PE20141999A1 - Proceso para la produccion de por lo menos un producto a partir de por lo menos un reactivo gaseoso en un lecho de suspension - Google Patents

Proceso para la produccion de por lo menos un producto a partir de por lo menos un reactivo gaseoso en un lecho de suspension

Info

Publication number
PE20141999A1
PE20141999A1 PE2013002712A PE2013002712A PE20141999A1 PE 20141999 A1 PE20141999 A1 PE 20141999A1 PE 2013002712 A PE2013002712 A PE 2013002712A PE 2013002712 A PE2013002712 A PE 2013002712A PE 20141999 A1 PE20141999 A1 PE 20141999A1
Authority
PE
Peru
Prior art keywords
product
gaseous
suspension
reagent
gaseous reagent
Prior art date
Application number
PE2013002712A
Other languages
English (en)
Inventor
Berthold Berend Breman
Original Assignee
Sasol Technology Propietary Ltd
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 Sasol Technology Propietary Ltd filed Critical Sasol Technology Propietary Ltd
Publication of PE20141999A1 publication Critical patent/PE20141999A1/es

Links

Classifications

    • 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
    • C10G2/342—Apparatus, reactors with moving solid catalysts
    • C10G2/344—Apparatus, reactors with moving solid catalysts according to the "fluidised-bed" technique
    • 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
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/20—Chemical 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
    • B01J8/22—Chemical 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
    • 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
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1818—Feeding of the fluidising gas
    • B01J8/1827—Feeding of the fluidising gas the fluidising gas being a reactant
    • 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
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1836—Heating and cooling the reactor
    • 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
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24—Chemical 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
    • B01J8/26—Chemical 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 two or more fluidised beds, e.g. reactor and regeneration installations
    • B01J8/28—Chemical 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 two or more fluidised beds, e.g. reactor and regeneration installations the one above the other
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
    • C07C1/02—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon
    • C07C1/04—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon from carbon monoxide with hydrogen
    • C07C1/0455—Reaction conditions
    • 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
    • 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
    • C10G2/33—Production 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
    • C10G2/331—Production 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 containing group VIII-metals
    • C10G2/332—Production 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 containing group VIII-metals of the iron-group
    • 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
    • C10G2/342—Apparatus, reactors with moving solid catalysts
    • 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
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • B01J2208/00141—Coils
    • 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
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00265—Part of all of the reactants being heated or cooled outside the reactor while recycling
    • B01J2208/00274—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant vapours
    • 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/582—Recycling of unreacted starting or intermediate materials

Abstract

REFERIDA A UN PROCESO PARA LA PRODUCCION DE UN PRODUCTO A PARTIR DE POR LO MENOS UN REACTIVO GASEOSO, EL CUAL COMPRENDE ALIMENTAR DICHO REACTIVO GASEOSO, COMO UNA ALIMENTACION GASEOSA O COMO PARTE DE UNA ALIMENTACION GASEOSA EN UN RECIPIENTE QUE SOSTIENE UN LECHO DE SUSPENSION EXPANDIDO DE PARTICULAS DE CATALIZADOR SOLIDO SUSPENDIDAS EN UN LIQUIDO DE SUSPENSION DE MODO QUE EL REACTIVO GASEOSO PUEDE BURBUJEAR EN FORMA ASCENDENTE A TRAVES DEL LECHO DE SUSPENSION, DONDE EL LECHO DE SUSPENSION TIENE UNA CARGA DE CATALIZADOR INFERIOR A 14% EN VOLUMEN DE SUSPENSION DESGASIFICADA, LUEGO HACER REACCIONAR DICHO REACTIVO GASEOSO EN FORMA CATALITICA A UNA PRESION SUPERIOR A LA PRESION ATMOSFERICA, A MEDIDA QUE EL REACTIVO GASEOSO BURBUJEA EN FORMA ASCENDENTE A TRAVES DEL LECHO DE SUSPENSION PARA PRODUCIR UN PRODUCTO, RETIRAR DICHO PRODUCTO Y CUALQUIER OTRO REACTIVO GASEOSO NO REACCIONADO, DEL RECIPIENTE
PE2013002712A 2011-06-07 2012-05-30 Proceso para la produccion de por lo menos un producto a partir de por lo menos un reactivo gaseoso en un lecho de suspension PE20141999A1 (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US201161493988P 2011-06-07 2011-06-07
ZA201104229 2011-06-07

