NO20061191L - Fremgangsmate for innforing av en katalysator i en reaktor som er egnet for reaksjoner i heterogen fase - Google Patents

Fremgangsmate for innforing av en katalysator i en reaktor som er egnet for reaksjoner i heterogen fase

Info

Publication number
NO20061191L
NO20061191L NO20061191A NO20061191A NO20061191L NO 20061191 L NO20061191 L NO 20061191L NO 20061191 A NO20061191 A NO 20061191A NO 20061191 A NO20061191 A NO 20061191A NO 20061191 L NO20061191 L NO 20061191L
Authority
NO
Norway
Prior art keywords
catalyst
introducing
phase reactions
heterogeneous phase
reactor suitable
Prior art date
Application number
NO20061191A
Other languages
English (en)
Other versions
NO343243B1 (no
Inventor
Giovanni Pederzani
Christina Maretto
Original Assignee
Enitecnologie Spa
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 Enitecnologie Spa filed Critical Enitecnologie Spa
Publication of NO20061191L publication Critical patent/NO20061191L/no
Publication of NO343243B1 publication Critical patent/NO343243B1/no

Links

Classifications

    • 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
    • C10G2/00Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
    • C10G2/30Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
    • C10G2/32Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts
    • C10G2/33Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts characterised by the catalyst used
    • 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
    • C10G2/00Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
    • 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
    • B01J8/0015Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
    • 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
    • B01J8/20Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
    • B01J8/22Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
    • 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
    • C10G2/00Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
    • C10G2/30Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
    • C10G2/32Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts
    • C10G2/34Apparatus, reactors
    • C10G2/342Apparatus, reactors with moving solid catalysts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00743Feeding or discharging of solids
    • B01J2208/00752Feeding
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00743Feeding or discharging of solids
    • B01J2208/00769Details of feeding or discharging
    • B01J2208/00787Bringing the solid in the form of a slurry before feeding it to the reactor
    • 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
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/70Catalyst aspects

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

Fremgangsmåte for tilførsel av en katalysator og for drift av en reaktor hvori reaksjoner finner sted i flerfase-systemer, hvori en gass-fase som hovedsakelig består av CO og Hbobles inn i en suspensjon av et faststoff i form av partikler (katalysator) i en væske (vanligvis reaksjonsprodukt), i henhold til Fischer-Tropsch teknologien.
NO20061191A 2003-09-18 2006-03-14 Fremgangsmåte for tilførselen av en katalysator i en bobletårnslurryreaktor i oppstartsfasen. NO343243B1 (no)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
IT001776A ITMI20031776A1 (it) 2003-09-18 2003-09-18 Procedimento per il caricamento di un catalizzatore in un reattore adatto a reazioni in fase eterogenea
PCT/EP2004/010650 WO2005026293A1 (en) 2003-09-18 2004-09-17 Process for the charging of a catalyst into a reactor suitable for reactions in heterogeneous phase

Publications (2)

Publication Number Publication Date
NO20061191L true NO20061191L (no) 2006-06-15
NO343243B1 NO343243B1 (no) 2018-12-17

Family

ID=34308103

Family Applications (1)

Application Number Title Priority Date Filing Date
NO20061191A NO343243B1 (no) 2003-09-18 2006-03-14 Fremgangsmåte for tilførselen av en katalysator i en bobletårnslurryreaktor i oppstartsfasen.

Country Status (13)

Country Link
US (1) US7579382B2 (no)
EP (2) EP1820838B9 (no)
CN (2) CN101230287B (no)
AT (1) ATE400628T1 (no)
AU (2) AU2004272745B2 (no)
CY (1) CY1115506T1 (no)
DE (1) DE602004014947D1 (no)
EA (1) EA009488B1 (no)
EG (2) EG26146A (no)
ES (2) ES2309552T3 (no)
IT (1) ITMI20031776A1 (no)
NO (1) NO343243B1 (no)
WO (1) WO2005026293A1 (no)

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
MY145762A (en) * 2005-12-09 2012-04-13 Shell Int Research Method to start a process for producing hydrocarbons from synthesis gas
BRPI0619491A2 (pt) 2005-12-09 2011-10-04 Shell Int Research método para iniciar um processo em estado estacionário para produzir hidrocarbonetos a partir de gás de sìntese
US7855235B2 (en) 2005-12-09 2010-12-21 Shell Oil Company Method to start a process for producing hydrocarbons from synthesis gas
US7544719B2 (en) * 2006-07-12 2009-06-09 Rentech, Inc. Method for activating an iron-based fischer-tropsch catalyst
JP5119412B2 (ja) * 2007-12-19 2013-01-16 独立行政法人石油天然ガス・金属鉱物資源機構 ワックス留分貯蔵タンクの管理方法
EP2366001A1 (en) * 2008-12-16 2011-09-21 Shell Internationale Research Maatschappij B.V. High-speed stop in a fischer-tropsch process
WO2010063850A1 (en) * 2008-12-16 2010-06-10 Shell Internationale Research Maatschappij B.V. High-speed stop in a fischer-tropsch process
BRPI0923094B1 (pt) 2008-12-16 2017-11-07 Shell Internacionale Research Maatschappij B.V. "process for performing a high speed interruption in a fischer-tropsch process"
GB0919182D0 (en) * 2009-11-03 2009-12-16 Compactgtl Plc Catalytic reactor treatment process
CN102161609B (zh) * 2010-02-24 2013-06-26 中国石油化工股份有限公司 一种固定床费托合成工艺的停工方法
AU2014363104B2 (en) 2013-12-11 2017-12-07 Sasol Technology Proprietary Limited A method of shutting down an operating three-phase slurry bubble column reactor
GB2554618B (en) * 2015-06-12 2021-11-10 Velocys Inc Synthesis gas conversion process
FR3044565B1 (fr) * 2015-12-08 2017-12-01 Ifp Energies Now Chargement d'un catalyseur dans une colonne a bulles pour la synthese fischer-tropsch

