AT238859B - Kontinuierliches Verfahren zum Kracken eines Kohlenwasserstoffbeschickungsstromes - Google Patents

Kontinuierliches Verfahren zum Kracken eines Kohlenwasserstoffbeschickungsstromes

Info

Publication number
AT238859B
AT238859B AT855062A AT855062A AT238859B AT 238859 B AT238859 B AT 238859B AT 855062 A AT855062 A AT 855062A AT 855062 A AT855062 A AT 855062A AT 238859 B AT238859 B AT 238859B
Authority
AT
Austria
Prior art keywords
cracking
feed stream
continuous process
hydrocarbon feed
hydrocarbon
Prior art date
Application number
AT855062A
Other languages
German (de)
English (en)
Original Assignee
Universal Oil Prod Co
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 Universal Oil Prod Co filed Critical Universal Oil Prod Co
Application granted granted Critical
Publication of AT238859B publication Critical patent/AT238859B/de

Links

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
    • 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
    • B01J8/38—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 fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it
    • B01J8/384—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 fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only
    • B01J8/388—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 fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only externally, i.e. the particles leaving the vessel and subsequently re-entering it
    • 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
    • C10G11/187—Controlling or regulating

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)
AT855062A 1962-06-29 1962-10-29 Kontinuierliches Verfahren zum Kracken eines Kohlenwasserstoffbeschickungsstromes AT238859B (de)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US206271A US3161583A (en) 1962-06-29 1962-06-29 Fluid catalytic cracking of hydrocarbons

Publications (1)

Publication Number Publication Date
AT238859B true AT238859B (de) 1965-03-10

Family

ID=22765666

Family Applications (1)

Application Number Title Priority Date Filing Date
AT855062A AT238859B (de) 1962-06-29 1962-10-29 Kontinuierliches Verfahren zum Kracken eines Kohlenwasserstoffbeschickungsstromes

Country Status (10)

Country Link
US (1) US3161583A (fr)
AT (1) AT238859B (fr)
BE (1) BE623712A (fr)
CH (1) CH446283A (fr)
DE (1) DE1202925B (fr)
ES (1) ES282531A1 (fr)
FR (1) FR1359156A (fr)
GB (1) GB971966A (fr)
NL (1) NL283942A (fr)
OA (1) OA00545A (fr)

Families Citing this family (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3206393A (en) * 1964-11-24 1965-09-14 Universal Oil Prod Co Fluid catalytic cracking of hydrocarbons
US3494858A (en) * 1967-11-17 1970-02-10 Exxon Research Engineering Co Two-stage countercurrent catalyst regenerator
GB1434111A (en) * 1972-06-29 1976-05-05 Texaco Development Corp Continuous fluidised catalytic cracking process
US4217243A (en) * 1976-04-30 1980-08-12 Phillips Petroleum Company Catalyst regenerator control
US4149963A (en) * 1977-09-28 1979-04-17 Phillips Petroleum Company Control of afterburning in catalytic cracking
US4356082A (en) * 1980-12-18 1982-10-26 Mobil Oil Corporation Heat balance in FCC process
US4411773A (en) * 1980-12-18 1983-10-25 Mobil Oil Corporation Heat balance in FCC process and apparatus with downflow reactor riser
US4780195A (en) * 1983-07-25 1988-10-25 Ashland Oil, Inc. Addition of water to regeneration air
US6114265A (en) * 1994-03-15 2000-09-05 Exxon Research And Engineering Company Combustion control in a fluid catalytic cracking regenerator
EP0931587A1 (fr) 1998-01-08 1999-07-28 Evc Technology Ag Catalyseur, procédé pour sa préparation et son utilisation pour la synthèse de 1,2-dichlorétane
US20040104149A1 (en) * 1999-08-20 2004-06-03 Lomas David A. Controllable volume reactor and process
US7169293B2 (en) * 1999-08-20 2007-01-30 Uop Llc Controllable space velocity reactor and process
EP1572343B1 (fr) 2002-12-20 2015-01-14 Uop Llc Reacteur et procede permettant une regulation de temps de sejour variable dans une zone de reaction fluidisee
CN1819870B (zh) * 2002-12-20 2010-12-08 环球油品公司 带有停留时间控制的流化床反应器
US8932452B2 (en) 2012-01-11 2015-01-13 Cameron International Corporation Method for separating entrained catalyst and catalyst fines from slurry oil
CN115739059B (zh) * 2022-12-29 2024-03-19 安徽国孚环境科技股份有限公司 一种废硅油胶的脱附再生装置

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2445351A (en) * 1941-12-27 1948-07-20 Standard Oil Dev Co Process of adding heat in the regeneration of catalyst for the conversion of hydrocarbons
US2409751A (en) * 1943-12-22 1946-10-22 Universal Oil Prod Co Catalytic conversion of hydrocarbons
US2414002A (en) * 1944-02-28 1947-01-07 Universal Oil Prod Co Regeneration of subdivided solid contact material
US2891001A (en) * 1953-12-14 1959-06-16 Kellogg M W Co Fluidized hydrocarbon conversion system with an improved regenerator distributor
DE1010683B (de) * 1954-11-08 1957-06-19 Otto & Co Gmbh Dr C Verfahren zur thermischen Spaltung von Kohlenwasserstoffen

Also Published As

Publication number Publication date
NL283942A (fr)
ES282531A1 (es) 1963-06-16
OA00545A (fr) 1966-07-15
BE623712A (fr)
FR1359156A (fr) 1964-04-24
CH446283A (de) 1967-11-15
GB971966A (en) 1964-10-07
US3161583A (en) 1964-12-15
DE1202925B (de) 1965-10-14

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