GB1406837A - High temperature catalytic cracking with zeolite catalysts - Google Patents

High temperature catalytic cracking with zeolite catalysts

Info

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withdrawn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
Application number
GB4113072A
Other languages
English (en)
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mobil Oil AS
Original Assignee
Mobil Oil AS
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Mobil Oil AS filed Critical Mobil Oil AS
Publication of GB1406837A publication Critical patent/GB1406837A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00Catalysts comprising molecular sieves
    • B01J29/90Regeneration or reactivation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00Catalysts comprising molecular sieves
    • B01J29/04Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/40Crystalline 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24Chemical 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
    • B01J8/26Chemical 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
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G11/00Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/14Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
    • C10G11/18Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2229/00Aspects of molecular sieve catalysts not covered by B01J29/00
    • B01J2229/30After treatment, characterised by the means used
    • B01J2229/40Special temperature treatment, i.e. other than just for template removal
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P30/00Technologies relating to oil refining and petrochemical industry
    • Y02P30/40Ethylene production
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S208/00Mineral oils: processes and products
    • Y10S208/02Molecular 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)
GB4113072A 1971-10-05 1972-09-05 High temperature catalytic cracking with zeolite catalysts Expired GB1406837A (en)

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)

* Cited by examiner, † Cited by third party
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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)

* Cited by examiner, † Cited by third party
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

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