DK0726929T3 - Fremgangsmåde og reaktor til katalytisk reformering - Google Patents

Fremgangsmåde og reaktor til katalytisk reformering

Info

Publication number
DK0726929T3
DK0726929T3 DK94927550T DK94927550T DK0726929T3 DK 0726929 T3 DK0726929 T3 DK 0726929T3 DK 94927550 T DK94927550 T DK 94927550T DK 94927550 T DK94927550 T DK 94927550T DK 0726929 T3 DK0726929 T3 DK 0726929T3
Authority
DK
Denmark
Prior art keywords
pct
reactor
catalytic reforming
hydrocarbons
sec
Prior art date
Application number
DK94927550T
Other languages
Danish (da)
English (en)
Inventor
Michael Grigorjewitsch Lapunow
Walerie Iwanowitsch Abramow
Volker Sommerfeld
Aleksander Petrowit Puschkarew
Peter Wasiliewitsc Bolsewitsch
Original Assignee
Michael Grigorjewitsch Lapunow
Walerie Iwanowitsch Abramow
Volker Sommerfeld
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 Michael Grigorjewitsch Lapunow, Walerie Iwanowitsch Abramow, Volker Sommerfeld filed Critical Michael Grigorjewitsch Lapunow
Application granted granted Critical
Publication of DK0726929T3 publication Critical patent/DK0726929T3/da

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
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/0207—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal
    • B01J8/0214—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal in a cylindrical annular shaped bed
    • 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
    • C10G35/00—Reforming naphtha
    • C10G35/04—Catalytic reforming
    • Y—GENERAL 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
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S585/00—Chemistry of hydrocarbon compounds
    • Y10S585/919—Apparatus considerations
    • Y10S585/921—Apparatus considerations using recited apparatus structure
    • Y—GENERAL 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
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S585/00—Chemistry of hydrocarbon compounds
    • Y10S585/919—Apparatus considerations
    • Y10S585/921—Apparatus considerations using recited apparatus structure
    • Y10S585/922—Reactor fluid manipulating device
    • Y—GENERAL 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
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S585/00—Chemistry of hydrocarbon compounds
    • Y10S585/919—Apparatus considerations
    • Y10S585/921—Apparatus considerations using recited apparatus structure
    • Y10S585/924—Reactor shape or disposition

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)
DK94927550T 1994-09-02 1994-09-02 Fremgangsmåde og reaktor til katalytisk reformering DK0726929T3 (da)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/EP1994/002932 WO1996007712A1 (fr) 1994-09-02 1994-09-02 Procede de reformage catalytique et reacteur

Publications (1)

Publication Number Publication Date
DK0726929T3 true DK0726929T3 (da) 2000-05-29

Family

ID=8165884

Family Applications (1)

Application Number Title Priority Date Filing Date
DK94927550T DK0726929T3 (da) 1994-09-02 1994-09-02 Fremgangsmåde og reaktor til katalytisk reformering

Country Status (11)

Country Link
US (1) US5885442A (fr)
EP (1) EP0726929B1 (fr)
JP (1) JP3761195B2 (fr)
AT (1) ATE186941T1 (fr)
AU (1) AU7693594A (fr)
DE (1) DE59408954D1 (fr)
DK (1) DK0726929T3 (fr)
ES (1) ES2142957T3 (fr)
GR (1) GR3032758T3 (fr)
PT (1) PT726929E (fr)
WO (1) WO1996007712A1 (fr)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6245303B1 (en) * 1998-01-14 2001-06-12 Arthur D. Little, Inc. Reactor for producing hydrogen from hydrocarbon fuels
US6413487B1 (en) * 2000-06-02 2002-07-02 The Board Of Regents Of The University Of Oklahoma Method and apparatus for producing carbon nanotubes
US6773580B2 (en) 2001-12-11 2004-08-10 Corning Incorporated Catalytic reforming system and process
US7128775B2 (en) * 2004-05-12 2006-10-31 Praxair Technology, Inc. Radial bed flow distributor for radial pressure adsorber vessel
DE102006060507A1 (de) * 2006-12-19 2008-06-26 Basf Se Reaktor zur Durchführung einer Reaktion zwischen zwei fluiden Edukten an einem Katalysatorbett mit Vorvermischen der fluiden Edukte in einer Einmischvorrichtung
CN102489223A (zh) * 2011-12-16 2012-06-13 南京大学 一种液流强化浸没式固定床反应器
RU2672752C1 (ru) * 2015-06-25 2018-11-19 Юоп Ллк Сужающиеся трубчатые каналы для реакторов

