FR2608623B1 - METHOD AND APPARATUS FOR CATALYTIC CRACKING OF A HYDROCARBON CHARGE IN A REACTIONAL AREA WHERE SUBSTANTIALLY INERT SOLIDS PARTICLES AND CATALYTIC PARTICLES ARE MOVING - Google Patents
METHOD AND APPARATUS FOR CATALYTIC CRACKING OF A HYDROCARBON CHARGE IN A REACTIONAL AREA WHERE SUBSTANTIALLY INERT SOLIDS PARTICLES AND CATALYTIC PARTICLES ARE MOVINGInfo
- Publication number
- FR2608623B1 FR2608623B1 FR8617787A FR8617787A FR2608623B1 FR 2608623 B1 FR2608623 B1 FR 2608623B1 FR 8617787 A FR8617787 A FR 8617787A FR 8617787 A FR8617787 A FR 8617787A FR 2608623 B1 FR2608623 B1 FR 2608623B1
- Authority
- FR
- France
- Prior art keywords
- particles
- catalytic
- zone
- cracking
- substantially inert
- 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
Links
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
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
- C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
Abstract
According to the process, the feedstock and a first mixture of a major part of substantially inert solid particles originating from the line (4) are introduced into a vaporisation zone (1a) at a temperature T'2 of between 650 DEG C and 1200 DEG C, the feedstock and the first mixture of solid particles are caused to flow into a stream of carrier gas and a second stage of a major part of catalyst particles of smaller particle size and lower density originating from the line (6) is introduced into a cracking zone (1b) continuous with the vaporisation zone, at a temperature T'1 of between 300 and 750 DEG C, lower than T'2; the resulting mixture is circulated countercurrentwise in the cracking zone (1b), the cracking effluents and the solid and catalyst particles are recovered (9), the said effluents are separated from the said particles, the said particles are separated off (13a) and regenerated, an inert solid particle fraction and a catalyst particle fraction are recovered separately and are recycled into the vaporisation zone and into the cracking zone respectively. Application in the oil industry.
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR8617787A FR2608623B1 (en) | 1986-12-17 | 1986-12-17 | METHOD AND APPARATUS FOR CATALYTIC CRACKING OF A HYDROCARBON CHARGE IN A REACTIONAL AREA WHERE SUBSTANTIALLY INERT SOLIDS PARTICLES AND CATALYTIC PARTICLES ARE MOVING |
EP87402781A EP0272973B1 (en) | 1986-12-17 | 1987-12-08 | Process and apparatus for the catalytic cracking of a hydrocarbonaceous food in a reaction zone in which circulate substantially inert and catalytic particles |
AT87402781T ATE64408T1 (en) | 1986-12-17 | 1987-12-08 | PROCESS AND APPARATUS FOR THE CATALYTIC CRACKING OF HYDROCARBON FEED IN A TRANSFORMATION ZONE WHERE INERT AND CATALYTIC PARTICLES CIRCULATE. |
DE8787402781T DE3770789D1 (en) | 1986-12-17 | 1987-12-08 | METHOD AND DEVICE FOR THE CATALYTIC CRACKING OF HYDROCARBON INSERTS IN A CONVERSION ZONE, IN WHICH CIRCULATE INERT AND CATALYTIC PARTICLES. |
JP62321129A JPS63165484A (en) | 1986-12-17 | 1987-12-17 | Method and apparatus for catalytic cracking of hydrocarbon charge raw material in reaction zone through which extremely inert solid particle and catalyst particle flow |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR8617787A FR2608623B1 (en) | 1986-12-17 | 1986-12-17 | METHOD AND APPARATUS FOR CATALYTIC CRACKING OF A HYDROCARBON CHARGE IN A REACTIONAL AREA WHERE SUBSTANTIALLY INERT SOLIDS PARTICLES AND CATALYTIC PARTICLES ARE MOVING |
