CL2025003763A1 - Método para poner en marcha una planta de fischer-tropsch. - Google Patents

Método para poner en marcha una planta de fischer-tropsch.

Info

Publication number
CL2025003763A1
CL2025003763A1 CL2025003763A CL2025003763A CL2025003763A1 CL 2025003763 A1 CL2025003763 A1 CL 2025003763A1 CL 2025003763 A CL2025003763 A CL 2025003763A CL 2025003763 A CL2025003763 A CL 2025003763A CL 2025003763 A1 CL2025003763 A1 CL 2025003763A1
Authority
CL
Chile
Prior art keywords
fischer
tropsch
unit
starting
providing
Prior art date
Application number
CL2025003763A
Other languages
English (en)
Inventor
Lorna Solveig Cook Amelia
Ying Chan Chi
Original Assignee
Johnson Matthey Davy Technologies 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 Johnson Matthey Davy Technologies Ltd filed Critical Johnson Matthey Davy Technologies Ltd
Publication of CL2025003763A1 publication Critical patent/CL2025003763A1/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
    • C10G2/341—Apparatus, reactors with stationary catalyst bed
    • 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
    • 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
    • C10G2/50—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon dioxide with hydrogen
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K3/00—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K3/00—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide
    • C10K3/02—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide by catalytic treatment
    • C10K3/026—Increasing the carbon monoxide content, e.g. reverse water-gas shift [RWGS]
    • 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
    • B01J2219/00002—Chemical plants
    • B01J2219/00004—Scale aspects
    • B01J2219/00006—Large-scale industrial plants
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/40—Characteristics of the process deviating from typical ways of processing
    • C10G2300/4031—Start up or shut down operations

Landscapes

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

Abstract

Un método para poner en marcha una planta de Fischer-Tropsch, el método comprende: proporcionar una planta de Fischer-Tropsch que comprende una unidad de Fischer-Tropsch de lecho fijo corriente abajo de una unidad de desplazamiento inverso agua-gas; proporcionar una alimentación que comprende hidrógeno y dióxido de carbono; pasar la alimentación a la unidad de desplazamiento inverso agua-gas para producir un gas de síntesis enriquecido en monóxido de carbono; proporcionar una primera fuente de agua; generar un primer vapor a partir de la primera fuente de agua usando calor del gas de síntesis para formar de esa manera un gas de síntesis enfriado; pasar al menos parte del primer vapor a la unidad de Fischer-Tropsch para aumentar la temperatura de la unidad de Fischer-Tropsch a una primera temperatura de funcionamiento de la unidad de Fischer-Tropsch.
CL2025003763A 2023-06-15 2025-11-28 Método para poner en marcha una planta de fischer-tropsch. CL2025003763A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB202308962 2023-06-15

Publications (1)

Publication Number Publication Date
CL2025003763A1 true CL2025003763A1 (es) 2026-01-09

Family

ID=90828980

Family Applications (1)

Application Number Title Priority Date Filing Date
CL2025003763A CL2025003763A1 (es) 2023-06-15 2025-11-28 Método para poner en marcha una planta de fischer-tropsch.

Country Status (7)

Country Link
EP (1) EP4728022A1 (es)
KR (1) KR20260023629A (es)
CN (1) CN121195044A (es)
AU (1) AU2024305460A1 (es)
CL (1) CL2025003763A1 (es)
GB (1) GB2631009B (es)
WO (1) WO2024256792A1 (es)

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7939953B2 (en) 2008-04-16 2011-05-10 Schlumberger Technology Corporation Micro scale fischer-tropsch and oxygenate synthesis process startup unit
GB201120399D0 (en) * 2011-11-25 2012-01-11 Air Fuel Synthesis Ltd Convertion of carbon dioxide
US20160160128A1 (en) 2013-07-24 2016-06-09 Shell Oil Company Method for starting up a fischer tropsch process
AP2016009375A0 (en) 2014-03-17 2016-08-31 Shell Int Research A method for start-up and operation of a fischer-tropsch reactor
EP3119857B1 (en) 2014-03-17 2025-01-22 Shell Internationale Research Maatschappij B.V. A method for start-up and operation of a fischer-tropsch reactor
KR102425630B1 (ko) * 2014-10-20 2022-07-27 벨로시스 테크놀로지스 리미티드 열을 제거하는 방법
EP3344728A1 (en) * 2015-09-04 2018-07-11 Shell International Research Maatschappij B.V. Fischer-tropsch process
GB201702248D0 (en) 2017-02-10 2017-03-29 Bp Plc Start-up procedure for a fischer-tropsch process
WO2021139898A1 (en) 2020-01-10 2021-07-15 Bp P.L.C. Process for producing a fischer-tropsch synthesis catalyst and fischer-tropsch start-up process
GB202016416D0 (en) * 2020-10-16 2020-12-02 Johnson Matthey Davy Technologies Ltd Process for synthesising hydrocarbons
GB202016417D0 (en) * 2020-10-16 2020-12-02 Johnson Matthey Davy Technologies Ltd Process for producing a gas stream comprising carbon monoxide
EP3992265A1 (de) * 2020-10-30 2022-05-04 Ineratec GmbH Verfahren und anlage zur produktaufbereitung fischer-tropsch basierter rohprodukte zur produktion von vorformulierten oder normgerechten kraftstoffen
GB202204767D0 (en) * 2022-04-01 2022-05-18 Johnson Matthey Davy Technologies Ltd A method of forming a syngas for producing liquid hydrocarbons

Also Published As

Publication number Publication date
GB2631009B (en) 2025-06-04
AU2024305460A1 (en) 2025-11-13
CN121195044A (zh) 2025-12-23
GB2631009A (en) 2024-12-18
WO2024256792A1 (en) 2024-12-19
KR20260023629A (ko) 2026-02-20
GB202405262D0 (en) 2024-05-29
EP4728022A1 (en) 2026-04-22

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