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003068715A1 (en) * 2002-02-13 2003-08-21 Sasol Technology (Proprietary) Limited Process for starting up a fischer-tropsch reactor

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6307119B1 (en) 1999-06-15 2001-10-23 Kimberly-Clark Worldwide, Inc. Absorbent articles having wetness indicating graphics incorporating a training zone

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003068715A1 (en) * 2002-02-13 2003-08-21 Sasol Technology (Proprietary) Limited Process for starting up a fischer-tropsch reactor

Also Published As

Publication number Publication date
WO2005026293A1 (en) 2005-03-24
ES2494844T3 (es) 2014-09-16
EP1820838B1 (en) 2014-05-28
AU2010201932A1 (en) 2010-06-03
AU2004272745B2 (en) 2010-05-20
EG25400A (en) 2011-12-27
US20070066690A1 (en) 2007-03-22
ES2309552T3 (es) 2008-12-16
EP1820838B9 (en) 2014-09-03
CY1115506T1 (el) 2017-01-04
CN101230287B (zh) 2012-09-05
EP1664241A1 (en) 2006-06-07
CN101230287A (zh) 2008-07-30
CN100379840C (zh) 2008-04-09
EP1820838A2 (en) 2007-08-22
WO2005026293A8 (en) 2006-03-30
NO343243B1 (no) 2018-12-17
CN1852965A (zh) 2006-10-25
AU2004272745A8 (en) 2010-04-22
US7579382B2 (en) 2009-08-25
EP1664241B1 (en) 2008-07-09
AU2004272745A1 (en) 2005-03-24
ITMI20031776A1 (it) 2005-03-19
EA200600413A1 (ru) 2006-08-25
EA009488B1 (ru) 2008-02-28
ATE400628T1 (de) 2008-07-15
AU2010201932B2 (en) 2012-07-12
EP1820838A3 (en) 2008-03-05
DE602004014947D1 (de) 2008-08-21
EG26146A (en) 2013-03-27

Similar Documents

Publication Publication Date Title
NO20061191L (no) Fremgangsmate for innforing av en katalysator i en reaktor som er egnet for reaksjoner i heterogen fase
NO20061188L (no) Fremgangsmate for a drive en reaktor som er egnet for heterogene reaksjoner kombinert med reaksjoner som finner sted i trefase-systemer
MY139227A (en) Partial dehydrogenation method using continuous heterogeneous catalysis
TW200708675A (en) Reactor sealing methods
NO20063528L (no) Reaktor-regenerator-anordning og dens anvendelse i produksjonen av styren
Kathe et al. Modularization strategy for syngas generation in chemical looping methane reforming systems with CO2 as feedstock
CA2314332A1 (en) Gas conversion using hydrogen from synthesis gas and hydroconversion tail gas
MXPA05009912A (es) Proceso de hidroconversion de una carga pesada con un catalizador disperso.
AU2003300361A1 (en) Reactor with a filter for fixed-bed catalysts
NO20083063L (no) Fremgangsmate for oppstarting av en prosess for fremstilling av hydrokarboner fra syntesegass
MY147936A (en) Charging of a reactor
FR2879213B1 (fr) Enchainement de procedes d'hydroconversion et de reformage a la vapeur en vue d'optimiser la production d'hydrogene sur sur des champs de production
WO2009008423A1 (ja) エポキシ化合物の製造装置および製造方法
MX2007012405A (es) Metodo para la produccion continua de metilmercaptano.
EG25431A (en) Process for the production in the continuous of hydrocarbons from synthesis gas, in slurry reactors and for the separation from the solid phase of theliquid phase produced
BR0317831A (pt) Método para transição de um catalisador para um catalisador incompatìvel em um reator de fase gasosa
TW200628461A (en) Improved seal swell agent and process therefor
DE502004006576D1 (de) Verfahren der heterogen katalysierten partiellen gasphasenoxidation von propen zu acrylsäure
WO2002096834A3 (en) Fischer-tropsch process
MY134279A (en) Process for the production of hydrocarbons from gaseous hydrocarbonaceous feed
GB0112797D0 (en) Process
AR023295A1 (es) Proceso para la puesta en marcha de un proceso de polimerizacion y proceso de polimerizacion
Yoshida et al. Ring Size‐Selective Ring‐Closing Olefin Metathesis: Taking Advantage of the Deleterious Effect of Ethylene Gas
MY166759A (en) Monitoring, control and/or regulation of reactions of a fluid reaction mixture in a reactor having thermoplates
TR200300978T2 (tr) Oksidasyon reaktörünün üretim kapasitesini arttırma yöntemi.

Legal Events

Date Code Title Description
CHAD Change of the owner's name or address (par. 44 patent law, par. patentforskriften)

Owner name: ENI SPA, FR