GB1406837A - High temperature catalytic cracking with zeolite catalysts - Google Patents
High temperature catalytic cracking with zeolite catalystsInfo
- Publication number
- GB1406837A GB1406837A GB4113072A GB4113072A GB1406837A GB 1406837 A GB1406837 A GB 1406837A GB 4113072 A GB4113072 A GB 4113072A GB 4113072 A GB4113072 A GB 4113072A GB 1406837 A GB1406837 A GB 1406837A
- Authority
- GB
- United Kingdom
- Prior art keywords
- catalyst
- bed
- feed
- standpipe
- withdrawn
- 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
-
- 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
- B01J29/90—Regeneration or reactivation
-
- 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
-
- 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
-
- 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
- B01J2229/40—Special temperature treatment, i.e. other than just for template removal
-
- 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
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S208/00—Mineral oils: processes and products
- Y10S208/02—Molecular sieve
Abstract
1406837 Cracking MOBIL OIL CORP 5 Sept 1972 [5 Oct 1971] 41130/72 Heading C5E Hydrocarbon oils are converted to gasoline by (a) combining a first hydrocarbon feed (2) with particles of hot regenerated zeolite catalyst (8) to form a suspension at 1000‹ F. or above; (b) passing this suspension through a first conversion zone (10) to give a residence time of 1 to 12 seconds; (c) separating vaporous product from (b) from catalyst; (d) combining the catalyst from (c) (26) with hot, freshly regenerated catalyst particles (28) and a second hydrocarbon feed (32) more refractory than the first, to form a second suspension; (e) passing this second suspension at 950‹ F. or above through a second conversion zone (36) to give a residence time of 2 to 15 seconds; (f) separating vaporous product from (e) from catalyst; (g) stripping the catalyst from (f); and (h) regenerating stripped catalyst from (g) by burning in an oxygencontaining gas. The first feed may be a fraction of low molecular weight, the second of higher molecular weight; or the first may be a virgin gas oil and the second a coker gas oil, recycle oil or residual stock. The catalyst may contain two different zeolites, and may also contain a metal oxide that will enhance regeneration by catalysing the conversion of CO to CO 2 , e.g. chromium oxide. As shown, a first feed is heated in furnace 4, diluted if desired by steam or light hydrocarbons at 6, combined with regenerated catalyst from standpipe 8 and cracked in riser 10. Further portions of feed may be injected at 7<SP>1</SP> and 7<SP>11</SP> to adjust the residence time. The cracked material is discharged through cyclone separators 11 into hopper 14; the vaporous product is collected at 12 and taken off at 16, the catalyst is collected in dense bed 20, where it is stripped by steam from a line 22. A vertical baffle 24 separates catalyst beds 20 and 40, but the upper parts of the hopper are in open communication. Catalyst is withdrawn from bed 20, while still hot, by standpipe 26 and mixed with freshly regenerated catalyst from standpipe 28. The second feed 32 is cracked in a similar fashion to the first, but using a lower temperature, longer residence time, higher catalyst-to-oil ratio, and mixed catalyst from the standpipes 26 and 28. The product is separated in cyclone 38, and the catalyst passes to bed 40 and is stripped there. Catalyst fines in the stripping gases are removed by the central cyclone and returned to bed 40. Catalyst is withdrawn from bed 40 by standpipe 44, suspended in air from line 46 and carried into regenerator 52. In Fig. 4 (not shown) the baffle 24 has slots for controlled flow of catalyst between the two beds 20 and 40. In Fig. 5 (not shown) the catalysts from both reaction zones discharge into a common bed; part of this catalyst is withdrawn from a point above the stripping zone to be used in the second cracking zone, another part is withdrawn from below the stripping zone and sent to the regenerator; alternatively both streams can be taken from below the stripping zone. In this modification also a third feed can be injected into the dense bed, and used to control the amount of coke deposited on the catalyst, and so the temperature of the catalyst leaving the regenerator.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US00186639A US3849291A (en) | 1971-10-05 | 1971-10-05 | High temperature catalytic cracking with low coke producing crystalline zeolite catalysts |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1406837A true GB1406837A (en) | 1975-09-17 |
