[go: up one dir, main page]

PE20180157A1 - Proceso para preparar un gas de sintesis y un dispositivo de enfriamiento de gas de sintesis - Google Patents

Proceso para preparar un gas de sintesis y un dispositivo de enfriamiento de gas de sintesis

Info

Publication number
PE20180157A1
PE20180157A1 PE2017002406A PE2017002406A PE20180157A1 PE 20180157 A1 PE20180157 A1 PE 20180157A1 PE 2017002406 A PE2017002406 A PE 2017002406A PE 2017002406 A PE2017002406 A PE 2017002406A PE 20180157 A1 PE20180157 A1 PE 20180157A1
Authority
PE
Peru
Prior art keywords
gas
synthesis gas
methane
cooling device
heat exchange
Prior art date
Application number
PE2017002406A
Other languages
English (en)
Inventor
Goeb Manfred Heinrich Schmitz
Ruben Smit
Original Assignee
Shell Int Research
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 Shell Int Research filed Critical Shell Int Research
Publication of PE20180157A1 publication Critical patent/PE20180157A1/es

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
    • C01B3/386—Catalytic partial combustion
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/36—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using oxygen or mixtures containing oxygen as gasifying agents
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
    • C01B3/382—Multi-step processes
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/02—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled
    • F28D7/024—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled the conduits of only one medium being helically coiled tubes, the coils having a cylindrical configuration
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/10—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically
    • F28D7/12—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically the surrounding tube being closed at one end, e.g. return type
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02—Processes for making hydrogen or synthesis gas
    • C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
    • C01B2203/0227—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
    • C01B2203/0244—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being an autothermal reforming step, e.g. secondary reforming processes
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02—Processes for making hydrogen or synthesis gas
    • C01B2203/025—Processes for making hydrogen or synthesis gas containing a partial oxidation step
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02—Processes for making hydrogen or synthesis gas
    • C01B2203/025—Processes for making hydrogen or synthesis gas containing a partial oxidation step
    • C01B2203/0255—Processes for making hydrogen or synthesis gas containing a partial oxidation step containing a non-catalytic partial oxidation step
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02—Processes for making hydrogen or synthesis gas
    • C01B2203/025—Processes for making hydrogen or synthesis gas containing a partial oxidation step
    • C01B2203/0261—Processes for making hydrogen or synthesis gas containing a partial oxidation step containing a catalytic partial oxidation step [CPO]
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/08—Methods of heating or cooling
    • C01B2203/0872—Methods of cooling
    • C01B2203/0883—Methods of cooling by indirect heat exchange
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/08—Methods of heating or cooling
    • C01B2203/0872—Methods of cooling
    • C01B2203/0888—Methods of cooling by evaporation of a fluid
    • C01B2203/0894—Generation of steam
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/12—Feeding the process for making hydrogen or synthesis gas
    • C01B2203/1205—Composition of the feed
    • C01B2203/1211—Organic compounds or organic mixtures used in the process for making hydrogen or synthesis gas
    • C01B2203/1235—Hydrocarbons
    • C01B2203/1241—Natural gas or methane
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/80—Aspect of integrated processes for the production of hydrogen or synthesis gas not covered by groups C01B2203/02 - C01B2203/1695
    • C01B2203/82—Several process steps of C01B2203/02 - C01B2203/08 integrated into a single apparatus

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

La invencion se refiere a un proceso para la preparacion de un gas de sintesis, que comprende hidrogeno y monoxido de carbono, que comprende las etapas de: (a) hacer reaccionar un gas que comprende metano precalentado con un gas oxidante para obtener un gas de sintesis bruto caliente que comprende monoxido de carbono e hidrogeno; (b) enfriar el gas de sintesis bruto caliente producido de la etapa (a) para obtener el gas de sintesis mediante intercambio de calor indirecto con el agua para producir vapor saturado; (e) volver a enfriar el gas de sintesis bruto obtenido en la etapa (b) mediante intercambio de calor indirecto con un gas que comprende metano para obtener un gas de sintesis bruto enfriado y el gas que comprende metano precalentado para usar en la etapa (a), en donde: (i) las etapas (b) y (e) se realizan en un dispositivo de enfriamiento unico para intercambio de calor indirecto combinado, con el agua y con el gas que comprende metano; y (ii) el gas que comprende metano precalentado obtenido en la etapa (e) tiene una temperatura de 400 a 650 'C. La invencion tambien se refiere a un dispositivo de enfriamiento que se puede usar como el dispositivo de enfriamiento unico en el proceso anterior. El dispositivo de enfriamiento comprende una seccion de evaporacion para producir vapor saturado, una seccion de intercambio de calor del gas para precalentar la alimentacion que comprende metano usada en la etapa (a) con el gas de sintesis bruto y un espacio de recoleccion de vapor seco. Este espacio de recoleccion de vapor seco esta separado de la seccion de evaporacion en donde el vapor saturado humedo se forma
PE2017002406A 2015-05-14 2016-05-04 Proceso para preparar un gas de sintesis y un dispositivo de enfriamiento de gas de sintesis PE20180157A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP15167763 2015-05-14

Publications (1)

Publication Number Publication Date
PE20180157A1 true PE20180157A1 (es) 2018-01-18

Family

ID=53175368

Family Applications (1)

Application Number Title Priority Date Filing Date
PE2017002406A PE20180157A1 (es) 2015-05-14 2016-05-04 Proceso para preparar un gas de sintesis y un dispositivo de enfriamiento de gas de sintesis

Country Status (7)

