EA201301250A1 - Способ обработки синтез-газа и система, использующая медный катализатор в двухступенчатых реакциях при 475-525°c и 250-290°c - Google Patents

Способ обработки синтез-газа и система, использующая медный катализатор в двухступенчатых реакциях при 475-525°c и 250-290°c

Info

Publication number
EA201301250A1
EA201301250A1 EA201301250A EA201301250A EA201301250A1 EA 201301250 A1 EA201301250 A1 EA 201301250A1 EA 201301250 A EA201301250 A EA 201301250A EA 201301250 A EA201301250 A EA 201301250A EA 201301250 A1 EA201301250 A1 EA 201301250A1
Authority
EA
Eurasian Patent Office
Prior art keywords
synthesis gas
synthesis
gas
treatment
copper catalyst
Prior art date
Application number
EA201301250A
Other languages
English (en)
Inventor
Рифат Ал Чалаби
Офнэйл Хенри Перри
Ке Ли
Original Assignee
Чинук Энд-Стейдж Ресайклинг Лимитед
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 Чинук Энд-Стейдж Ресайклинг Лимитед filed Critical Чинук Энд-Стейдж Ресайклинг Лимитед
Publication of EA201301250A1 publication Critical patent/EA201301250A1/ru

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
    • 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
    • C01B3/06—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
    • C01B3/20—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of metal hydroxides with carbon monoxide
    • 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
    • B01J15/00—Chemical processes in general for reacting gaseous media with non-particulate solids, e.g. sheet material; Apparatus specially adapted therefor
    • B01J15/005—Chemical processes in general for reacting gaseous media with non-particulate solids, e.g. sheet material; Apparatus specially adapted therefor in the presence of catalytically active bodies, e.g. porous plates
    • 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0006—Controlling or regulating processes
    • B01J19/0013—Controlling the temperature of the process
    • 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/72—Copper
    • 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
    • B01J8/008—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
    • 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
    • C01B3/06—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
    • C01B3/12—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide
    • C01B3/16—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide 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
    • C01B3/06—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
    • C01B3/12—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide
    • C01B3/18—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide using moving solid particles
    • 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
    • C01B3/22—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds
    • C01B3/24—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds of hydrocarbons
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00—Carbon; Compounds thereof
    • C01B32/40—Carbon monoxide
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00—Carbon; Compounds thereof
    • C01B32/50—Carbon dioxide
    • 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
    • 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
    • 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
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00105—Controlling the temperature by indirect heating or cooling employing heat exchange fluids part or all of the reactants being heated or cooled outside the reactor while recycling
    • B01J2219/00108—Controlling the temperature by indirect heating or cooling employing heat exchange fluids part or all of the reactants being heated or cooled outside the reactor while recycling involving reactant vapours
    • 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
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00159—Controlling the temperature controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
    • 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
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00164—Controlling or regulating processes controlling the flow
    • 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
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00186—Controlling or regulating processes controlling the composition of the reactive mixture
    • 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
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00191—Control algorithm
    • B01J2219/00193—Sensing a parameter
    • B01J2219/00195—Sensing a parameter of the reaction system
    • B01J2219/00202—Sensing a parameter of the reaction system at the reactor outlet
    • 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
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00191—Control algorithm
    • B01J2219/00222—Control algorithm taking actions
    • B01J2219/00227—Control algorithm taking actions modifying the operating conditions
    • B01J2219/00229—Control algorithm taking actions modifying the operating conditions of the reaction system
    • 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
    • Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • Catalysts (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Industrial Gases (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

Изобретение представляет способ увеличения отношения CO к Hв синтез-газе. Способ включает пропускание синтез-газа через первый реактор (10), содержащий Cu, при первой температуре, эффективной для взаимодействия COв синтез-газе с Cu с образованием оксида меди и СО. Температура синтез-газа затем понижается до второй температуры, эффективной для взаимодействия водорода в синтез-газе с оксидом меди, с образованием Cu и HO. Синтез-газ затем пропускают через второй реактор (12), содержащий оксид меди, так что Hв синтез-газе взаимодействует с оксидом меди.
EA201301250A 2011-05-11 2012-04-27 Способ обработки синтез-газа и система, использующая медный катализатор в двухступенчатых реакциях при 475-525°c и 250-290°c EA201301250A1 (ru)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB1107813.6A GB2490703B (en) 2011-05-11 2011-05-11 Control of gas composition
PCT/GB2012/000392 WO2012153080A1 (en) 2011-05-11 2012-04-27 Synthesis gas processing and system using copper catalyst in two step reactions at475-525°c and 250-290°c

Publications (1)

Publication Number Publication Date
EA201301250A1 true EA201301250A1 (ru) 2014-04-30

Family

ID=44243904

Family Applications (1)

Application Number Title Priority Date Filing Date
EA201301250A EA201301250A1 (ru) 2011-05-11 2012-04-27 Способ обработки синтез-газа и система, использующая медный катализатор в двухступенчатых реакциях при 475-525°c и 250-290°c

Country Status (15)