Family
ID=22685724
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB4113072A Expired GB1406837A (en) | 1971-10-05 | 1972-09-05 | High temperature catalytic cracking with zeolite catalysts |
Country Status (8)
Country | Link |
---|---|
US (1) | US3849291A (en) |
JP (1) | JPS4845505A (en) |
AU (1) | AU464473B2 (en) |
DE (1) | DE2248826A1 (en) |
FR (1) | FR2155962B1 (en) |
GB (1) | GB1406837A (en) |
IT (1) | IT968612B (en) |
NL (1) | NL7213453A (en) |
Families Citing this family (81)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4324688A (en) * | 1972-07-17 | 1982-04-13 | Texaco Inc. | Regeneration of cracking catalyst |
US3926778A (en) * | 1972-12-19 | 1975-12-16 | Mobil Oil Corp | Method and system for controlling the activity of a crystalline zeolite cracking catalyst |
US4064038A (en) * | 1973-05-21 | 1977-12-20 | Universal Oil Products Company | Fluid catalytic cracking process for conversion of residual oils |
US3948757A (en) * | 1973-05-21 | 1976-04-06 | Universal Oil Products Company | Fluid catalytic cracking process for upgrading a gasoline-range feed |
US4174272A (en) * | 1973-09-20 | 1979-11-13 | Mobil Oil Corporation | Catalytic cracking of hydrocarbons |
ZA744642B (en) * | 1973-09-20 | 1976-02-25 | Mobil Oil Corp | Cracking catalyst and cracking process using same |
US4072600A (en) * | 1974-02-08 | 1978-02-07 | Mobil Oil Corporation | Catalytic cracking process |
US3894931A (en) * | 1974-04-02 | 1975-07-15 | Mobil Oil Corp | Method for improving olefinic gasoline product of low conversion fluid catalytic cracking |
US3894933A (en) * | 1974-04-02 | 1975-07-15 | Mobil Oil Corp | Method for producing light fuel oil |
US4035285A (en) * | 1974-05-28 | 1977-07-12 | Mobil Oil Corporation | Hydrocarbon conversion process |
US4002557A (en) * | 1974-05-28 | 1977-01-11 | Mobil Oil Corporation | Catalytic conversion of high metals feed stocks |
US4090949A (en) * | 1974-07-31 | 1978-05-23 | Mobil Oil Corportion | Upgrading of olefinic gasoline with hydrogen contributors |
US4012455A (en) * | 1974-07-31 | 1977-03-15 | Mobil Oil Corporation | Upgrading refinery light olefins with hydrogen contributor |
US3974063A (en) * | 1974-10-17 | 1976-08-10 | Mobil Oil Corporation | Denitrogenating and upgrading of high nitrogen containing hydrocarbon stocks with low molecular weight carbon-hydrogen fragment contributors |
US3974062A (en) * | 1974-10-17 | 1976-08-10 | Mobil Oil Corporation | Conversion of full range crude oils with low molecular weight carbon-hydrogen fragment contributors over zeolite catalysts |
US4153535A (en) * | 1975-12-19 | 1979-05-08 | Standard Oil Company (Indiana) | Catalytic cracking with reduced emission of noxious gases |
US4064039A (en) * | 1976-01-28 | 1977-12-20 | Mobil Oil Corporation | Fluid catalytic cracking |
US4148751A (en) * | 1976-02-02 | 1979-04-10 | Uop Inc. | Method of regenerating coke-contaminated catalyst with simultaneous combustion of carbon monoxide |
US4064037A (en) * | 1976-07-09 | 1977-12-20 | Mobil Oil Corporation | Temporary shutdown of co-combustion devices |
US4116814A (en) * | 1977-07-18 | 1978-09-26 | Mobil Oil Corporation | Method and system for effecting catalytic cracking of high boiling hydrocarbons with fluid conversion catalysts |
US4226701A (en) * | 1979-01-08 | 1980-10-07 | Mobil Oil Corporation | Temporary shutdown of co-combustion devices |
US4359378A (en) * | 1979-04-16 | 1982-11-16 | Chevron Research Company | Catalytic cracking process for improved octane |
US4312743A (en) * | 1979-07-23 | 1982-01-26 | Uop Inc. | FCC Process using catalyst produced from used FCC catalyst |
US4312744A (en) * | 1979-08-29 | 1982-01-26 | Uop Inc. | FCC Process using low coke-make FCC catalyst |
US4347122A (en) * | 1979-11-14 | 1982-08-31 | Ashland Oil, Inc. | Carbo-metallic oil conversion with liquid water |
GB2063293B (en) * | 1979-11-14 | 1983-12-21 | Ashland Oil Inc | Carbo-metallic oil conversion with controlled co:co2 ratio in regeneration |
