CO5540337A2 - Proceso para convertir gas de sintesis a hidrocarburos liquidos en presencia de un catalizador fischer-tropsch, con mejoramiento de la transferencia de masa y energia en la zona de mezclado con alto esfuerzo de corte - Google Patents

Proceso para convertir gas de sintesis a hidrocarburos liquidos en presencia de un catalizador fischer-tropsch, con mejoramiento de la transferencia de masa y energia en la zona de mezclado con alto esfuerzo de corte

Info

Publication number
CO5540337A2
CO5540337A2 CO03101600A CO03101600A CO5540337A2 CO 5540337 A2 CO5540337 A2 CO 5540337A2 CO 03101600 A CO03101600 A CO 03101600A CO 03101600 A CO03101600 A CO 03101600A CO 5540337 A2 CO5540337 A2 CO 5540337A2
Authority
CO
Colombia
Prior art keywords
synthesis gas
high cutting
suspension
cutting effort
mixing zone
Prior art date
Application number
CO03101600A
Other languages
English (en)
Inventor
Helena Maria Font Friede Josephus Johanes
Hensman John Richard
Newton David
Sharp Christopher
Smith Geoffrey Benedict
Original Assignee
Bp Exploration Operating
Davy Process Techn 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
Priority claimed from GB0112788A external-priority patent/GB0112788D0/en
Priority claimed from GB0112798A external-priority patent/GB0112798D0/en
Priority claimed from GB0112787A external-priority patent/GB0112787D0/en
Priority claimed from GB0112795A external-priority patent/GB0112795D0/en
Priority claimed from GB0113786A external-priority patent/GB0113786D0/en
Application filed by Bp Exploration Operating, Davy Process Techn Ltd filed Critical Bp Exploration Operating
Publication of CO5540337A2 publication Critical patent/CO5540337A2/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
    • 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
    • B01J8/224—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 the particles being subject to a circulatory movement
    • B01J8/228—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 the particles being subject to a circulatory movement externally, i.e. the particles leaving the vessel and subsequently re-entering it
    • 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
    • C07C1/0485—Set-up of reactors or accessories; Multi-step processes
    • 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
    • B01J2208/00132—Tubes
    • 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
    • B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • B01J2208/00256—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles in a heat exchanger for the heat exchange medium separate from 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
    • 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
    • B01J2208/00292—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant solids
    • B01J2208/003—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant solids involving reactant slurries

Landscapes

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

Abstract

1.- Un proceso para la conversión de gas de síntesis a hidrocarburos CARACTERIZADO PORQUE comprende poner en contacto el gas de síntesis a temperatura y presión elevadas con una suspensión que comprende un catalizador en partículas sólidas suspendido en un medio líquido, puesta en contacto que ocurre en un sistema que comprende por lo menos una zona de mezclado de alto esfuerzo de corte y un recipiente de reacción tal que el volumen de suspensión presente en la(s) zona(s) de mezclado con alto esfuerzo de corte es sustancialmente menor del volumen de suspensión presente en el recipiente de reacción, la suspensión se mezcla con gas de síntesis en la(s) zona(s) de mezclado con alto esfuerzo de corte, la mezcla resultante de la suspensión y el gas de síntesis se descarga desde la(s) zona(s) de mezclado con alto esfuerzo de corte en el recipiente de reacción y tal que energía cinética se disipa a la suspensión presente en la(s) zona(s) de mezclado con alto esfuerzo de corte a una tasa de por lo menos 0,5 kW/m3 respecto del volumen total de suspensión presente en el sistema.
CO03101600A 2001-05-25 2003-11-18 Proceso para convertir gas de sintesis a hidrocarburos liquidos en presencia de un catalizador fischer-tropsch, con mejoramiento de la transferencia de masa y energia en la zona de mezclado con alto esfuerzo de corte CO5540337A2 (es)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
GB0112788A GB0112788D0 (en) 2001-05-25 2001-05-25 Process
GB0112798A GB0112798D0 (en) 2001-05-25 2001-05-25 Process
GB0112787A GB0112787D0 (en) 2001-05-25 2001-05-25 Process
GB0112795A GB0112795D0 (en) 2001-05-25 2001-05-25 Process
GB0113786A GB0113786D0 (en) 2001-06-06 2001-06-06 Process

Publications (1)

Publication Number Publication Date
CO5540337A2 true CO5540337A2 (es) 2005-07-29

Family

ID=27516024

Family Applications (1)

Application Number Title Priority Date Filing Date
CO03101600A CO5540337A2 (es) 2001-05-25 2003-11-18 Proceso para convertir gas de sintesis a hidrocarburos liquidos en presencia de un catalizador fischer-tropsch, con mejoramiento de la transferencia de masa y energia en la zona de mezclado con alto esfuerzo de corte