Country Link
US (1) US9540236B2 (ru)
EP (1) EP2707130B1 (ru)
JP (1) JP2014528884A (ru)
KR (1) KR20140043897A (ru)
CN (1) CN103687665B (ru)
AU (1) AU2012252206A1 (ru)
BR (1) BR112013028965A2 (ru)
CA (1) CA2835547A1 (ru)
CR (1) CR20130611A (ru)
EA (1) EA201301250A1 (ru)
ES (1) ES2744839T3 (ru)
GB (1) GB2490703B (ru)
MA (1) MA35166B1 (ru)
MX (1) MX2013013160A (ru)
WO (1) WO2012153080A1 (ru)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10670262B2 (en) * 2014-02-26 2020-06-02 University Of Connecticut Reactor for chemical-looping combustion
EP3599218A1 (de) * 2015-10-01 2020-01-29 L'air Liquide, Société Anonyme Pour L'Étude Et L'exploitation Des Procédés Georges Claude Verfahren und anlage zur erzeugung von synthesegas mit variabler zusammensetzung
KR20190094651A (ko) * 2018-02-05 2019-08-14 엘지전자 주식회사 이산화탄소 전환용 촉매 및 그 제조 방법
JP7491505B2 (ja) 2020-02-05 2024-05-28 Ｅｎｅｏｓ株式会社 一酸化炭素の生成方法、前駆体の製造方法およびケミカルルーピングシステム用材料
WO2022065339A1 (ja) 2020-09-24 2022-03-31 積水化学工業株式会社 酸素キャリア、酸素キャリアの製造方法およびガスの製造方法
CN115236219A (zh) * 2022-06-22 2022-10-25 华能海南昌江核电有限公司 一种高温气冷堆氦气中氧气含量测定装置及其测定方法

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU1799865C (ru) 1991-03-04 1993-03-07 Государственный научно-исследовательский и проектный институт метанола и продуктов органического синтеза Способ получени метанола
ES2381105T3 (es) * 2003-02-05 2012-05-23 Haldor Topsoe A/S Procedimiento para el tratamiento de gas de síntesis
US7540893B2 (en) * 2005-12-06 2009-06-02 General Electric Company System and method for producing synthesis gas
CN1880414A (zh) * 2006-05-17 2006-12-20 成都恒新威石化科技有限公司 一种利用逆水煤气变换技术优化合成气组分的方法和流程
GB0914500D0 (en) * 2009-08-19 2009-09-30 Johnson Matthey Plc Process

Also Published As

Publication number Publication date
GB2490703A (en) 2012-11-14
GB2490703B (en) 2015-11-18
KR20140043897A (ko) 2014-04-11
ES2744839T3 (es) 2020-02-26
JP2014528884A (ja) 2014-10-30
AU2012252206A1 (en) 2013-12-12
CR20130611A (es) 2014-03-20
MX2013013160A (es) 2017-02-16
US20140070144A1 (en) 2014-03-13
CN103687665B (zh) 2015-08-12
EP2707130B1 (en) 2019-06-26
CN103687665A (zh) 2014-03-26
WO2012153080A1 (en) 2012-11-15
CA2835547A1 (en) 2012-11-15
GB201107813D0 (en) 2011-06-22
BR112013028965A2 (pt) 2017-03-21
EP2707130A1 (en) 2014-03-19
MA35166B1 (fr) 2014-06-02
US9540236B2 (en) 2017-01-10

Similar Documents

Publication Publication Date Title
EA201301250A1 (ru) Способ обработки синтез-газа и система, использующая медный катализатор в двухступенчатых реакциях при 475-525°c и 250-290°c
CL2017002195A1 (es) Metodo para producir metano a partir de biomasa.
EA201590158A1 (ru) Процесс фишера-тропша
WO2013135710A3 (de) Verfahren zur durchführung der rwgs-reaktion in einem rohrbündelreaktor
MX2012007043A (es) Proceso para el arranque de epoxidacion.
EA201400726A1 (ru) Способ получения аммиака и мочевины
MX2012001157A (es) Procedimiento para la preparacion de 2,2-difluoroetilamina.
FR2984346B1 (fr) Procede de fabrication d'hydrocarbures avec chargement en continu du catalyseur
MX336316B (es) Metodo para producir hidrogeno destinado a su almacenamiento y transporte.
MX368822B (es) Proceso de reduccion directa con calidad de producto y eficiencia de proceso mejoradas.
FI3132009T3 (fi) Menetelmä
EA201490336A1 (ru) Способ и система для производства богатых водородом газовых смесей
EA201001501A1 (ru) Активный реактор риформинга
TR201905563T4 (tr) Hidrojen üretimine yönelik olarak uygun bir sentez gazı aracının üretilmesine yönelik proses.
EA201690088A1 (ru) Способ получения метанола в параллельных реакторах
MX2013006982A (es) Uso de complejos de rutenio-carbeno soportados en reactores operados cotinuamente.
EA201590045A1 (ru) Способ реформинга углеводородов и способ инициирования процесса газ-в-жидкость
MX2015013145A (es) Proceso para separar gas de producto usando proceso de carbonilación.
MY161681A (en) Method of starting up autothermal reforming reactors
BR112015006869A2 (pt) processo de separação e reforma de gás de síntese
EA201891476A1 (ru) Способ подавления загрязнения металлами устройства для получения синтез-газа
EA201590313A1 (ru) Катализатор для получения углеводорода из синтез-газа, способ получения катализатора, способ регенерации катализатора и способ получения углеводорода из синтез-газа
MX2012007447A (es) Proceso de epoxidacion y microestructura.
WO2014067664A3 (en) Methods and systems for reducing metal oxides
BR112012014718A2 (pt) método para a produção de óxido de propileno