Publications (1)

Publication Number Publication Date
PE20141999A1 true PE20141999A1 (es) 2014-12-24

Family

ID=47295555

Family Applications (1)

Application Number Title Priority Date Filing Date
PE2013002712A PE20141999A1 (es) 2011-06-07 2012-05-30 Proceso para la produccion de por lo menos un producto a partir de por lo menos un reactivo gaseoso en un lecho de suspension

Country Status (13)

Country Link
US (1) US9080108B2 (es)
CN (1) CN103596674B (es)
AP (1) AP2013007262A0 (es)
AR (1) AR086856A1 (es)
AU (1) AU2012265887B2 (es)
BR (1) BR112013031529B1 (es)
CA (1) CA2838466C (es)
PE (1) PE20141999A1 (es)
PL (1) PL406362A1 (es)
RU (1) RU2583457C2 (es)
UA (1) UA112649C2 (es)
WO (1) WO2012168830A1 (es)
ZA (1) ZA201308769B (es)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2019523702A (ja) * 2016-06-02 2019-08-29 レール・リキード−ソシエテ・アノニム・プール・レテュード・エ・レクスプロワタシオン・デ・プロセデ・ジョルジュ・クロード フィッシャー・トロプシュ法に用いるスラリーバブルカラム反応器
CN110385089A (zh) * 2018-04-20 2019-10-29 国家能源投资集团有限责任公司 浆态床反应器和费托合成的方法

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA2038774C (en) 1990-04-04 2001-09-25 Eric Herbolzheimer Slurry bubble column
GB9203959D0 (en) * 1992-02-25 1992-04-08 Norske Stats Oljeselskap Method of conducting catalytic converter multi-phase reaction
BR9814061B1 (pt) * 1997-10-07 2010-07-13 processo e instalação para produzir produtos lìquidos e gasosos a partir de reagentes gasosos.
US6117814A (en) 1998-02-10 2000-09-12 Exxon Research And Engineering Co. Titania catalysts their preparation and use in fischer-tropsch synthesis
DZ2724A1 (fr) 1998-02-20 2003-09-01 Sasol Tech Pty Ltd Procédé pour la production d'hydrocarbures à partir d'un gaz de synthèse et leurs catalyseurs.
US6262132B1 (en) 1999-05-21 2001-07-17 Energy International Corporation Reducing fischer-tropsch catalyst attrition losses in high agitation reaction systems
FR2806736B1 (fr) 2000-03-27 2002-05-10 Inst Francais Du Petrole Procede de production d'hydrocarbures a partir de gaz de synthese dans un reacteur triphasique
GB0023781D0 (en) * 2000-09-28 2000-11-08 Kvaerner Process Tech Ltd Process
US6914082B2 (en) 2001-12-14 2005-07-05 Conocophillips Company Slurry bubble reactor operated in well-mixed gas flow regime
CA2525007C (en) * 2003-05-16 2012-02-14 Sasol Technology (Proprietary) Limited Process for producing liquid and, optionally, gaseous products from gaseous reactants
US6800664B1 (en) * 2003-05-23 2004-10-05 Conocophillips Company Conjoined reactor system
GB2429714B (en) 2004-05-10 2008-12-17 Sasol Technology The production of liquid and,optionally,gaseous hydrocarbons from gaseous reactants into an expanded slurry bed

Also Published As

Publication number Publication date
RU2013154045A (ru) 2015-07-20
AU2012265887B2 (en) 2016-12-22
US20140107232A1 (en) 2014-04-17
AU2012265887A1 (en) 2014-01-09
PL406362A1 (pl) 2014-11-10
US9080108B2 (en) 2015-07-14
BR112013031529B1 (pt) 2020-11-10
UA112649C2 (uk) 2016-10-10
NZ618392A (en) 2014-12-24
AP2013007262A0 (en) 2013-11-30
CA2838466A1 (en) 2012-12-13
CN103596674B (zh) 2015-12-02
WO2012168830A1 (en) 2012-12-13
CN103596674A (zh) 2014-02-19
ZA201308769B (en) 2014-08-27
BR112013031529A2 (pt) 2016-12-13
CA2838466C (en) 2018-09-18
RU2583457C2 (ru) 2016-05-10
AR086856A1 (es) 2014-01-29

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