SE7608715L - WAY TO REGENATE A COKE UNIT CRACKING CATALYST - Google Patents
WAY TO REGENATE A COKE UNIT CRACKING CATALYSTInfo
- Publication number
- SE7608715L SE7608715L SE7608715A SE7608715A SE7608715L SE 7608715 L SE7608715 L SE 7608715L SE 7608715 A SE7608715 A SE 7608715A SE 7608715 A SE7608715 A SE 7608715A SE 7608715 L SE7608715 L SE 7608715L
- Authority
- SE
- Sweden
- Prior art keywords
- regeneration gas
- catalyst
- oxygen concentration
- temperature
- conversion
- 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
- B01J8/1809—Controlling 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
- 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
-
- 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
- C10G11/187—Controlling or regulating
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00026—Controlling or regulating the heat exchange system
- B01J2208/00035—Controlling or regulating the heat exchange system involving measured parameters
- B01J2208/0007—Pressure measurement
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00265—Part of all of the reactants being heated or cooled outside the reactor while recycling
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00539—Pressure
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00548—Flow
-
- 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)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Carbon And Carbon Compounds (AREA)
Abstract
A process for initiating and controlling the regeneration of spent fluid catalytic cracking catalyst containing catalytically effective amounts of a C0 conversion promotor and for the essentially complete catalytic conversion of C0 to C02 both in a dense bed of catalyst maintained in an FCC regeneration zone. The process comprises (a) passing to a dense-phase catalyst bed in a regeneration zone said catalyst and fresh regeneration gas at a first flow rate sufficient to oxidize coke to produce partially spent regeneration gas, (b) oxidizing coke at first oxidizing conditions including a catalyst bed first temperature of from 399.degree.C to 677.degree.C to produce regenerated catalyst and partially spent regeneration gas containing C0, (c) increasing the catalyst bed temperature from said first temperature to a second temperature of from 677.degree.C to 760.degree.C, (d) passing to the catalyst bed fresh regeneration gas at a second flow rate stoichiometrically sufficient to essentially completely oxidize C0 to C02, (e) oxidizing in said catalyst bed, maintained at second oxidizing conditions including the presence of said C0 conversion promotor, C0 to produce spent regeneration gas, (f) analyzing spent regeneration gas to obtain a measured free-oxygen concentration and comparing the measured free-oxygen concentration to a predetermined free-oxygen concentration, and (g) thereafter regulating fresh regeneration gas at a third flow rate to maintain the measured free-oxygen concentration equal to the predetermined free-oxygen concentration thereby ensuring essentially complete conversion of C0 to C02. The process is generally distinguishable from the prior art in terms of the C0 conversion temperature employed.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US60185175A | 1975-08-04 | 1975-08-04 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| SE7608715L true SE7608715L (en) | 1977-02-05 |
| SE427427B SE427427B (en) | 1983-04-11 |
Family
ID=24409020
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SE7608715A SE427427B (en) | 1975-08-04 | 1976-08-03 | SET TO REGENERATE A COOK-POLLUTED CATALYST |
Country Status (29)
| Country | Link |
|---|---|
| JP (1) | JPS5242492A (en) |
| AT (1) | AT353753B (en) |
| AU (1) | AU501360B2 (en) |
| BE (1) | BE844870A (en) |
| BR (1) | BR7605098A (en) |
| CA (1) | CA1072527A (en) |
| CS (1) | CS226165B2 (en) |
| DD (1) | DD126209A5 (en) |
| DE (1) | DE2633995C3 (en) |
| DK (1) | DK350076A (en) |
| EG (1) | EG12448A (en) |
| ES (1) | ES450414A1 (en) |
| FI (1) | FI61513C (en) |
| FR (1) | FR2320137A2 (en) |
| GB (1) | GB1551925A (en) |
| GR (1) | GR61129B (en) |
| IE (1) | IE43837B1 (en) |
| IL (1) | IL50141A (en) |
| IN (1) | IN155728B (en) |
| IT (1) | IT1066750B (en) |
| MX (1) | MX143792A (en) |
| NL (1) | NL7608620A (en) |
| PH (1) | PH13774A (en) |
| PL (1) | PL107089B3 (en) |
| PT (1) | PT65408B (en) |
| SE (1) | SE427427B (en) |
| TR (1) | TR18951A (en) |
| YU (1) | YU39970B (en) |
| ZA (1) | ZA764638B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61127613A (en) * | 1984-11-22 | 1986-06-14 | Mitsui Toatsu Chem Inc | Purifying method of carbon dioxide |
Family Cites Families (3)
