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- withdrawn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
- 239000003054 catalyst Substances 0.000 title abstract 23
- 239000010457 zeolite Substances 0.000 title abstract 3
- 229910021536 Zeolite Inorganic materials 0.000 title abstract 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 title abstract 2
- 238000004523 catalytic cracking Methods 0.000 title 1
- 239000003921 oil Substances 0.000 abstract 6
- 238000006243 chemical reaction Methods 0.000 abstract 4
- 239000007789 gas Substances 0.000 abstract 4
- 229930195733 hydrocarbon Natural products 0.000 abstract 4
- 239000000725 suspension Substances 0.000 abstract 4
- 239000004215 Carbon black (E152) Substances 0.000 abstract 3
- 150000002430 hydrocarbons Chemical class 0.000 abstract 3
- 238000005336 cracking Methods 0.000 abstract 2
- 239000002245 particle Substances 0.000 abstract 2
- -1 C5E Hydrocarbon Chemical class 0.000 abstract 1
- WGLPBDUCMAPZCE-UHFFFAOYSA-N Trioxochromium Chemical compound O=[Cr](=O)=O WGLPBDUCMAPZCE-UHFFFAOYSA-N 0.000 abstract 1
- 229910000423 chromium oxide Inorganic materials 0.000 abstract 1
- 239000000571 coke Substances 0.000 abstract 1
- 239000000463 material Substances 0.000 abstract 1
- 229910044991 metal oxide Inorganic materials 0.000 abstract 1
- 150000004706 metal oxides Chemical class 0.000 abstract 1
- 238000012986 modification Methods 0.000 abstract 1
- 230000004048 modification Effects 0.000 abstract 1
- 230000001172 regenerating effect Effects 0.000 abstract 1
- 230000008929 regeneration Effects 0.000 abstract 1
- 238000011069 regeneration method Methods 0.000 abstract 1
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
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Crystallography & Structural Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
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 (enrdf_load_stackoverflow) |
JP (1) | JPS4845505A (enrdf_load_stackoverflow) |
AU (1) | AU464473B2 (enrdf_load_stackoverflow) |
DE (1) | DE2248826A1 (enrdf_load_stackoverflow) |
FR (1) | FR2155962B1 (enrdf_load_stackoverflow) |
GB (1) | GB1406837A (enrdf_load_stackoverflow) |
IT (1) | IT968612B (enrdf_load_stackoverflow) |
NL (1) | NL7213453A (enrdf_load_stackoverflow) |
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 |
ZA744642B (en) * | 1973-09-20 | 1976-02-25 | Mobil Oil Corp | Cracking catalyst and cracking process using same |
US4174272A (en) * | 1973-09-20 | 1979-11-13 | Mobil Oil Corporation | Catalytic cracking of hydrocarbons |
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 |
US4002557A (en) * | 1974-05-28 | 1977-01-11 | Mobil Oil Corporation | Catalytic conversion of high metals feed stocks |
US4035285A (en) * | 1974-05-28 | 1977-07-12 | Mobil Oil Corporation | Hydrocarbon conversion process |
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 |
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 |
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 |
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 (pt) * | 1982-07-15 | 1984-02-21 | Petroleo Brasileiro Sa | Processo para craqueamento catalitico fluido de hidrocarbonetos |
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 |
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 |
EP0489723A2 (en) * | 1986-09-03 | 1992-06-10 | Mobil Oil Corporation | Process for fluidized catalytic cracking with reactive fragments |
US4717466A (en) * | 1986-09-03 | 1988-01-05 | Mobil Oil Corporation | Multiple riser fluidized catalytic cracking process utilizing hydrogen and carbon-hydrogen contributing fragments |
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 |
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 |
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 |
US4802971A (en) * | 1986-09-03 | 1989-02-07 | Mobil Oil Corporation | Single riser fluidized catalytic cracking process utilizing hydrogen and carbon-hydrogen contributing 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 |
US7169293B2 (en) * | 1999-08-20 | 2007-01-30 | Uop Llc | Controllable space velocity reactor and process |
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 |
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 (zh) * | 2011-07-27 | 2015-08-11 | Exxonmobil Chem Patents Inc | 具有分階擋板的流體床反應器 |
US9187700B2 (en) | 2012-01-13 | 2015-11-17 | United Technologies Corporation | Method for reducing coke deposition |
US10508064B2 (en) | 2012-11-12 | 2019-12-17 | Uop Llc | Process for oligomerizing gasoline without further upgrading |
US9834492B2 (en) | 2012-11-12 | 2017-12-05 | Uop Llc | Process for fluid catalytic cracking oligomerate |
WO2014074833A1 (en) | 2012-11-12 | 2014-05-15 | Uop Llc | Process for making gasoline by oligomerization |
US9522375B2 (en) | 2012-11-12 | 2016-12-20 | Uop Llc | Apparatus for fluid catalytic cracking oligomerate |
US9441173B2 (en) | 2012-11-12 | 2016-09-13 | Uop Llc | Process for making diesel by oligomerization |
US9663415B2 (en) | 2012-11-12 | 2017-05-30 | Uop Llc | Process for making diesel by oligomerization of gasoline |
US9914673B2 (en) | 2012-11-12 | 2018-03-13 | Uop Llc | Process for oligomerizing light olefins |
US9644159B2 (en) | 2012-11-12 | 2017-05-09 | Uop Llc | Composition of oligomerate |
US9522373B2 (en) | 2012-11-12 | 2016-12-20 | Uop Llc | Apparatus for oligomerizing light olefins |
US9434891B2 (en) | 2012-11-12 | 2016-09-06 | Uop Llc | Apparatus for recovering oligomerate |
US9567267B2 (en) | 2012-11-12 | 2017-02-14 | Uop Llc | Process for oligomerizing light olefins including pentenes |
CN106102900A (zh) | 2014-03-04 | 2016-11-09 | 巴斯夫公司 | 临时添加或注入系统 |
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/it active
- 1972-10-04 NL NL7213453A patent/NL7213453A/xx unknown
- 1972-10-05 DE DE19722248826 patent/DE2248826A1/de active Pending
Also Published As
Publication number | Publication date |
---|---|
FR2155962A1 (enrdf_load_stackoverflow) | 1973-05-25 |
DE2248826A1 (de) | 1973-04-12 |
FR2155962B1 (enrdf_load_stackoverflow) | 1975-01-03 |
US3849291A (en) | 1974-11-19 |
NL7213453A (enrdf_load_stackoverflow) | 1973-04-09 |
JPS4845505A (enrdf_load_stackoverflow) | 1973-06-29 |
AU4673872A (en) | 1974-03-21 |
AU464473B2 (en) | 1975-08-28 |
IT968612B (it) | 1974-03-20 |
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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 |