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BRPI0606800A2 - reator catalìtico compacto para sìntese fischertropsch, e, planta para converter gás natural em hidrocarbonetos de cadeia mais longa - Google Patents

reator catalìtico compacto para sìntese fischertropsch, e, planta para converter gás natural em hidrocarbonetos de cadeia mais longa

Info

Publication number
BRPI0606800A2
BRPI0606800A2 BRPI0606800-6A BRPI0606800A BRPI0606800A2 BR PI0606800 A2 BRPI0606800 A2 BR PI0606800A2 BR PI0606800 A BRPI0606800 A BR PI0606800A BR PI0606800 A2 BRPI0606800 A2 BR PI0606800A2
Authority
BR
Brazil
Prior art keywords
catalytic reactor
plant
natural gas
multiplicity
reactor
Prior art date
Application number
BRPI0606800-6A
Other languages
English (en)
Inventor
Clive Derek Lee-Tuffnell
Original Assignee
Compactgtl Pic
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 Compactgtl Pic filed Critical Compactgtl Pic
Publication of BRPI0606800A2 publication Critical patent/BRPI0606800A2/pt

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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/248—Reactors comprising multiple separated flow channels
    • B01J19/249—Plate-type reactors
    • 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • 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
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2451—Geometry of the reactor
    • B01J2219/2453—Plates arranged in parallel
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2451—Geometry of the reactor
    • B01J2219/2456—Geometry of the plates
    • B01J2219/2458—Flat plates, i.e. plates which are not corrugated or otherwise structured, e.g. plates with cylindrical shape
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2451—Geometry of the reactor
    • B01J2219/2456—Geometry of the plates
    • B01J2219/2459—Corrugated 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2461—Heat exchange aspects
    • B01J2219/2462—Heat exchange aspects the reactants being in indirect heat exchange with a non reacting heat exchange medium
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2469—Feeding means
    • B01J2219/2471—Feeding means for the catalyst
    • B01J2219/2472—Feeding means for the catalyst the catalyst being exchangeable on inserts other than plates, e.g. in bags
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2476—Construction materials
    • B01J2219/2477—Construction materials of the catalysts
    • B01J2219/2479—Catalysts coated on the surface of plates or inserts
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2476—Construction materials
    • B01J2219/2477—Construction materials of the catalysts
    • B01J2219/2482—Catalytically active foils; Plates having catalytically activity on their own
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2476—Construction materials
    • B01J2219/2483—Construction materials of the plates
    • B01J2219/2485—Metals or alloys
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2491—Other constructional details
    • B01J2219/2492—Assembling means
    • B01J2219/2493—Means for assembling plates together, e.g. sealing means, screws, bolts
    • B01J2219/2495—Means for assembling plates together, e.g. sealing means, screws, bolts the plates being assembled interchangeably or in a disposable way
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2491—Other constructional details
    • B01J2219/2498—Additional structures inserted in the channels, e.g. plates, catalyst holding meshes

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (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)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Hydrogen, Water And Hydrids (AREA)

Abstract

REATOR CATALìTICO COMPACTO PARA SINTESE FISCHER-TROPSCH, E, PLANTA PARA CONVERTER GáS NATURAL EM HIDROCARBONETOS DE CADEIA MAIS LONGA. Um reator catalítico compacto para síntese Fischer-Tropsch define uma multiplicidade de primeiros e segundos canais de escoamento dispostos alternadamente no reator, para transportar uma mistura de gás que sofre síntese Fischer-Tropsch, e um fluido refrigerante, respectivamente. Cada primeiro canal de escoamento contém uma estrutura de catalisador removível, permeável a gás, incorporando um substrato de metal. Uma multiplicidade de canais de escoamento é definida através da estrutura do catalisador, e o volume de vazios, isto é, a proporção de área de seção transversal do primeiro canal de escoamento, constituído pela referida multiplicidade de canais de escoamento, está entre 25% e 75%. Isto proporciona um equilíbrio ótimo entre a produtividade e a seletividade, de modo que a operação do reator pode ser económica e controlável.
BRPI0606800-6A 2005-01-31 2006-01-18 reator catalìtico compacto para sìntese fischertropsch, e, planta para converter gás natural em hidrocarbonetos de cadeia mais longa BRPI0606800A2 (pt)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GBGB0501731.4A GB0501731D0 (en) 2005-01-31 2005-01-31 Catalytic reactor
PCT/GB2006/050011 WO2006079848A1 (en) 2005-01-31 2006-01-18 Catalytic reactor

Publications (1)

Publication Number Publication Date
BRPI0606800A2 true BRPI0606800A2 (pt) 2009-07-14

Family

ID=34259785

Family Applications (1)

Application Number Title Priority Date Filing Date
BRPI0606800-6A BRPI0606800A2 (pt) 2005-01-31 2006-01-18 reator catalìtico compacto para sìntese fischertropsch, e, planta para converter gás natural em hidrocarbonetos de cadeia mais longa

Country Status (19)

Country Link
US (1) US7842256B2 (pt)
EP (1) EP1853379B1 (pt)
JP (1) JP5001177B2 (pt)
KR (1) KR101258223B1 (pt)
CN (1) CN100584446C (pt)
AT (1) ATE424252T1 (pt)
AU (1) AU2006208873B2 (pt)
BR (1) BRPI0606800A2 (pt)
CA (1) CA2595702C (pt)
DE (1) DE602006005471D1 (pt)
DK (1) DK1853379T3 (pt)
EA (1) EA013780B1 (pt)
EG (1) EG24878A (pt)
GB (1) GB0501731D0 (pt)
MX (1) MX2007008996A (pt)
MY (1) MY141997A (pt)
NO (1) NO20073908L (pt)
TW (1) TWI403364B (pt)
WO (1) WO2006079848A1 (pt)

