process for the hydrocracking of a hydrocarbonaceous feedstock |
| FR2754742B1 (fr) * | 1996-10-22 | 1998-12-11 | Inst Francais Du Petrole | Catalyseur contenant au moins deux zeolithes y desaluminees et procede d'hydroconversion conventionnelle de coupes petrolieres avec ce catalyseur |
-
1996
- 1996-10-22 FR FR9612958A patent/FR2754826B1/fr not_active Expired - Lifetime
-
1997
- 1997-10-16 EP EP97402445A patent/EP0838516B1/fr not_active Expired - Lifetime
- 1997-10-16 DE DE69711804T patent/DE69711804T2/de not_active Expired - Lifetime
- 1997-10-16 ES ES97402445T patent/ES2175301T3/es not_active Expired - Lifetime
- 1997-10-22 BR BR9705240A patent/BR9705240A/pt not_active IP Right Cessation
- 1997-10-22 JP JP28975997A patent/JP3994237B2/ja not_active Expired - Fee Related
- 1997-10-22 US US08/955,623 patent/US5954947A/en not_active Expired - Lifetime
- 1997-10-22 KR KR1019970054126A patent/KR100504448B1/ko not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JP3994237B2 (ja) | 2007-10-17 |
| KR19980033043A (ko) | 1998-07-25 |
| US5954947A (en) | 1999-09-21 |
| EP0838516A1 (fr) | 1998-04-29 |
| JPH10130661A (ja) | 1998-05-19 |
| DE69711804T2 (de) | 2002-08-08 |
| ES2175301T3 (es) | 2002-11-16 |
| EP0838516B1 (fr) | 2002-04-10 |
| KR100504448B1 (ko) | 2005-10-31 |
| BR9705240A (pt) | 1999-05-25 |
| DE69711804D1 (de) | 2002-05-16 |
| FR2754826A1 (fr) | 1998-04-24 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| CD | Change of name or company name | ||
| PLFP | Fee payment |
Year of fee payment: 20 |