BE623712A - - Google Patents

Info

Publication number
BE623712A
BE623712A BE623712DA BE623712A BE 623712 A BE623712 A BE 623712A BE 623712D A BE623712D A BE 623712DA BE 623712 A BE623712 A BE 623712A
Authority
BE
Belgium
Application number
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.)
Publication of BE623712A publication Critical patent/BE623712A/xx

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
    • B01J8/38Chemical 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
    • B01J8/384Chemical 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
    • B01J8/388Chemical 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
    • 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
    • C10G11/187Controlling 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)
BE623712D 1962-06-29 BE623712A (US07179912-20070220-C00144.png)

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
BE623712A true BE623712A (US07179912-20070220-C00144.png)

Family

ID=22765666

Family Applications (1)

Application Number Title Priority Date Filing Date
BE623712D BE623712A (US07179912-20070220-C00144.png) 1962-06-29

Country Status (10)

Country Link
US (1) US3161583A (US07179912-20070220-C00144.png)
AT (1) AT238859B (US07179912-20070220-C00144.png)
BE (1) BE623712A (US07179912-20070220-C00144.png)
CH (1) CH446283A (US07179912-20070220-C00144.png)
DE (1) DE1202925B (US07179912-20070220-C00144.png)
ES (1) ES282531A1 (US07179912-20070220-C00144.png)
FR (1) FR1359156A (US07179912-20070220-C00144.png)
GB (1) GB971966A (US07179912-20070220-C00144.png)
NL (1) NL283942A (US07179912-20070220-C00144.png)
OA (1) OA00545A (US07179912-20070220-C00144.png)

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
US4411773A (en) * 1980-12-18 1983-10-25 Mobil Oil Corporation Heat balance in FCC process and apparatus with downflow reactor riser
US4356082A (en) * 1980-12-18 1982-10-26 Mobil Oil Corporation Heat balance in FCC process
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 (en) 1998-01-08 1999-07-28 Evc Technology Ag Catalyst, process for its preparation, and its use in the synthesis of 1,2-dichloroethane
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
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
EP1572343B1 (en) 2002-12-20 2015-01-14 Uop Llc Fluidized bed reactor with residence time control
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
US3161583A (en) 1964-12-15
CH446283A (de) 1967-11-15
AT238859B (de) 1965-03-10
NL283942A (US07179912-20070220-C00144.png)
OA00545A (fr) 1966-07-15
GB971966A (en) 1964-10-07
FR1359156A (fr) 1964-04-24
DE1202925B (de) 1965-10-14
ES282531A1 (es) 1963-06-16

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