JPS5558289A - Method of stripping high temperature regeneration catalyst with fuel gas before hydrocarbon converting process - Google Patents

Method of stripping high temperature regeneration catalyst with fuel gas before hydrocarbon converting process

Info

Publication number
JPS5558289A
JPS5558289A JP10672279A JP10672279A JPS5558289A JP S5558289 A JPS5558289 A JP S5558289A JP 10672279 A JP10672279 A JP 10672279A JP 10672279 A JP10672279 A JP 10672279A JP S5558289 A JPS5558289 A JP S5558289A
Authority
JP
Japan
Prior art keywords
high temperature
fuel gas
gas before
converting process
temperature 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.)
Granted
Application number
JP10672279A
Other languages
English (en)
Other versions
JPS6334200B2 (ja
Inventor
Suteiibun Zurinsukak Furetsudo
Jieemuzu Makugabuan Suteiibun
Uiruherumu Shiyatsu Kurausu
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.)
ExxonMobil Oil Corp
Original Assignee
Mobil Oil Corp
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 Corp filed Critical Mobil Oil Corp
Publication of JPS5558289A publication Critical patent/JPS5558289A/ja
Publication of JPS6334200B2 publication Critical patent/JPS6334200B2/ja
Granted 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
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/005Separating solid material from the gas/liquid stream
    • B01J8/0055Separating solid material from the gas/liquid stream using cyclones
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • B04C5/02Construction of inlets by which the vortex flow is generated, e.g. tangential admission, the fluid flow being forced to follow a downward path by spirally wound bulkheads, or with slightly downwardly-directed tangential admission
    • B04C5/06Axial inlets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • B04C5/12Construction of the overflow ducting, e.g. diffusing or spiral exits
    • 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
    • C10G11/182Regeneration
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)
  • Industrial Gases (AREA)
JP10672279A 1978-08-25 1979-08-23 Method of stripping high temperature regeneration catalyst with fuel gas before hydrocarbon converting process Granted JPS5558289A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US05/937,035 US4176083A (en) 1978-08-25 1978-08-25 Separating flue gas from regenerated cracking catalyst

Publications (2)

Publication Number Publication Date
JPS5558289A true JPS5558289A (en) 1980-04-30
JPS6334200B2 JPS6334200B2 (ja) 1988-07-08

Family

ID=25469391

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10672279A Granted JPS5558289A (en) 1978-08-25 1979-08-23 Method of stripping high temperature regeneration catalyst with fuel gas before hydrocarbon converting process

Country Status (8)

Country Link
US (1) US4176083A (ja)
EP (1) EP0008879B1 (ja)
JP (1) JPS5558289A (ja)
BR (1) BR7905468A (ja)
CA (1) CA1133452A (ja)
DE (1) DE2961607D1 (ja)
ES (1) ES483630A1 (ja)
ZA (1) ZA794426B (ja)

Families Citing this family (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4268416A (en) * 1979-06-15 1981-05-19 Uop Inc. Gaseous passivation of metal contaminants on cracking catalyst
US4298459A (en) * 1979-11-05 1981-11-03 Standard Oil Company (Indiana) Fluid catalytic cracking of heavy petroleum fractions
US4372840A (en) * 1979-12-31 1983-02-08 Exxon Research And Engineering Co. Process for reducing coke formation in heavy feed catalytic cracking
US4280895A (en) * 1979-12-31 1981-07-28 Exxon Research & Engineering Co. Passivation of cracking catalysts
US4280896A (en) * 1979-12-31 1981-07-28 Exxon Research & Engineering Co. Passivation of cracking catalysts
US4370220A (en) * 1979-12-31 1983-01-25 Exxon Research And Engineering Co. Process for reducing coke formation in heavy feed catalytic cracking
US4372841A (en) * 1979-12-31 1983-02-08 Exxon Research And Engineering Co. Process for reducing coke formation in heavy feed catalytic cracking
US4364848A (en) * 1980-03-21 1982-12-21 Uop Inc. Passivation of metal contaminants on cracking catalyst
US4361496A (en) * 1980-07-07 1982-11-30 Uop Inc. Passivation of metal contaminants on cracking catalyst
US5358630A (en) 1980-11-17 1994-10-25 Phillips Petroleum Company Regenerating zeolitic cracking catalyst
US4404090A (en) * 1980-11-21 1983-09-13 Uop Inc. Passivation of metal contaminants on cracking catalyst
US4382015A (en) * 1980-11-21 1983-05-03 Uop Inc. Passivation of metal contaminants on cracking catalyst
US4409093A (en) * 1981-05-04 1983-10-11 Exxon Research And Engineering Co. Process for reducing coke formation in heavy feed catalytic cracking
US4692311A (en) * 1982-12-23 1987-09-08 Shell Oil Company Apparatus for the separation of fluid cracking catalyst particles from gaseous hydrocarbons
US4519990A (en) * 1983-05-24 1985-05-28 Rockwell International Corporation Spray dryer for the purification of a gas
US4556542A (en) * 1984-06-04 1985-12-03 Texaco Inc. FCCU Catalyst-high velocity vapor separator
US4689206A (en) * 1984-10-22 1987-08-25 Mobil Oil Corporation Multistage stripper for FCC unit with improved catalyst separation
GB2166662A (en) * 1984-11-09 1986-05-14 Shell Int Research Separating hydrocarbon products from catalyst particles
US4994424A (en) * 1989-11-06 1991-02-19 Mobil Oil Corporation Catalytic cracking process with improved flow in swirl regenerator
US5190650A (en) * 1991-06-24 1993-03-02 Exxon Research And Engineering Company Tangential solids separation transfer tunnel
US5290431A (en) * 1993-01-08 1994-03-01 Mobil Oil Corporation FCC process with concentrators on cyclone inlets
US5464528A (en) * 1993-12-30 1995-11-07 Mobil Oil Corporation FCC process and apparatus with upset tolerant third stage separator
US6248298B1 (en) * 1996-12-23 2001-06-19 Mobil Oil Corporation FCC unit catalyst stripper
US6965057B2 (en) * 2004-03-24 2005-11-15 Exxonmobil Chemical Patents Inc. Oxygenate to olefin process
US9370783B2 (en) * 2014-03-28 2016-06-21 Uop Llc Apparatuses and methods for gas-solid separations using cyclones

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2408943A (en) * 1944-07-17 1946-10-08 Universal Oil Prod Co Conversion of hydrocarbons
BE530987A (ja) * 1953-08-07
US2981695A (en) * 1957-06-20 1961-04-25 Shell Oil Co Regeneration of carbonized finely divided contact agents
US3408286A (en) * 1967-07-06 1968-10-29 Sun Oil Co Catalytic cracking with the purging of the regenerated catalyst with a liquid hydrocarbon
FR2071125A5 (en) * 1969-12-18 1971-09-17 Exxon Research Engineering Co Catalyst regenerator with two regeneration - zones
US4043899A (en) * 1976-02-27 1977-08-23 Mobil Oil Corporation Method and means for separating gasiform materials from finely divided catalyst particles
US4071436A (en) * 1976-03-11 1978-01-31 Chevron Research Company Process for removing sulphur from a gas

Also Published As

Publication number Publication date
DE2961607D1 (en) 1982-02-11
EP0008879A1 (en) 1980-03-19
ES483630A1 (es) 1980-04-16
US4176083A (en) 1979-11-27
EP0008879B1 (en) 1981-12-23
CA1133452A (en) 1982-10-12
ZA794426B (en) 1981-04-29
BR7905468A (pt) 1980-07-15
JPS6334200B2 (ja) 1988-07-08

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