SE7610732L - WAY TO REGENERATE COOKING CATALYST PARTICLES - Google Patents

WAY TO REGENERATE COOKING CATALYST PARTICLES

Info

Publication number
SE7610732L
SE7610732L SE7610732A SE7610732A SE7610732L SE 7610732 L SE7610732 L SE 7610732L SE 7610732 A SE7610732 A SE 7610732A SE 7610732 A SE7610732 A SE 7610732A SE 7610732 L SE7610732 L SE 7610732L
Authority
SE
Sweden
Prior art keywords
catalyst
regenerated catalyst
conversion
coke
regeneration
Prior art date
Application number
SE7610732A
Other languages
Unknown language ( )
Swedish (sv)
Other versions
SE428762B (en
Inventor
A J Conner
L O Stine
Original Assignee
Uop Inc
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 Uop Inc filed Critical Uop Inc
Publication of SE7610732L publication Critical patent/SE7610732L/en
Publication of SE428762B publication Critical patent/SE428762B/en

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
    • B01J8/18Chemical 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
    • 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)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)

Abstract

A process for the regeneration of a coke-contaminated catalytic cracking catalyst removed from a hydrocarbon reaction zone, said catalyst containing catalytically effective amounts of a CO conversion promoter comprising one or more oxides of metals, and for the catalytic conversion of CO, resulting from the oxidation of coke from said catalyst, to carbon monoxide. The process comprises the steps of: oxidizing coke in a first dense bed of catalyst maintained in a regeneration zone to produce partially spent regeneration gas and regenerated catalyst; passing the regeneration gas and regenerated catalyst to a dilute phase transport riser wherein CO is essentially completely converted in the presence of the CU conversion promoter to CO2 and wherein at least a portion of the heat of CO conversion is transferred to the regenerated catalyst; and, passing regenerated catalyst to a second dense bed from which regenerated catalyst is returned to the hydrocarbon reaction zone.
SE7610732A 1975-09-29 1976-09-28 VIEW TO REGULATE A FLUIDIZED CATALYTIC CRACKING USING COOK POLLUTED CATALYST CONTAINING A CO-CONVERSION PROMOTER SE428762B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US61747475A 1975-09-29 1975-09-29

Publications (2)

Publication Number Publication Date
SE7610732L true SE7610732L (en) 1977-03-30
SE428762B SE428762B (en) 1983-07-25

Family

ID=24473791

Family Applications (1)

Application Number Title Priority Date Filing Date
SE7610732A SE428762B (en) 1975-09-29 1976-09-28 VIEW TO REGULATE A FLUIDIZED CATALYTIC CRACKING USING COOK POLLUTED CATALYST CONTAINING A CO-CONVERSION PROMOTER

Country Status (27)

Country Link
JP (1) JPS5814261B2 (en)
AR (1) AR218614A1 (en)
AT (1) AT357988B (en)
AU (1) AU501212B2 (en)
BE (1) BE846037R (en)
BG (1) BG41303A3 (en)
BR (1) BR7606466A (en)
CA (1) CA1078805A (en)
CS (1) CS191886B2 (en)
DD (1) DD128386A5 (en)
DE (1) DE2636217C3 (en)
DK (1) DK436176A (en)
ES (1) ES451916A2 (en)
FI (1) FI61514C (en)
FR (1) FR2325429A2 (en)
GB (1) GB1551788A (en)
IE (1) IE43943B1 (en)
IN (1) IN145334B (en)
IT (1) IT1080509B (en)
MX (1) MX146294A (en)
NL (1) NL7609876A (en)
PH (1) PH13627A (en)
PL (1) PL106688B3 (en)
PT (1) PT65495B (en)
SE (1) SE428762B (en)
YU (1) YU39972B (en)
ZA (1) ZA765780B (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07105595A (en) * 1993-10-06 1995-04-21 Akai Electric Co Ltd Cassette tape recorder
CN107335429A (en) * 2017-06-29 2017-11-10 连云港师范高等专科学校 A kind of manufacture method of indoor formaldehyde through catalytic oxidation cleanser

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2436927A (en) * 1943-11-29 1948-03-02 Universal Oil Prod Co Prevention of afterburning in fluidized catalytic cracking processes
IL42265A (en) * 1972-05-30 1976-04-30 Universal Oil Prod Co Process for the regeneration of fluidized catalyst
CA1051411A (en) * 1973-09-20 1979-03-27 Mobil Oil Corporation Cracking catalyst and cracking process using same
NL7501695A (en) * 1974-03-04 1975-09-08 Standard Oil Co METHOD FOR REGENERATING CRACK CATALYSTS.

Also Published As

Publication number Publication date
ZA765780B (en) 1977-09-28
PH13627A (en) 1980-08-14
IN145334B (en) 1978-09-23
MX146294A (en) 1982-06-03
SE428762B (en) 1983-07-25
NL7609876A (en) 1977-03-31
YU39972B (en) 1985-06-30
ATA616676A (en) 1980-01-15
GB1551788A (en) 1979-08-30
DE2636217A1 (en) 1977-03-31
AT357988B (en) 1980-08-11
JPS5814261B2 (en) 1983-03-18
CS191886B2 (en) 1979-07-31
PL106688B3 (en) 1980-01-31
ES451916A2 (en) 1978-02-16
IE43943L (en) 1977-03-29
DK436176A (en) 1977-03-30
FR2325429A2 (en) 1977-04-22
JPS5242491A (en) 1977-04-02
FR2325429B2 (en) 1981-09-25
DE2636217B2 (en) 1978-04-27
DE2636217C3 (en) 1986-05-28
AU501212B2 (en) 1979-06-14
DD128386A5 (en) 1977-11-16
PT65495B (en) 1978-02-13
FI61514B (en) 1982-04-30
AR218614A1 (en) 1980-06-30
BE846037R (en) 1976-12-31
IE43943B1 (en) 1981-07-01
FI61514C (en) 1982-08-10
BG41303A3 (en) 1987-05-15
AU1695476A (en) 1978-02-23
FI762613A (en) 1977-03-30
BR7606466A (en) 1977-06-28
PT65495A (en) 1976-09-01
CA1078805A (en) 1980-06-03
YU231176A (en) 1982-05-31
IT1080509B (en) 1985-05-16

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