Country Link
US (1) US20180086634A1 (es)
EP (1) EP3294669B1 (es)
AU (1) AU2016259682B2 (es)
MY (1) MY186964A (es)
PE (1) PE20180157A1 (es)
RU (1) RU2721837C2 (es)
WO (1) WO2016180701A1 (es)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109029021A (zh) * 2018-08-14 2018-12-18 中国原子能科学研究院 一种换热器的换热管及采用该换热管的换热器
CN115597402B (zh) * 2022-09-30 2023-08-04 镇海石化建安工程股份有限公司 一种用于加氢装置的换热组件及换热工艺

Family Cites Families (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB8711156D0 (en) 1987-05-12 1987-06-17 Shell Int Research Partial oxidation of hydrocarbon-containing fuel
GB9225188D0 (en) * 1992-12-02 1993-01-20 Rolls Royce & Ass Combined reformer and shift reactor
MY115440A (en) 1994-07-22 2003-06-30 Shell Int Research A process for the manufacture of synthesis gas by partial oxidation of a gaseous hydrocarbon-containing fuel using a multi-orifice (co-annular)burner
EG20966A (en) 1995-06-06 2000-07-30 Shell Int Research A method for flame stabilization in a process for preparing synthesis gas
US5931978A (en) 1995-12-18 1999-08-03 Shell Oil Company Process for preparing synthesis gas
US6077323A (en) * 1997-06-06 2000-06-20 Air Products And Chemicals, Inc. Synthesis gas production by ion transport membranes
JP4045564B2 (ja) * 1999-10-20 2008-02-13 株式会社日本ケミカル・プラント・コンサルタント 自己酸化内部加熱型改質装置及び方法
EP1403216B1 (en) 2002-09-26 2011-03-23 Haldor Topsoe A/S Process for the preparation of synthesis gas
GB0225961D0 (en) 2002-11-07 2002-12-11 Johnson Matthey Plc Production of hydrocarbons
US6946493B2 (en) 2003-03-15 2005-09-20 Conocophillips Company Managing hydrogen in a gas to liquid plant
US7090816B2 (en) * 2003-07-17 2006-08-15 Kellogg Brown & Root Llc Low-delta P purifier for nitrogen, methane, and argon removal from syngas
US7485767B2 (en) 2005-06-29 2009-02-03 Exxonmobil Chemical Patents Inc. Production of synthesis gas blends for conversion to methanol or Fischer-Tropsch liquids
US7552701B2 (en) 2006-05-16 2009-06-30 Shell Oil Company Boiler for making super heated steam and its use
US7832364B2 (en) * 2006-12-14 2010-11-16 Texaco Inc. Heat transfer unit for steam generation and gas preheating
WO2010133621A1 (en) * 2009-05-20 2010-11-25 Shell Internationale Research Maatschappij B.V. Process to prepare a mixture of carbon monoxide and hydrogen

Also Published As

Publication number Publication date
RU2721837C2 (ru) 2020-05-22
MY186964A (en) 2021-08-26
RU2017143599A (ru) 2019-06-14
RU2017143599A3 (es) 2019-07-26
AU2016259682A1 (en) 2017-11-09
AU2016259682B2 (en) 2018-09-13
WO2016180701A1 (en) 2016-11-17
US20180086634A1 (en) 2018-03-29
EP3294669A1 (en) 2018-03-21
EP3294669B1 (en) 2019-01-02

Similar Documents

Publication Publication Date Title
EA201270090A1 (ru) Способ получения пара с использованием тепла, извлеченного из реакции полимеризации
CL2012002119A1 (es) Proceso y planta para enfriar acido que se extrae desde un aparato de absorcion de una planta de acido sulfurico.
CO6531461A2 (es) Procesamiento de gases de hidrocarburos
AR090719A1 (es) Disposicion para la produccion de un alotropo de carbono, metodo para formar un catalizador de nanotubos de carbono y metodo para la formacion de nanotubos de carbono
WO2012138766A3 (en) System for generating power from a syngas fermentation process
CU24383B1 (es) Método de generación de energía por combustión de material de biomasa sacarificado
UY32661A (es) Procedimiento para la realizacion de la pirolisis y aparatos para la pirolisis
PH12014502770B1 (en) Cooling water supply system and binary cycle power plant including same
PE20161535A1 (es) Procedimiento para producir hidrogeno
MX2016016748A (es) Proceso para produccion de amoniaco y derivados, en particular urea.
JO3678B1 (ar) عملية ووحدة صناعية لإنتاج حمض الكبريتيك بشكل محسَّن وفعَّال من حيث الطاقة
CL2017000511A1 (es) Proceso para la producción de amoniaco y sus derivados, en particular urea.
EA201890451A1 (ru) Способ получения мочевины и установка для получения мочевины
PE20180157A1 (es) Proceso para preparar un gas de sintesis y un dispositivo de enfriamiento de gas de sintesis
EA201890092A1 (ru) Способ и установка для охлаждения синтез-газа
ES2571004A1 (es) Planta térmica con ciclos de procesos cerrados acoplados en cascada
EA201300679A1 (ru) Способ переработки угля
GB201303399D0 (en) A thermal energy plant for and process of utilising waste from the tanning process
AR099463A1 (es) Procedimiento de transformación de una biomasa en al menos un biocarbón
RU2015104766A (ru) Способ получения водорода из биомассы
DE602008003222D1 (de) Kraftwärmekopplung bei der herstellung von hygienepapieren
ES2441691B1 (es) Procedimiento para el acondicionamiento de una corriente de gas proveniente de un gasificador, craqueo termico de alquitranes y reformado con vapor y reactor empleado
AR089617A1 (es) Metodo y sistemas para formar nanotubos de carbono
PE20091146A1 (es) Procedimiento mejorado para preparar acido cianhidrico
RU2012121538A (ru) Способ получения синтез-газа из древесных отходов