SE7416054L - - Google Patents
Info
- Publication number
- SE7416054L SE7416054L SE7416054A SE7416054A SE7416054L SE 7416054 L SE7416054 L SE 7416054L SE 7416054 A SE7416054 A SE 7416054A SE 7416054 A SE7416054 A SE 7416054A SE 7416054 L SE7416054 L SE 7416054L
- Authority
- SE
- Sweden
- Prior art keywords
- catalyst
- dense bed
- downstream
- coke
- bed
- Prior art date
Links
Classifications
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/12—Oxidising
- B01J37/14—Oxidising with gases containing free oxygen
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
- B01J8/26—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations
-
- 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
- C10G11/182—Regeneration
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Catalysts (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
1486478 Catalyst regeneration UOP INC 19 Dec 1974 [28 Dec 1973 (3)] 54859/74 Heading B1F A catalyst regeneration process comprises introducing spent, coke contaminated catalyst into a coke oxidation zone, e.g. 4, containing a first dense bed of catalyst where coke is oxidised from the catalyst, e.g. at 675-760‹C, passing the resulting catalyst e.g. via 3B to at least one downstream dense bed e.g. 5, which is maintained at a higher temperature than the first dense bed, e.g. 690-800‹C, and recovering regenerated catalyst from the downstream dense bed e.g. via 32, a portion of the regenerated catalyst from the downstream bed being returned to the first dense bed e.g. via 6. without being reused as a catalyst. Specification 1486477 is referred to.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US42942373A | 1973-12-28 | 1973-12-28 | |
| US429421A US3893812A (en) | 1972-05-30 | 1973-12-28 | Regeneration apparatus with external regenerated-catalyst recycle means |
| US05/429,422 US3953175A (en) | 1973-12-28 | 1973-12-28 | Regeneration apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| SE7416054L true SE7416054L (en) | 1975-06-30 |
| SE403573B SE403573B (en) | 1978-08-28 |
Family
ID=27411625
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SE7416054A SE403573B (en) | 1973-12-28 | 1974-12-19 | WAY TO REGENERATE A COOKING CATALYT DISABLED BY COKE COAT |
Country Status (12)
| Country | Link |
|---|---|
| AR (1) | AR207340A1 (en) |
| BR (1) | BR7410887D0 (en) |
| CS (1) | CS216826B2 (en) |
| DE (1) | DE2459879C3 (en) |
| EG (1) | EG11686A (en) |
| FI (1) | FI60403C (en) |
| FR (1) | FR2255948B1 (en) |
| GB (1) | GB1486478A (en) |
| IT (1) | IT1026076B (en) |
| NO (1) | NO142471C (en) |
| PL (1) | PL99780B1 (en) |
| SE (1) | SE403573B (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| IT1115928B (en) * | 1976-03-15 | 1986-02-10 | Uop Inc | APPLIANCE AND REGENERATION PROCEDURE FOR CATALYST CONTAMINATED WITH COKE |
| GB1535797A (en) * | 1976-05-07 | 1978-12-13 | Texaco Development Corp | Fluidized cracking catalyst regeneration process and apparatus |
| DE3006615C2 (en) * | 1980-02-22 | 1986-04-10 | Uop Inc., Des Plaines, Ill. | Method and apparatus for the regeneration of hydrocarbon conversion catalysts |
| US6558531B2 (en) | 2000-04-04 | 2003-05-06 | Exxonmobil Chemical Patents Inc. | Method for maintaining heat balance in a fluidized bed catalytic cracking unit |
-
1974
- 1974-01-01 AR AR257096A patent/AR207340A1/en active
- 1974-12-18 IT IT54641/74A patent/IT1026076B/en active
- 1974-12-18 DE DE2459879A patent/DE2459879C3/en not_active Expired
- 1974-12-18 FI FI3673/74A patent/FI60403C/en active
- 1974-12-19 GB GB54859/74A patent/GB1486478A/en not_active Expired