Country Status (13)

Country Link
US (1) US6822005B2 (es)
EP (1) EP1392622B1 (es)
JP (1) JP2004536173A (es)
CN (1) CN1269777C (es)
AR (1) AR034047A1 (es)
AT (1) ATE286866T1 (es)
BR (1) BR0209981A (es)
CO (1) CO5540337A2 (es)
DE (1) DE60202604T2 (es)
EA (1) EA006222B1 (es)
NO (1) NO335115B1 (es)
OA (1) OA12695A (es)
WO (1) WO2002096837A2 (es)

Families Citing this family (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB0112789D0 (en) * 2001-05-25 2001-07-18 Bp Exploration Operating Process
US20100175320A1 (en) * 2006-12-29 2010-07-15 Pacific Renewable Fuels Llc Energy efficient system and process for the continuous production of fuels and energy from syngas
CN101679173B (zh) * 2007-05-29 2013-09-18 Lg化学株式会社 烯烃的醛化方法及其装置
US8133925B2 (en) * 2007-06-27 2012-03-13 H R D Corporation System and process for fischer-tropsch conversion
US8026403B2 (en) * 2007-06-27 2011-09-27 H R D Corporation System and process for production of liquid product from light gas
US8394861B2 (en) 2007-06-27 2013-03-12 Hrd Corporation Gasification of carbonaceous materials and gas to liquid processes
NO2194111T3 (es) * 2007-09-27 2018-03-31
US8461285B2 (en) * 2010-03-09 2013-06-11 Basf Se Process for preparing polyether polyols
EP2681294A2 (en) * 2011-02-28 2014-01-08 The Trustees of Columbia University in the City of New York Methods and systems for converting gaseous hydrocarbons to synthetic gas
US8722573B2 (en) * 2012-08-22 2014-05-13 Council Of Scientific & Industrial Research Sulfonated carbon silica composite material and a process for the preparation thereof
CN102798259B (zh) * 2012-08-31 2014-04-30 浙江科维节能技术股份有限公司 一种降低冷却循环水系统水泵能耗的方法
WO2014080408A2 (en) * 2012-11-25 2014-05-30 Turbulent Technologies Ltd. A mixing method and device for solvent extraction, especially in hydrometallurgical processes
CN103537248A (zh) * 2013-10-30 2014-01-29 江苏泰丰化工有限公司 一种混合碱回收的文丘里喷射式反应装置
JP6931270B2 (ja) * 2016-05-31 2021-09-01 三菱ケミカルエンジニアリング株式会社 マイクロナノバブル発生装置を備えた気液反応装置及びこの気液反応装置を用いた気液反応方法

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB728543A (en) * 1952-03-05 1955-04-20 Koppers Gmbh Heinrich Process for the synthesis of hydrocarbons
GB8508613D0 (en) * 1985-04-02 1985-05-09 British Petroleum Co Plc Chemical process
FR2751564B1 (fr) * 1996-07-26 2001-10-12 Inst Francais Du Petrole Procede et dispositif pour le fonctionnement d'une colonne a bulles triphasique avec application en synthese fischer-tropsch
US6160026A (en) * 1997-09-24 2000-12-12 Texaco Inc. Process for optimizing hydrocarbon synthesis
US5905094A (en) * 1997-10-21 1999-05-18 Exxon Research And Engineering Co. Slurry hydrocarbon synthesis with reduced catalyst attrition and deactivation
DE19854637A1 (de) * 1998-11-26 2000-05-31 Basf Ag Reaktor zur kontinuierlichen Durchführung von Gas-Flüssig-, Flüssig-Flüssig- oder Gas-Flüssig-Fest-Reaktionen
GB9928132D0 (en) * 1999-11-26 2000-01-26 Bp Amoco Plc Process

Also Published As

Publication number Publication date
DE60202604D1 (de) 2005-02-17
EA006222B1 (ru) 2005-10-27
CN1269777C (zh) 2006-08-16
OA12695A (en) 2006-06-21
US6822005B2 (en) 2004-11-23
EP1392622A2 (en) 2004-03-03
ATE286866T1 (de) 2005-01-15
DE60202604T2 (de) 2005-06-16
WO2002096837A2 (en) 2002-12-05
JP2004536173A (ja) 2004-12-02
AR034047A1 (es) 2004-01-21
CN1635983A (zh) 2005-07-06
BR0209981A (pt) 2004-04-06
EA200301176A1 (ru) 2004-06-24
NO20035219D0 (no) 2003-11-24
US20040132836A1 (en) 2004-07-08
WO2002096837A3 (en) 2003-05-08
NO335115B1 (no) 2014-09-15
EP1392622B1 (en) 2005-01-12

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