ES8107295A1 - Carbo-metallic oil conversion with controlled CO:CO2 ratio in regeneration - Google Patents

Carbo-metallic oil conversion with controlled CO:CO2 ratio in regeneration

Info

Publication number
ES8107295A1
ES8107295A1 ES497232A ES497232A ES8107295A1 ES 8107295 A1 ES8107295 A1 ES 8107295A1 ES 497232 A ES497232 A ES 497232A ES 497232 A ES497232 A ES 497232A ES 8107295 A1 ES8107295 A1 ES 8107295A1
Authority
ES
Spain
Prior art keywords
catalyst
carbo
cracking
feed
weight
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
ES497232A
Other languages
Spanish (es)
Other versions
ES497232A0 (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.)
Ashland LLC
Original Assignee
Ashland Oil 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
Priority claimed from US06/094,227 external-priority patent/US4354923A/en
Priority claimed from US06/094,091 external-priority patent/US4299687A/en
Application filed by Ashland Oil Inc filed Critical Ashland Oil Inc
Publication of ES8107295A1 publication Critical patent/ES8107295A1/en
Publication of ES497232A0 publication Critical patent/ES497232A0/en
Granted legal-status Critical Current

Links

Classifications

    • 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
    • B01J29/00Catalysts comprising molecular sieves
    • B01J29/90Regeneration or reactivation
    • 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)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)
  • Investigating Or Analysing Materials By Optical Means (AREA)

Abstract

In a process for the production of high octane gasoline and/or other valuable lower molecular weight products from carbo-metallic oils (such as crude oil, topped crude, reduced crude, residua, the extract from solvent de-asphalting and other heavy hydrocarbon fractions) by cracking in a fluid catalytic cracking riser zone operated with a vapour riser residence time of 0.5- 10 secs at 900-1400 DEG F and 10-50 psia, a conversion of at least 50% per pass and a coke production of 4-14% based on the weight of the feed and 0.3 to 3% based on the weight of the catalyst, the catalyst is regenerated to a carbon content of at least 0.25 ml% with at least the major proportion of the coke being burned at a CO:CO2 molar ratio of at least 0.25. This incomplete combustion helps to avoid supplying the regenerated catalyst with more heat than is desirable for cracking the feed.
ES497232A 1979-11-14 1980-11-14 PROCEDURE FOR THE ECONOMIC CONVERSION OF OILS AND THE LIKE IN LIGHTER PRODUCTS Granted ES497232A0 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US06/094,227 US4354923A (en) 1979-11-14 1979-11-14 Carbo-metallic oil conversion with liquid water, ballistic separation and controlled CO:CO2 ratio during catalyst regeneration
US06/094,091 US4299687A (en) 1979-11-14 1979-11-14 Carbo-metallic oil conversion with controlled CO:CO2 ratio in regeneration

Publications (2)

Publication Number Publication Date
ES8107295A1 true ES8107295A1 (en) 1981-10-16
ES497232A0 ES497232A0 (en) 1981-10-16

Family

ID=26788363

Family Applications (1)

Application Number Title Priority Date Filing Date
ES497232A Granted ES497232A0 (en) 1979-11-14 1980-11-14 PROCEDURE FOR THE ECONOMIC CONVERSION OF OILS AND THE LIKE IN LIGHTER PRODUCTS

Country Status (15)

Country Link
AT (1) AT373616B (en)
AU (1) AU542322B2 (en)
BR (1) BR8007424A (en)
CA (1) CA1175770A (en)
DE (1) DE3043107A1 (en)
EG (1) EG15396A (en)
ES (1) ES497232A0 (en)
FR (1) FR2470790B1 (en)
GB (1) GB2063293B (en)
IL (1) IL61490A (en)
IN (1) IN155032B (en)
IT (1) IT1142187B (en)
MX (1) MX160516A (en)
NO (1) NO162247C (en)
YU (1) YU42708B (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4431515A (en) * 1979-11-14 1984-02-14 Ashland Oil, Inc. Carbometallic oil conversion with hydrogen in a riser using a high metals containing catalyst
US4405445A (en) * 1981-08-24 1983-09-20 Ashland Oil, Inc. Homogenization of water and reduced crude for catalytic cracking
US4508839A (en) * 1981-08-27 1985-04-02 Ashland Oil, Inc. Catalyst for the conversion of carbo-metallic containing oils

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3303123A (en) * 1964-10-16 1967-02-07 Phillips Petroleum Co Catalytic cracking of residuum oils containing metal contaminants in several stages
US3849291A (en) * 1971-10-05 1974-11-19 Mobil Oil Corp High temperature catalytic cracking with low coke producing crystalline zeolite catalysts
US3944482A (en) * 1973-08-08 1976-03-16 Gulf Research & Development Company Process for the cracking of high metals content feedstocks
DE2508804A1 (en) * 1974-03-14 1975-09-18 Standard Oil Co METHOD OF CATALYTIC CRACKING OF HYDROCARBONS
AT364745B (en) * 1975-03-24 1981-11-10 Ashland Oil Inc METHOD AND DEVICE FOR SEPARATING FINE SOLID PARTICLES FROM FLOWING GASES
US4036740A (en) * 1975-10-28 1977-07-19 Gulf Research & Development Company Hydrocarbon catalytic cracking process
US4162213A (en) * 1976-04-29 1979-07-24 Mobil Oil Corporation Catalytic cracking of metal-contaminated oils
US4162231A (en) * 1977-12-28 1979-07-24 The United States Of America As Represented By The United States Department Of Energy Method for recovering palladium and technetium values from nuclear fuel reprocessing waste solutions

Also Published As

Publication number Publication date
GB2063293B (en) 1983-12-21
EG15396A (en) 1991-12-30
FR2470790A1 (en) 1981-06-12
FR2470790B1 (en) 1988-08-12
DE3043107A1 (en) 1981-09-10
AU542322B2 (en) 1985-02-21
DE3043107C2 (en) 1989-07-20
NO162247C (en) 1989-11-29
NO162247B (en) 1989-08-21
GB2063293A (en) 1981-06-03
YU290480A (en) 1983-12-31
IL61490A (en) 1984-04-30
ATA558980A (en) 1983-06-15
IT8050154A0 (en) 1980-11-13
IN155032B (en) 1984-12-22
AU6439380A (en) 1981-05-21
YU42708B (en) 1988-12-31
BR8007424A (en) 1981-05-26
CA1175770A (en) 1984-10-09
MX160516A (en) 1990-03-15
AT373616B (en) 1984-02-10
IT1142187B (en) 1986-10-08
NO803424L (en) 1981-05-15
ES497232A0 (en) 1981-10-16

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