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AU2002349143A1 (en) * 2001-12-05 2003-06-17 GTL Mircosystems AG Process an apparatus for steam-methane reforming
US8497308B2 (en) 2006-09-05 2013-07-30 Velocys, Inc. Integrated microchannel synthesis and separation
US7820725B2 (en) * 2006-09-05 2010-10-26 Velocys, Inc. Integrated microchannel synthesis and separation
EP2111438B1 (en) 2007-01-19 2014-08-06 Velocys, Inc. Process for converting natural gas to higher molecular weight hydrocarbons using microchannel process technology
AU2008306591B2 (en) 2007-10-02 2012-12-06 Compactgtl Limited Gas-to-liquid plant using parallel units
WO2009062681A1 (de) * 2007-11-13 2009-05-22 Basf Se Verbessertes verfahren zur herstellung von blausäure durch katalytische dehydratisierung von gasförmigem formamid
GB0725140D0 (en) * 2007-12-24 2008-01-30 Compactgtl Plc Catalytic Reactor
US8100996B2 (en) 2008-04-09 2012-01-24 Velocys, Inc. Process for upgrading a carbonaceous material using microchannel process technology
EP2282828A2 (en) 2008-04-09 2011-02-16 Velocys, Inc. Process for converting a carbonaceous material to methane, methanol and/or dimethyl ether using microchannel process technology
WO2010042794A2 (en) 2008-10-10 2010-04-15 Velocys Inc. Process and apparatus employing microchannel process technology
JP5581028B2 (ja) * 2009-09-16 2014-08-27 住友精密工業株式会社 触媒反応器
GB201016926D0 (en) * 2010-10-07 2010-11-24 Compactgtl Plc Catalytic reactor and catalyst structure
US20130041050A1 (en) 2011-07-19 2013-02-14 Robert Luzenski Microchannel reactors and fabrication processes
TW201334862A (zh) * 2011-12-19 2013-09-01 Compactgtl Ltd 觸媒結構及催化方法
TWI519470B (zh) * 2012-12-18 2016-02-01 英威達技術有限公司 使用觸媒床製造氰化氫之方法
US9676623B2 (en) 2013-03-14 2017-06-13 Velocys, Inc. Process and apparatus for conducting simultaneous endothermic and exothermic reactions
KR102378451B1 (ko) * 2014-03-21 2022-03-23 쉘 인터내셔날 리써취 마트샤피지 비.브이. 촉매
CN106622057B (zh) * 2015-10-30 2019-02-01 中国石油化工股份有限公司 一种费托合成微反应器和费托合成方法
CN106622056B (zh) * 2015-10-30 2019-02-01 中国石油化工股份有限公司 费托合成反应系统和费托合成方法
CN106622058B (zh) * 2015-10-30 2019-04-16 中国石油化工股份有限公司 一种费托合成反应装置和费托合成方法
FR3068263B1 (fr) * 2017-06-28 2019-10-25 Commissariat A L'energie Atomique Et Aux Energies Alternatives Module de reacteur-echangeur a au moins deux circuits de fluide realise par empilement de plaques, applications aux reactions catalytiques exothermiques ou endothermiques
US11358111B2 (en) * 2019-03-20 2022-06-14 Battelle Memorial Institute, Pacific Northwest National Laboratories Reactor assemblies and methods of performing reactions

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Also Published As

Publication number Publication date
NO20073908L (no) 2007-10-24
DE602006005471D1 (de) 2009-04-16
CN100584446C (zh) 2010-01-27
US20080193347A1 (en) 2008-08-14
AU2006208873A1 (en) 2006-08-03
EA013780B1 (ru) 2010-06-30
WO2006079848A1 (en) 2006-08-03
DK1853379T3 (da) 2009-06-15
KR101258223B1 (ko) 2013-04-25
KR20070102725A (ko) 2007-10-19
AU2006208873B2 (en) 2010-11-25
JP2008528271A (ja) 2008-07-31
EP1853379A1 (en) 2007-11-14
EG24878A (en) 2010-12-01
TWI403364B (zh) 2013-08-01
MY141997A (en) 2010-08-16
ATE424252T1 (de) 2009-03-15
MX2007008996A (es) 2007-09-19
CA2595702A1 (en) 2006-08-03
CA2595702C (en) 2013-07-09
EA200701635A1 (ru) 2007-12-28
EP1853379B1 (en) 2009-03-04
TW200631662A (en) 2006-09-16
CN101151094A (zh) 2008-03-26
JP5001177B2 (ja) 2012-08-15
GB0501731D0 (en) 2005-03-02
US7842256B2 (en) 2010-11-30

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B25D Requested change of name of applicant approved

Owner name: COMPACTGTL LIMITED (GB)

B25G Requested change of headquarter approved

Owner name: COMPACTGTL LIMITED (GB)

B08F Application dismissed because of non-payment of annual fees [chapter 8.6 patent gazette]

Free format text: REFERENTE A 9A ANUIDADE.

B08K Patent lapsed as no evidence of payment of the annual fee has been furnished to inpi [chapter 8.11 patent gazette]

Free format text: REFERENTE AO DESPACHO 8.6 PUBLICADO NA RPI 2289 DE 18/11/2014.