NO20030371L - A reactor comprising a packed layer of supported catalyst or supported catalyst precursor, and an application of the reactor - Google Patents

A reactor comprising a packed layer of supported catalyst or supported catalyst precursor, and an application of the reactor

Info

Publication number
NO20030371L
NO20030371L NO20030371A NO20030371A NO20030371L NO 20030371 L NO20030371 L NO 20030371L NO 20030371 A NO20030371 A NO 20030371A NO 20030371 A NO20030371 A NO 20030371A NO 20030371 L NO20030371 L NO 20030371L
Authority
NO
Norway
Prior art keywords
reactor
supported catalyst
packed layer
catalyst precursor
catalyst
Prior art date
Application number
NO20030371A
Other languages
Norwegian (no)
Other versions
NO20030371D0 (en
Inventor
Frederik Willem Hendrik Gimpel
Robert Martijn Van Hardeveld
Carolus Matthias Anna Mesters
Gerardus Petrus Lambert Niesen
Franciscus Johannes Schrauwen
Guy Lode Magda Maria Verbist
Original Assignee
Shell Int Research
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 Shell Int Research filed Critical Shell Int Research
Publication of NO20030371D0 publication Critical patent/NO20030371D0/en
Publication of NO20030371L publication Critical patent/NO20030371L/en

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
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02—Impregnation, coating or precipitation
    • B01J37/0215—Coating
    • B01J37/0225—Coating of metal substrates
    • 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
    • B01J12/00—Chemical processes in general for reacting gaseous media with gaseous media; Apparatus specially adapted therefor
    • B01J12/007—Chemical processes in general for reacting gaseous media with gaseous media; Apparatus specially adapted therefor in the presence of catalytically active bodies, e.g. porous plates
    • 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/889—Manganese, technetium or rhenium
    • B01J23/8892—Manganese
    • 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
    • B01J8/008—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
    • 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
    • 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
    • C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
    • C10G2/30—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
    • C10G2/32—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts
    • C10G2/34—Apparatus, reactors
    • C10G2/341—Apparatus, reactors with stationary catalyst bed
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00796—Details of the reactor or of the particulate material
    • B01J2208/00805—Details of the particulate material

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Hydrogen, Water And Hydrids (AREA)

Abstract

En reaktor som omfatter et pakket lag av båren katalysator eller båren katalysator- forløper, hvor den bårne katalysator eller den bårne katalysatorforløper omfatter en ekstern overflate som omfatter et katalytisk aktivt metall eller en forløperforbindelse for dette, og det pakkede lag har et tomromsinnhold av mer enn 50 volum% og et spesifikt overflateareal av mer enn 10 cm/cmhvilket er beregnet som det samlede eksterne overflateareal til partiklene i forhold til lagvolumet; anvendelsen av den nevnte reaktor i en kjemisk omvandlingsprosess; en fremgangsmåte for fremstilling av hydrokarboner fra syntesegass, omfattende at en blanding av karbonmonoksid og hydrogen bringes i kontakt i den nevnte reaktor, idet det forstås at det katalytisk aktive metall er et metall fra gruppe Vin som i det minste delvis er til stede i metallisk form; et pakket lag av katalysatorpartikler eller. katalysatorforløperpartikler; og en katalysatorpartikkel eller katalysatorforløperpartikkel.A reactor comprising a packed layer of supported catalyst or supported catalyst precursor, wherein the supported catalyst or supported catalyst precursor comprises an external surface comprising a catalytically active metal or a precursor compound therefor, and the packed layer has a void content of more than 50% by volume and a specific surface area of more than 10 cm / cm which is calculated as the total external surface area of the particles in relation to the layer volume; the use of said reactor in a chemical conversion process; a process for the preparation of hydrocarbons from synthesis gas, comprising contacting a mixture of carbon monoxide and hydrogen in said reactor, it being understood that the catalytically active metal is a metal from group Vin which is at least partially present in metallic form ; a packed layer of catalyst particles or. catalyst precursor particles; and a catalyst particle or catalyst precursor particle.