Publications (2)
Publication Number | Publication Date |
---|---|
FR2608623A1 FR2608623A1 (en) | 1988-06-24 |
FR2608623B1 true FR2608623B1 (en) | 1989-10-27 |
Family
ID=9342071
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
FR8617787A Expired FR2608623B1 (en) | 1986-12-17 | 1986-12-17 | METHOD AND APPARATUS FOR CATALYTIC CRACKING OF A HYDROCARBON CHARGE IN A REACTIONAL AREA WHERE SUBSTANTIALLY INERT SOLIDS PARTICLES AND CATALYTIC PARTICLES ARE MOVING |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP0272973B1 (en) |
JP (1) | JPS63165484A (en) |
AT (1) | ATE64408T1 (en) |
DE (1) | DE3770789D1 (en) |
FR (1) | FR2608623B1 (en) |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4810360A (en) * | 1984-11-02 | 1989-03-07 | Mobil Oil Corp. | Method and apparatus for withdrawal of small catalyst particles in FCC systems |
US4895637A (en) * | 1988-10-18 | 1990-01-23 | Mobil Oil Corporation | Resid cracking process and apparatus |
CA2013626A1 (en) * | 1989-05-16 | 1990-11-16 | W. Benedict Johnson | Method and apparatus for the fluid catalytic cracking of hydrocarbon feed employing a separable mixture of catalyst and sorbent particles |
AU777436B2 (en) * | 1998-12-21 | 2004-10-14 | Indian Oil Corporation Limited | A fluidized catalytic cracking (FCC) process |
EP1013743B1 (en) * | 1998-12-21 | 2005-02-02 | INDIAN OIL CORPORATION Ltd. | A fluid catalytic cracking (FCC) process |
EP1046696B1 (en) * | 1999-04-23 | 2014-06-11 | China Petrochemical Corporation | A catalytic conversion process for producing isobutane and isoparaffin-enriched gasoline |
DE10219863B4 (en) * | 2002-05-03 | 2014-03-27 | Indian Oil Corporation Limited | Residue cracker with catalyst and adsorbent regenerators and method therefor |
KR102305664B1 (en) * | 2016-09-16 | 2021-09-28 | 루머스 테크놀로지 엘엘씨 | Fluid Catalytic Cracking Process and Apparatus and Other Applications to Maximize Light Olefin Yields |
US10758883B2 (en) | 2016-09-16 | 2020-09-01 | Lummus Technology Llc | Fluid catalytic cracking process and apparatus for maximizing light olefin yield and other applications |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3380911A (en) * | 1966-02-15 | 1968-04-30 | Mobil Oil Corp | Method for converting hydrocarbons in two stages |
US4243514A (en) * | 1979-05-14 | 1981-01-06 | Engelhard Minerals & Chemicals Corporation | Preparation of FCC charge from residual fractions |
US4490241A (en) * | 1983-04-26 | 1984-12-25 | Mobil Oil Corporation | Secondary injection of ZSM-5 type zeolite in catalytic cracking |
-
1986
- 1986-12-17 FR FR8617787A patent/FR2608623B1/en not_active Expired
-
1987
- 1987-12-08 AT AT87402781T patent/ATE64408T1/en not_active IP Right Cessation
- 1987-12-08 DE DE8787402781T patent/DE3770789D1/en not_active Expired - Fee Related
- 1987-12-08 EP EP87402781A patent/EP0272973B1/en not_active Expired - Lifetime
- 1987-12-17 JP JP62321129A patent/JPS63165484A/en active Pending
Also Published As
Publication number | Publication date |
---|---|
DE3770789D1 (en) | 1991-07-18 |
EP0272973B1 (en) | 1991-06-12 |
EP0272973A1 (en) | 1988-06-29 |
ATE64408T1 (en) | 1991-06-15 |
FR2608623A1 (en) | 1988-06-24 |
JPS63165484A (en) | 1988-07-08 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
ST | Notification of lapse |