US4444651A (en) * | 1979-11-14 | 1984-04-24 | Ashland Oil, Inc. | Carbo-metallic oil conversion with controlled CO:CO2 ratio in multistage regeneration |
JPS5682886A (en) * | 1979-12-12 | 1981-07-06 | Mitsubishi Heavy Ind Ltd | Method for converting heavy oil into light oil |
US4239615A (en) * | 1979-12-19 | 1980-12-16 | Uop Inc. | High octane FCC process |
US4333821A (en) * | 1980-05-08 | 1982-06-08 | Uop Inc. | Process for use of a high octane FCC catalysts |
WO1982004061A1 (en) * | 1981-05-13 | 1982-11-25 | Mckay William E Jr | Stripping hydrocarbons from catalyst with combustion gases |
US4374019A (en) * | 1981-05-13 | 1983-02-15 | Ashland Oil, Inc. | Process for cracking high-boiling hydrocarbons using high ratio of catalyst residence time to vapor residence time |
US4402913A (en) * | 1981-09-30 | 1983-09-06 | Standard Oil Company (Indiana) | Apparatus for the fluidized catalytic cracking of hydrocarbon feedstocks |
US4422925A (en) * | 1981-12-28 | 1983-12-27 | Texaco Inc. | Catalytic cracking |
US4424116A (en) | 1982-03-25 | 1984-01-03 | Ashland Oil, Inc. | Converting and stripping heavy hydrocarbons in two stages of riser conversion with regenerated catalyst |
US4498976A (en) * | 1982-04-15 | 1985-02-12 | Mobil Oil Corporation | Suppression of light gas production in cracking processes by the addition of highly siliceous materials having high surface area and low acidity |
BR8204113A (en) * | 1982-07-15 | 1984-02-21 | Petroleo Brasileiro Sa | HYDROCARBON FLUID CATALYTIC CRACKING PROCESS |
US4417974A (en) * | 1982-08-23 | 1983-11-29 | Chevron Research Company | Riser cracking of catalyst-deactivating feeds |
US4601814A (en) * | 1983-05-27 | 1986-07-22 | Total Engineering And Research Company | Method and apparatus for cracking residual oils |
US4479870A (en) * | 1984-02-29 | 1984-10-30 | Jop Inc. | Use of lift gas in an FCC reactor riser |
US4606810A (en) * | 1985-04-08 | 1986-08-19 | Mobil Oil Corporation | FCC processing scheme with multiple risers |
US4693808A (en) * | 1986-06-16 | 1987-09-15 | Shell Oil Company | Downflow fluidized catalytic cranking reactor process and apparatus with quick catalyst separation means in the bottom thereof |
US4830728A (en) * | 1986-09-03 | 1989-05-16 | Mobil Oil Corporation | Upgrading naphtha in a multiple riser fluid catalytic cracking operation employing a catalyst mixture |
US4802971A (en) * | 1986-09-03 | 1989-02-07 | Mobil Oil Corporation | Single riser fluidized catalytic cracking process utilizing hydrogen and carbon-hydrogen contributing fragments |
US4861741A (en) * | 1986-09-03 | 1989-08-29 | Mobil Oil Corporation | Mixed catalyst system and catalytic conversion process employing same |
US4871446A (en) * | 1986-09-03 | 1989-10-03 | Mobil Oil Corporation | Catalytic cracking process employing mixed catalyst system |
US4888103A (en) * | 1986-09-03 | 1989-12-19 | Herbst Joseph A | Process of stripping in a catalytic cracking operation employing a catalyst mixture which includes a shape selective medium pore silicate zeolite component |
US4814068A (en) * | 1986-09-03 | 1989-03-21 | Mobil Oil Corporation | Fluid catalytic cracking process and apparatus for more effective regeneration of zeolite catalyst |
US4717466A (en) * | 1986-09-03 | 1988-01-05 | Mobil Oil Corporation | Multiple riser fluidized catalytic cracking process utilizing hydrogen and carbon-hydrogen contributing fragments |
US4892643A (en) * | 1986-09-03 | 1990-01-09 | Mobil Oil Corporation | Upgrading naphtha in a single riser fluidized catalytic cracking operation employing a catalyst mixture |
US4752375A (en) * | 1986-09-03 | 1988-06-21 | Mobil Oil Corporation | Single riser fluidized catalytic cracking process utilizing a C3-4 paraffin-rich co-feed and mixed catalyst system |
US4865718A (en) * | 1986-09-03 | 1989-09-12 | Mobil Oil Corporation | Maximizing distillate production in a fluid catalytic cracking operation employing a mixed catalyst system |
AU607435B2 (en) * | 1986-09-03 | 1991-03-07 | Mobil Oil Corporation | Process for fluidized catalytic cracking with reactive fragments |
US4874503A (en) * | 1988-01-15 | 1989-10-17 | Mobil Oil Corporation | Multiple riser fluidized catalytic cracking process employing a mixed catalyst |
GB8820358D0 (en) * | 1988-08-26 | 1988-09-28 | Shell Int Research | Process for catalytic cracking of hydrocarbon feedstock |
