ES443768A1 - Regeneration of cracking catalyst - Google Patents
Regeneration of cracking catalystInfo
- Publication number
- ES443768A1 ES443768A1 ES443768A ES443768A ES443768A1 ES 443768 A1 ES443768 A1 ES 443768A1 ES 443768 A ES443768 A ES 443768A ES 443768 A ES443768 A ES 443768A ES 443768 A1 ES443768 A1 ES 443768A1
- Authority
- ES
- Spain
- Prior art keywords
- catalyst
- regeneration zone
- coke
- phase
- regeneration
- 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
- C10G11/182—Regeneration
-
- 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
- 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
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Combustion & Propulsion (AREA)
- General Chemical & Material Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
Abstract
A process for the regeneration of a coke-contaminated fluidizable catalytic cracking catalyst, which has been partially deactivated by carbonaceous deposits, and which consists of continuously introducing the coke-contaminated catalyst into a dense catalyst phase of a regeneration zone comprising a single fluidized dense phase of catalyst in the lower section of the regeneration zone, maintained at a temperature sufficient to allow combustion of carbonaceous deposits, and a diluted phase in the upper section of the regeneration zone, to bring the contaminated catalyst into contact of coke in the regeneration zone with an upstream stream of regeneration gas containing oxygen thereby combusting the carbonaceous deposits of the contaminated coke catalyst, recovering a flue gas containing carbon monoxide and recovering a regenerated catalyst with contamination reduced from coke, whose procedure is characterized by: a) maintaining the fluidized dense phase of catalyst in the regeneration zone at a temperature of approximately between 1275ºF (690ºC) and 1350ºF (732ºC); b) keeping the catalyst in the dense fluidized catalyst phase of the regeneration zone for a residence time of about 3 to 10 minutes and c) contacting the contaminated coke catalyst in the regeneration zone with an upstream of regenerating gas containing oxygen in excess of that required to effect combustion of the coke to carbon dioxide and to provide about 1 at 10 mole percent oxygen in the stack gas, to thereby recover a stack gas from the regeneration zone containing carbon monoxide in a ratio of the order of 0 to 500 ppm, recover a regenerated catalyst from the dense phase fluidized catalyst from the regeneration zone with a carbon content of not more than about 0.15% by weight and maintaining the dilute phase of catalyst from the regeneration zone at a temperature of approximately between 1375ºF (746ºC) and 1455ºF (790ºC)). (Machine-translation by Google Translate, not legally binding)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US53527074A | 1974-12-23 | 1974-12-23 |
Publications (1)
Publication Number | Publication Date |
---|---|
ES443768A1 true ES443768A1 (en) | 1977-04-16 |
Family
ID=24133518
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ES443768A Expired ES443768A1 (en) | 1974-12-23 | 1975-12-22 | Regeneration of cracking catalyst |
Country Status (22)
Country | Link |
---|---|
JP (1) | JPS5188491A (en) |
AR (1) | AR218610A1 (en) |
AT (1) | AT346818B (en) |
AU (1) | AU496807B2 (en) |
BE (1) | BE836902A (en) |
BR (1) | BR7508454A (en) |
CA (1) | CA1046483A (en) |
CS (1) | CS193485B2 (en) |
DE (1) | DE2553025A1 (en) |
ES (1) | ES443768A1 (en) |
FI (1) | FI753609A (en) |
FR (1) | FR2295794A1 (en) |
GB (1) | GB1526295A (en) |
HU (1) | HU178762B (en) |
IT (1) | IT1059546B (en) |
MX (1) | MX3358E (en) |
NL (1) | NL7514815A (en) |
NO (1) | NO146975C (en) |
PH (1) | PH13098A (en) |
SE (1) | SE427426B (en) |
YU (1) | YU39955B (en) |
ZA (1) | ZA757672B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2627187B1 (en) * | 1988-02-15 | 1993-01-22 | Inst Francais Du Petrole | FLUID CRACKING PROCESS OF A HYDROCARBON LOAD |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE792165A (en) * | 1971-11-30 | 1973-05-30 | Standard Oil Co | PERFECTED PROCESS OF CATALYTIC CRACKING WITH SENSITIVELY COMPLETE COMBUSTION OF CARBON MONOXIDE DURING CATALYST REGENERATION |
JPS4951195A (en) * | 1973-05-30 | 1974-05-17 |
-
1975
- 1975-11-26 DE DE19752553025 patent/DE2553025A1/en not_active Withdrawn
- 1975-12-05 GB GB49955/75A patent/GB1526295A/en not_active Expired
- 1975-12-08 ZA ZA757672A patent/ZA757672B/en unknown
- 1975-12-10 NO NO754189A patent/NO146975C/en unknown
- 1975-12-11 SE SE7513988A patent/SE427426B/en unknown
- 1975-12-17 MX MX006855U patent/MX3358E/en unknown
- 1975-12-18 AT AT962275A patent/AT346818B/en not_active IP Right Cessation
- 1975-12-18 YU YU3235/75A patent/YU39955B/en unknown
- 1975-12-18 PH PH17888A patent/PH13098A/en unknown
- 1975-12-19 NL NL7514815A patent/NL7514815A/en not_active Application Discontinuation
- 1975-12-19 BR BR7508454*A patent/BR7508454A/en unknown
- 1975-12-19 FI FI753609A patent/FI753609A/fi not_active Application Discontinuation
- 1975-12-19 BE BE162969A patent/BE836902A/en not_active IP Right Cessation
- 1975-12-19 FR FR7538999A patent/FR2295794A1/en active Granted
- 1975-12-22 HU HU75TE847A patent/HU178762B/en not_active IP Right Cessation
- 1975-12-22 CS CS758751A patent/CS193485B2/en unknown
- 1975-12-22 AU AU87771/75A patent/AU496807B2/en not_active Expired
- 1975-12-22 ES ES443768A patent/ES443768A1/en not_active Expired
- 1975-12-22 JP JP50152037A patent/JPS5188491A/ja active Pending
- 1975-12-22 CA CA242,249A patent/CA1046483A/en not_active Expired
- 1975-12-23 IT IT30727/75A patent/IT1059546B/en active
- 1975-12-23 AR AR261740A patent/AR218610A1/en active
Also Published As
Publication number | Publication date |
---|---|
CS193485B2 (en) | 1979-10-31 |
FR2295794B1 (en) | 1983-01-21 |
SE7513988L (en) | 1976-06-24 |
ATA962275A (en) | 1978-04-15 |
MX3358E (en) | 1980-10-13 |
ZA757672B (en) | 1977-04-27 |
SE427426B (en) | 1983-04-11 |
NO754189L (en) | 1976-06-24 |
NO146975C (en) | 1983-01-12 |
AU8777175A (en) | 1977-06-30 |
YU39955B (en) | 1985-06-30 |
JPS5188491A (en) | 1976-08-03 |
PH13098A (en) | 1979-11-28 |
BE836902A (en) | 1976-06-21 |
YU323575A (en) | 1982-02-28 |
GB1526295A (en) | 1978-09-27 |
FR2295794A1 (en) | 1976-07-23 |
NO146975B (en) | 1982-10-04 |
AU496807B2 (en) | 1978-11-02 |
CA1046483A (en) | 1979-01-16 |
NL7514815A (en) | 1976-06-25 |
AT346818B (en) | 1978-11-27 |
IT1059546B (en) | 1982-06-21 |
FI753609A (en) | 1976-06-24 |
BR7508454A (en) | 1976-08-24 |
AR218610A1 (en) | 1980-06-30 |
DE2553025A1 (en) | 1976-06-24 |
HU178762B (en) | 1982-06-28 |
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