- 1974-12-19 SE SE7416054A patent/SE403573B/en not_active IP Right Cessation
- 1974-12-20 CS CS748817A patent/CS216826B2/en unknown
- 1974-12-21 EG EG579/74A patent/EG11686A/en active
- 1974-12-23 FR FR7442549A patent/FR2255948B1/fr not_active Expired
- 1974-12-27 BR BR10887/74A patent/BR7410887D0/en unknown
- 1974-12-27 NO NO744700A patent/NO142471C/en unknown
- 1974-12-28 PL PL1974176901A patent/PL99780B1/en unknown
Also Published As
| Publication number | Publication date |
|---|---|
| AR207340A1 (en) | 1976-09-30 |
| NO744700L (en) | 1975-07-28 |
| FI60403C (en) | 1982-01-11 |
| DE2459879B2 (en) | 1977-11-10 |
| BR7410887D0 (en) | 1975-09-02 |
| FR2255948A1 (en) | 1975-07-25 |
| FI60403B (en) | 1981-09-30 |
| FR2255948B1 (en) | 1980-04-04 |
| SE403573B (en) | 1978-08-28 |
| EG11686A (en) | 1978-03-29 |
| DE2459879C3 (en) | 1978-07-27 |
| GB1486478A (en) | 1977-09-21 |
| IT1026076B (en) | 1978-09-20 |
| NO142471B (en) | 1980-05-19 |
| FI367374A (en) | 1975-06-29 |
| CS216826B2 (en) | 1982-11-26 |
| NO142471C (en) | 1980-08-27 |
| PL99780B1 (en) | 1978-08-31 |
| AU7676574A (en) | 1976-06-24 |
| DE2459879A1 (en) | 1975-07-10 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| YU228274A (en) | Process for the regeneration of a molybdenum containing catalyst,used in the oxidization or oxidizing dehydrogenation of propylene in a fluidized bed reactor | |
| SE7416053L (en) | ||
| GB1307782A (en) | Staged regeneration of catalyst | |
| ZA756443B (en) | Process for recovering vanadium from deactivated catalysts | |
| SE7416054L (en) | ||
| IE40048L (en) | Improved process for producing alpha-6- deoxy- tetracyclines. | |
| GB1526490A (en) | Regeneration process for hydrocarbon conversion catalysts | |
| ZA764642B (en) | Process for the regeneration of a solid bed metal phthalocyanine catalyst system | |
| GB1551790A (en) | Process for the recovery of antimony pentachloride from a spent antimony catalyst mixture | |
| JPS52155102A (en) | Process for recovery of valuable metal from spent catalyst | |
| GB1478825A (en) | Process for the production of benzylamine and dibenzylamine | |
| ES8107121A1 (en) | Reactivation of chemical reconversion catalysts used in a cyclic production process of hydrogen peroxide, and use of an apparatus for putting it into practice. | |
| GB1383347A (en) | Method of at least partially removing nitrogen oxides from gases | |
| GB1405309A (en) | Gas purification | |
| US2963443A (en) | Reactivation of molybdenum containing catalysts | |
| CA959239A (en) | Process for the recovery of antimony pentachloride from catalyst solutions | |
| GB1269862A (en) | Process for regenerating a hydrogenation catalyst | |
| JPS52904A (en) | Process for recovering activity of washing liquid for acetylene gas purification | |
| JPS5242490A (en) | Method of regenerating nox-removal catalyst | |
| GB1518530A (en) | Method of initiating essentially complete oxidation of co to co2 in a spent-catalyst regenerating zone | |
| ES415063A1 (en) | Fluidized catalyst regeneration process | |
| JPS5226393A (en) | Method of regenerating vanadium-type catalysts for reductive purificat ion of nox | |
| YU76576A (en) | Process for the regeneration of palladium-cadmium-potassium carrier catalysts | |
| JPS5248609A (en) | Treatment process for product gases from oxidation reaction | |
| JPS5221277A (en) | Method of catalytic reaction and its apparatus |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| NUG | Patent has lapsed |
Ref document number: 7416054-0 Effective date: 19930709 Format of ref document f/p: F |