| 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 | ||
| BE832738A (en) * | 1975-08-26 | 1975-12-16 | PROCESS FOR INITIATING SUBSTANTIALLY COMPLETE OXIDATION OF CO TO CO 2 IN A DEPLETED CATALYST REGENERATION ZONE |
-
1976
- 1976-07-26 PT PT65408A patent/PT65408B/en unknown
- 1976-07-27 IL IL50141A patent/IL50141A/en unknown
- 1976-07-29 DE DE2633995A patent/DE2633995C3/en not_active Expired
- 1976-07-30 FI FI762190A patent/FI61513C/en not_active IP Right Cessation
- 1976-07-30 IN IN1360/CAL/76A patent/IN155728B/en unknown
- 1976-08-02 YU YU1901/76A patent/YU39970B/en unknown
- 1976-08-02 FR FR7623569A patent/FR2320137A2/en active Granted
- 1976-08-02 ZA ZA764638A patent/ZA764638B/en unknown
- 1976-08-03 SE SE7608715A patent/SE427427B/en not_active IP Right Cessation
- 1976-08-03 DK DK350076A patent/DK350076A/en not_active Application Discontinuation
- 1976-08-03 NL NL7608620A patent/NL7608620A/en not_active Application Discontinuation
- 1976-08-03 IE IE1711/76A patent/IE43837B1/en unknown
- 1976-08-03 AU AU16528/76A patent/AU501360B2/en not_active Expired
- 1976-08-03 GB GB32257/76A patent/GB1551925A/en not_active Expired
- 1976-08-03 ES ES450414A patent/ES450414A1/en not_active Expired
- 1976-08-03 CS CS765077A patent/CS226165B2/en unknown
- 1976-08-03 DD DD194198A patent/DD126209A5/xx unknown
- 1976-08-04 PH PH18756A patent/PH13774A/en unknown
- 1976-08-04 TR TR18951A patent/TR18951A/en unknown
- 1976-08-04 EG EG477/76A patent/EG12448A/en active
- 1976-08-04 IT IT50765/76A patent/IT1066750B/en active
- 1976-08-04 BR BR7605098A patent/BR7605098A/en unknown
- 1976-08-04 AT AT577876A patent/AT353753B/en not_active IP Right Cessation
- 1976-08-04 BE BE169547A patent/BE844870A/en not_active IP Right Cessation
- 1976-08-04 MX MX165772A patent/MX143792A/en unknown
- 1976-08-04 PL PL1976191617A patent/PL107089B3/en unknown
- 1976-08-04 JP JP51093094A patent/JPS5242492A/en active Pending
- 1976-08-04 GR GR51408A patent/GR61129B/en unknown
- 1976-08-04 CA CA258,417A patent/CA1072527A/en not_active Expired
Also Published As
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| SE7416053L (en) | ||
| ES8505834A1 (en) | Semi-continuous regeneration of sulfur-contaminated catalytic conversion systems | |
| GB1536158A (en) | Method of regenerating a cracking catalyst with substantially complete combustion of carbon monoxide | |
| GB1499891A (en) | Process for catalytically converting hydrocarbons | |
| ATE31253T1 (en) | ADDING WATER TO THE REGENERATION AIR. | |
| FR1359156A (en) | Continuous process for cracking hydrocarbon oils | |
| CA983877A (en) | Fluid catalytic cracking process with substantially complete combustion of carbon monoxide during regeneration of catalyst | |
| MY101859A (en) | Method and apparatus for regeneration of hydrocarbon conversion catalyst. | |
| JPS51148664A (en) | Method of reducing flue gas pollutants from fluid decomposing catalyst regenerator | |
| SE7608715L (en) | WAY TO REGENATE A COKE UNIT CRACKING CATALYST | |
| GB1439532A (en) | Dense bed after burning a catalystic regeneration zone | |
| ES458567A1 (en) | Fluidized cracking catalyst regeneration process and apparatus | |
| GB1518530A (en) | Method of initiating essentially complete oxidation of co to co2 in a spent-catalyst regenerating zone | |
| SE7416054L (en) | ||
| SE421381B (en) | WAY TO REGENATE A COOK-POLLUTED CATALYST UNDER AT THE SAME TIME CLEARLY REGULATED COMBUSTION OF CO | |
| SE7610732L (en) | WAY TO REGENERATE COOKING CATALYST PARTICLES | |
| ES454471A1 (en) | Fluidized cracking catalyst regeneration process and apparatus | |
| FR2331609A1 (en) | Initiation of carbon monoxide oxidn. - in fluid catalytic cracking regenerators by increase of coke content of regenerated catalyst and then of air flow rate | |
| JPS5339252A (en) | Moving bed type catalytic reaction vessel | |
| SU541416A3 (en) | Method for regeneration of zeolite-containing carbon cracking catalyst | |
| JPS6485143A (en) | Method and apparatus for recovering fluid catalyst for contact cracking | |
| SU472671A1 (en) | The method of cleaning exhaust gases from carbon monoxide | |
| GB1386694A (en) | Process for increasing the reactivity at solid surfaces | |
| ES442834A1 (en) | A method for initiating essentially complete oxidation of co to co2 in a bed of dessert phase catalyst. (Machine-translation by Google Translate, not legally binding) | |
| JPS528976A (en) | Process for catalytic reaction of solids entrained gases |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| NUG | Patent has lapsed |
Ref document number: 7608715-4 Effective date: 19930307 Format of ref document f/p: F |