BRPI0512157A - método de preparação de um fluxo rico de hidrogênio e fluxo rico de monóxido de carbono; método de conversão de uma planta de metanol original para uma planta convertida de sìntese de ácido acético e método para preparação de hidrogênio, monóxido de carbono e ácido acético a partir do metanol - Google Patents

método de preparação de um fluxo rico de hidrogênio e fluxo rico de monóxido de carbono; método de conversão de uma planta de metanol original para uma planta convertida de sìntese de ácido acético e método para preparação de hidrogênio, monóxido de carbono e ácido acético a partir do metanol

Info

Publication number
BRPI0512157A
BRPI0512157A BRPI0512157-4A BRPI0512157A BRPI0512157A BR PI0512157 A BRPI0512157 A BR PI0512157A BR PI0512157 A BRPI0512157 A BR PI0512157A BR PI0512157 A BRPI0512157 A BR PI0512157A
Authority
BR
Brazil
Prior art keywords
carbon monoxide
acetic acid
methanol
hydrogen
preparing
Prior art date
Application number
BRPI0512157-4A
Other languages
English (en)
Inventor
Daniel Marcel Thiebaut
Original Assignee
Acetex Cyprus 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 Acetex Cyprus Ltd filed Critical Acetex Cyprus Ltd
Publication of BRPI0512157A publication Critical patent/BRPI0512157A/pt

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/0204—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the feed stream
    • F25J3/0223—H2/CO mixtures, i.e. synthesis gas; Water gas or shifted synthesis gas
    • 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; Reversible storage of hydrogen
    • C01B3/02—Production of hydrogen; Production of gaseous mixtures containing hydrogen
    • C01B3/025—Preparation or purification of gas mixtures for ammonia synthesis
    • 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; Reversible storage of hydrogen
    • C01B3/02—Production of hydrogen; Production of gaseous mixtures containing hydrogen
    • C01B3/32—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide or air
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/10—Preparation of carboxylic acids or their salts, halides or anhydrides by reaction with carbon monoxide
    • C07C51/12—Preparation of carboxylic acids or their salts, halides or anhydrides by reaction with carbon monoxide on an oxygen-containing group in organic compounds, e.g. alcohols
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/0228—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream
    • F25J3/0252—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream separation of hydrogen
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/0228—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream
    • F25J3/0261—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream separation of carbon monoxide
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04521—Coupling of the air fractionation unit to an air gas-consuming unit, so-called integrated processes
    • F25J3/04527—Integration with an oxygen consuming unit, e.g. glass facility, waste incineration or oxygen based processes in general
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04521—Coupling of the air fractionation unit to an air gas-consuming unit, so-called integrated processes
    • F25J3/04527—Integration with an oxygen consuming unit, e.g. glass facility, waste incineration or oxygen based processes in general
    • F25J3/04539—Integration with an oxygen consuming unit, e.g. glass facility, waste incineration or oxygen based processes in general for the H2/CO synthesis by partial oxidation or oxygen consuming reforming processes of fuels
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04521—Coupling of the air fractionation unit to an air gas-consuming unit, so-called integrated processes
    • F25J3/04563—Integration with a nitrogen consuming unit, e.g. for purging, inerting, cooling or heating
    • F25J3/04587—Integration with a nitrogen consuming unit, e.g. for purging, inerting, cooling or heating for the NH3 synthesis, e.g. for adjusting the H2/N2 ratio
    • 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
    • C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
    • C01B2203/046—Purification by cryogenic separation
    • 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
    • C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
    • C01B2203/0465—Composition of the impurity
    • C01B2203/047—Composition of the impurity the impurity being carbon monoxide
    • 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
    • C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
    • C01B2203/0465—Composition of the impurity
    • C01B2203/0475—Composition of the impurity the impurity being carbon dioxide
    • 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
    • C01B2203/06—Integration with other chemical 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
    • C01B2203/06—Integration with other chemical processes
    • C01B2203/068—Ammonia synthesis
    • 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
    • C01B2203/1217—Alcohols
    • C01B2203/1223—Methanol
    • 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
    • C01B2203/1288—Evaporation of one or more of the different feed components
    • 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
    • C01B2203/14—Details of the flowsheet
    • C01B2203/148—Details of the flowsheet involving a recycle stream to the feed of the process for making hydrogen or synthesis gas
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
    • F25J2290/80—Retrofitting, revamping or debottlenecking of existing plant
    • 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
    • Y02P20/151—Reduction of greenhouse gas [GHG] emissions, e.g. CO2