Family Cites Families (28)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2315208A (en) * 1941-10-15 1943-03-30 Universal Oil Prod Co Catalytic apparatus
US2614033A (en) * 1949-04-26 1952-10-14 Gulf Oil Corp Hydrodesulfurization reactor
US2886517A (en) * 1954-05-06 1959-05-12 Kellogg M W Co Method and apparatus for catalytic reactions
BE562525A (fr) * 1956-11-22
US2997374A (en) * 1958-03-13 1961-08-22 California Research Corp Radial flow reactor
US3027244A (en) * 1959-02-09 1962-03-27 Union Oil Co Radial flow catalytic reactor
US3051561A (en) * 1959-05-14 1962-08-28 Standard Oil Co Radial flow reactor
US3067129A (en) * 1960-04-13 1962-12-04 Exxon Research Engineering Co Hydroforming with increments of highly active catalyst
US3249405A (en) * 1962-01-31 1966-05-03 Phillips Petroleum Co Catalytic reforming apparatus
US3475508A (en) * 1967-12-14 1969-10-28 Badger Co Dehydrogenation of alkyl aromatic compounds in the presence of nickelbearing alloy steels
US3751232A (en) * 1971-01-14 1973-08-07 Universal Oil Prod Co Means for effecting a multiple stage contact of a reactant stream
BE792236A (fr) * 1971-12-17 1973-06-01 Inst Francais Du Petrole Appareil pour la conversion d'hydrocarbures
US3799866A (en) * 1972-10-18 1974-03-26 Universal Oil Prod Co Hydrocarbon conversion process utilizing a moving bed reactor
US4040794A (en) * 1975-10-24 1977-08-09 Uop Inc. Moving bed contacting process and apparatus
FR2427378A1 (fr) * 1978-05-29 1979-12-28 Inst Francais Du Petrole Appareil pour la conversion d'hydrocarbures
US4244922A (en) * 1978-09-05 1981-01-13 Chevron Research Company Hold-down device for vertically movable member in apparatus which contains contact material
US4374094A (en) * 1981-10-29 1983-02-15 Chevron Research Company Method and apparatus for uniform flow through radial reactor centerpipes
US4374095A (en) * 1981-10-29 1983-02-15 Chevron Research Company Method and apparatus for restraining radial flow catalytic reactor centerpipes
US4421723A (en) * 1982-07-20 1983-12-20 Chevron Research Company Method and apparatus for supporting radial reactor centerpipes to accommodate thermal cycling
US4452761A (en) * 1982-07-30 1984-06-05 Chevron Research Company Method and apparatus for restraining lifting of radial reactor centerpipes
US4478793A (en) * 1982-09-22 1984-10-23 Uop Inc. Radial flow reactor with operating temperature profile
SU1524913A1 (ru) * 1988-01-29 1989-11-30 МГУ им.М.В.Ломоносова Радиальный химический реактор
US4869808A (en) * 1988-04-01 1989-09-26 Uop Hydrocarbon conversion process with radial flow and controlled hydrogen addition
FR2633635B1 (fr) * 1988-06-29 1993-05-07 Inst Francais Du Petrole Procede de reformage catalytique avec circulation d'un fluide caloporteur dans une pluralite d'espaces internes creux
SU1729565A1 (ru) * 1990-01-09 1992-04-30 Научно-производственное объединение "Ярсинтез" Реактор
EP0461988B1 (fr) * 1990-06-15 1994-01-05 Institut Francais Du Petrole Reacteur avec une paroi inferieure et/ou une paroi superieure comportant une couche d'un materiau souple réfractaire et son utilisation
DE4131446A1 (de) * 1991-09-21 1993-06-09 Basf Ag, 6700 Ludwigshafen, De Reaktor und verfahren zur durchfuehrung heterogenkatalytischer gasphasenreaktionen
US5250270A (en) * 1992-07-17 1993-10-05 The M. W. Kellogg Company Catalytic reactor bed

Also Published As

Publication number Publication date
JP3761195B2 (ja) 2006-03-29
ATE186941T1 (de) 1999-12-15
ES2142957T3 (es) 2000-05-01
AU7693594A (en) 1996-03-27
GR3032758T3 (en) 2000-06-30
EP0726929A1 (fr) 1996-08-21
WO1996007712A1 (fr) 1996-03-14
US5885442A (en) 1999-03-23
EP0726929B1 (fr) 1999-11-24
DE59408954D1 (de) 1999-12-30
JPH09504826A (ja) 1997-05-13
PT726929E (pt) 2000-05-31

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