NO20030371A 2000-07-25 2003-01-24 A reactor comprising a packed layer of supported catalyst or supported catalyst precursor, and an application of the reactor NO20030371L (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP00306331 2000-07-25
PCT/EP2001/008019 WO2002007872A1 (en) 2000-07-25 2001-07-11 A reactor comprising a packed bed of supported catalyst or supported catalyst precursor, and a use of the reactor

Publications (2)

Publication Number Publication Date
NO20030371D0 NO20030371D0 (en) 2003-01-24
NO20030371L true NO20030371L (en) 2003-03-20

Family

ID=8173146

Family Applications (1)

Application Number Title Priority Date Filing Date
NO20030371A NO20030371L (en) 2000-07-25 2003-01-24 A reactor comprising a packed layer of supported catalyst or supported catalyst precursor, and an application of the reactor

Country Status (12)

Country Link
EP (1) EP1303348A1 (en)
AR (1) AR029961A1 (en)
AU (2) AU2001287603B2 (en)
CA (1) CA2416459A1 (en)
DZ (1) DZ3395A1 (en)
MX (1) MXPA03000662A (en)
MY (1) MY124803A (en)
NO (1) NO20030371L (en)
NZ (1) NZ523660A (en)
RU (1) RU2273515C2 (en)
WO (1) WO2002007872A1 (en)
ZA (1) ZA200300334B (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6451864B1 (en) * 1999-08-17 2002-09-17 Battelle Memorial Institute Catalyst structure and method of Fischer-Tropsch synthesis
AU778040B2 (en) 1999-08-17 2004-11-11 Battelle Memorial Institute Catalyst structure and method of fischer-tropsch synthesis
AR061824A1 (en) * 2006-07-10 2008-09-24 Shell Int Research METHOD FOR SUPPORTING A HYDROCARBON SYNTHESIS CATALYST MATERIAL
US8497224B2 (en) 2009-12-16 2013-07-30 Shell Oil Company Process for preparing a catalyst substrate
EP2338592A1 (en) * 2009-12-16 2011-06-29 Shell Internationale Research Maatschappij B.V. Process for manufacturing a catalyst substrate comprising non-woven fibers
JP5615058B2 (en) * 2010-06-29 2014-10-29 バブコック日立株式会社 Method for producing metal substrate for exhaust gas denitration catalyst
EP2463027A1 (en) * 2010-12-08 2012-06-13 Shell Internationale Research Maatschappij B.V. Method for the manufacture of a coated fibrous structure and a catalyst therefrom
WO2018078082A1 (en) * 2016-10-27 2018-05-03 Shell Internationale Research Maatschappij B.V. A process for producing hydrocarbons

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3167600A (en) * 1960-09-13 1965-01-26 Robert G Worman Packing material
DE2818680A1 (en) * 1978-04-27 1979-10-31 Bayer Ag PROCESS FOR PROCESSING WASTE CONTAINING NITRO-HYDROXY AROMATES
EP0055535A1 (en) * 1980-12-31 1982-07-07 Imperial Chemical Industries Plc Fluid purification
DE3272205D1 (en) * 1981-12-21 1986-08-28 Ici Plc Process for steam reforming a hydrocarbon feedstock and catalyst therefor
JPH084749B2 (en) * 1985-01-21 1996-01-24 日本碍子株式会社 Ceramic honeycomb structure
DK156701C (en) * 1987-08-27 1990-01-29 Haldor Topsoe As PROCEDURE FOR IMPLEMENTING Heterogeneous CATALYTIC CHEMICAL REACTIONS
NL1006477C2 (en) * 1997-07-04 1999-01-05 Gastec Nv Reactor and method for carrying out a chemical reaction.
US6302188B1 (en) * 1998-04-28 2001-10-16 Megtec Systems, Inc. Multi-layer heat exchange bed containing structured media and randomly packed media

Also Published As

Publication number Publication date
NZ523660A (en) 2004-07-30
AR029961A1 (en) 2003-07-23
AU2001287603B2 (en) 2004-11-25
WO2002007872A1 (en) 2002-01-31
CA2416459A1 (en) 2002-01-31
MY124803A (en) 2006-07-31
AU8760301A (en) 2002-02-05
DZ3395A1 (en) 2002-01-31
MXPA03000662A (en) 2003-10-15
ZA200300334B (en) 2004-03-31
RU2273515C2 (en) 2006-04-10
EP1303348A1 (en) 2003-04-23
NO20030371D0 (en) 2003-01-24

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