US5114682A (en) * | 1988-11-18 | 1992-05-19 | Stone & Webster Engineering Corporation | Apparatus for recovering heat energy from catalyst regenerator flue gases |
US5009769A (en) * | 1989-02-06 | 1991-04-23 | Stone & Webster Engineering Corporation | Process for catalytic cracking of hydrocarbons |
US5154818A (en) * | 1990-05-24 | 1992-10-13 | Mobil Oil Corporation | Multiple zone catalytic cracking of hydrocarbons |
US5139748A (en) * | 1990-11-30 | 1992-08-18 | Uop | FCC riser with transverse feed injection |
US5198590A (en) * | 1992-01-28 | 1993-03-30 | Arco Chemical Technology, L.P. | Hydrocarbon conversion |
US5462652A (en) * | 1993-09-24 | 1995-10-31 | Uop | Short contact FCC process with catalyst blending |
US5346613A (en) * | 1993-09-24 | 1994-09-13 | Uop | FCC process with total catalyst blending |
US6869521B2 (en) * | 2002-04-18 | 2005-03-22 | Uop Llc | Process and apparatus for upgrading FCC product with additional reactor with thorough mixing |
US20040104149A1 (en) * | 1999-08-20 | 2004-06-03 | Lomas David A. | Controllable volume reactor and process |
US7169293B2 (en) * | 1999-08-20 | 2007-01-30 | Uop Llc | Controllable space velocity reactor and process |
US6866771B2 (en) * | 2002-04-18 | 2005-03-15 | Uop Llc | Process and apparatus for upgrading FCC product with additional reactor with catalyst recycle |
EP2726575A1 (en) * | 2011-06-30 | 2014-05-07 | Shell Internationale Research Maatschappij B.V. | A dual riser catalytic cracking process for making middle distillate and lower olefins |
TWI495511B (en) * | 2011-07-27 | 2015-08-11 | Exxonmobil Chem Patents Inc | Fluid bed reactor with staged baffles |
US9187700B2 (en) * | 2012-01-13 | 2015-11-17 | United Technologies Corporation | Method for reducing coke deposition |
US9567267B2 (en) | 2012-11-12 | 2017-02-14 | Uop Llc | Process for oligomerizing light olefins including pentenes |
US9522373B2 (en) | 2012-11-12 | 2016-12-20 | Uop Llc | Apparatus for oligomerizing light olefins |
US9914673B2 (en) | 2012-11-12 | 2018-03-13 | Uop Llc | Process for oligomerizing light olefins |
US9278893B2 (en) | 2012-11-12 | 2016-03-08 | Uop Llc | Process for making gasoline by oligomerization |
US9644159B2 (en) | 2012-11-12 | 2017-05-09 | Uop Llc | Composition of oligomerate |
US10508064B2 (en) | 2012-11-12 | 2019-12-17 | Uop Llc | Process for oligomerizing gasoline without further upgrading |
US9663415B2 (en) | 2012-11-12 | 2017-05-30 | Uop Llc | Process for making diesel by oligomerization of gasoline |
US9441173B2 (en) | 2012-11-12 | 2016-09-13 | Uop Llc | Process for making diesel by oligomerization |
US9434891B2 (en) | 2012-11-12 | 2016-09-06 | Uop Llc | Apparatus for recovering oligomerate |
US9522375B2 (en) | 2012-11-12 | 2016-12-20 | Uop Llc | Apparatus for fluid catalytic cracking oligomerate |
US9834492B2 (en) | 2012-11-12 | 2017-12-05 | Uop Llc | Process for fluid catalytic cracking oligomerate |
WO2015134338A1 (en) | 2014-03-04 | 2015-09-11 | Basf Corporation | Temporary addition or injection system |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2379159A (en) * | 1943-07-31 | 1945-06-26 | Universal Oil Prod Co | Process for the catalytic conversion of hydrocarbons |
-
1971
- 1971-10-05 US US00186639A patent/US3849291A/en not_active Expired - Lifetime
-
1972
- 1972-09-05 GB GB4113072A patent/GB1406837A/en not_active Expired
- 1972-09-15 AU AU46738/72A patent/AU464473B2/en not_active Expired
- 1972-09-22 JP JP47094668A patent/JPS4845505A/ja active Pending
- 1972-10-03 FR FR7234909A patent/FR2155962B1/fr not_active Expired
- 1972-10-04 IT IT30078/72A patent/IT968612B/en active
- 1972-10-04 NL NL7213453A patent/NL7213453A/xx unknown
- 1972-10-05 DE DE19722248826 patent/DE2248826A1/en active Pending
Also Published As
Publication number | Publication date |
---|---|
US3849291A (en) | 1974-11-19 |
IT968612B (en) | 1974-03-20 |
FR2155962A1 (en) | 1973-05-25 |
AU464473B2 (en) | 1975-08-28 |
NL7213453A (en) | 1973-04-09 |
DE2248826A1 (en) | 1973-04-12 |
AU4673872A (en) | 1974-03-21 |
FR2155962B1 (en) | 1975-01-03 |
JPS4845505A (en) | 1973-06-29 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
CSNS | Application of which complete specification have been accepted and published, but patent is not sealed |