Landscapes

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

Abstract

MéTODO DE PREPARAçãO DE UM FLUXO RICO DE HIDROGêNIO E FLUXO RICO DE MONóXIDO DE CARBONO; MéTODO DE CONVERSãO DE UMA INSTALAçãO DE METANOL ORIGINAL PARA UMA INSTALAçãO CONVERTIDA DE SìNTESE DE áCIDO ACéTICO E MéTODO PARA REPARAçãO DE HIDROGêNIO, MONóXIDO DE CARBONO E áCIDO ACéTICO A PARTIR DO METANOL. Um método para a produção do syngas a partir de estoque de alimentação de metanol é descrito, O suprimento de metanol é fornecido para um reator de oxidação parcial (112) com oxigênio (114) e opcionalmente vapor (116) para obter um vapor misturado (118) de hidrogênio, monóxido de carbono e dióxido de carbono. O dióxido de carbono (122) é separado fora e a mistura (124) de hidrogênio e o monóxido de carbono é alimentado para uma caixa de resfriamento (126) onde é separado dentro em um fluxo rico de hidrogênio e um fluxo rico de monóxido de carbono (130, 128). O dióxido de carbono separado (122) pode ser reciclado de volta para o reator de oxidação parcial (112) como um moderador de temperatura se desejado. O fluxo rico de monóxido de carbono (128) pode ser reagido com metanol (134) em uma unidade de síntese de ácido acético (132) por um processo convencional para produzir acido acético (136) ou um precursor de caldo acético. Opcionalmente, uma unidade de síntese de amónia (144) e/ou uma unidade de síntese do monómero de acetato de vinil (156) pode ser integrado dentro da instalação.
BRPI0512157-4A 2004-07-09 2005-06-23 método de preparação de um fluxo rico de hidrogênio e fluxo rico de monóxido de carbono; método de conversão de uma planta de metanol original para uma planta convertida de sìntese de ácido acético e método para preparação de hidrogênio, monóxido de carbono e ácido acético a partir do metanol BRPI0512157A (pt)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US58654704P 2004-07-09 2004-07-09
PCT/CY2005/000001 WO2006005269A2 (en) 2004-07-09 2005-06-23 Preparati0n of syngas for acetic acid synthesis by partial oxidation of methanol feedstock

Publications (1)

Publication Number Publication Date
BRPI0512157A true BRPI0512157A (pt) 2008-02-12

Family

ID=35395837

Family Applications (1)

Application Number Title Priority Date Filing Date
BRPI0512157-4A BRPI0512157A (pt) 2004-07-09 2005-06-23 método de preparação de um fluxo rico de hidrogênio e fluxo rico de monóxido de carbono; método de conversão de uma planta de metanol original para uma planta convertida de sìntese de ácido acético e método para preparação de hidrogênio, monóxido de carbono e ácido acético a partir do metanol

Country Status (17)

Country Link
US (2) US7498016B2 (pt)
EP (1) EP1776315A2 (pt)
JP (1) JP4914351B2 (pt)
CN (1) CN1942394B (pt)
AU (1) AU2005262160B2 (pt)
BR (1) BRPI0512157A (pt)
CA (1) CA2563220A1 (pt)
MX (1) MXPA06011400A (pt)
MY (1) MY146697A (pt)
NO (1) NO20070185L (pt)
NZ (1) NZ549991A (pt)
PL (1) PL211115B1 (pt)
RS (1) RS20060554A (pt)
RU (1) RU2393108C2 (pt)
UA (1) UA86079C2 (pt)
WO (1) WO2006005269A2 (pt)
ZA (1) ZA200610629B (pt)

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DK2029184T3 (da) 2006-05-26 2011-05-02 Baxter Int Injicerbar fibrinsammensætning til knogleforstærkning
DE602007011920D1 (de) 2006-05-26 2011-02-24 Baxter Healthcare Sa Injizierbarer füllstoff für knochenhohlräume
SG171695A1 (en) * 2008-12-19 2011-07-28 Daicel Chem Method for manufacturing acetic acid and ammonia
DK2467354T3 (en) * 2009-08-20 2014-03-10 Saudi Basic Ind Corp Process for simultaneous production of methanol and ammonia
GB201014304D0 (en) 2010-08-27 2010-10-13 Akay Galip Intensified integrated biomass-to-energy carrier conversion process
EP2592047A1 (en) * 2011-11-14 2013-05-15 L'Air Liquide Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Thermally integrated process and apparatus for purification and separation of components of a synthesis gas
CN105143169B (zh) * 2013-03-15 2017-06-23 国际人造丝公司 使用羰基化方法分离产品气体的方法
EP3031956B1 (en) * 2014-12-10 2017-07-26 Haldor Topsoe As Process for the preparation of ultra-high purity carbon monoxide
US10281203B2 (en) * 2016-08-05 2019-05-07 L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Method for liquefaction of industrial gas by integration of methanol plant and air separation unit
US10288346B2 (en) * 2016-08-05 2019-05-14 L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Method for liquefaction of industrial gas by integration of methanol plant and air separation unit
DE102022001997A1 (de) 2022-06-09 2023-12-14 Olaf Kühl Herstellung von Syngas aus Methanol hergestellt aus Syngas und/oder CO2
CN116272252A (zh) * 2023-03-22 2023-06-23 中海油石化工程有限公司 液氨和碳酸二甲酯的生产系统及应用、液氨和碳酸二甲酯的生产方法

Family Cites Families (53)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1961736A (en) 1929-07-18 1934-06-05 Tennessee Products Corp Process of forming acetic acid from methanol and carbon monoxide
US2896927A (en) 1956-09-26 1959-07-28 Texaco Inc Gas and liquid contacting apparatus
US3552924A (en) 1966-08-15 1971-01-05 Phillips Petroleum Co Hydrogen manufacture
US3769329A (en) 1970-03-12 1973-10-30 Monsanto Co Production of carboxylic acids and esters
US3920717A (en) 1973-03-26 1975-11-18 Texaco Development Corp Production of methanol
US3929429A (en) 1974-09-26 1975-12-30 Texaco Inc Fuel gas from solid carbonaceous fuels
US4006099A (en) 1975-06-16 1977-02-01 Texaco Inc. Manufacture of gaseous mixtures comprising hydrogen and carbon monoxide
US4081253A (en) * 1976-12-10 1978-03-28 Texaco Development Corporation Production of purified synthesis gas and carbon monoxide
US4110359A (en) * 1976-12-10 1978-08-29 Texaco Development Corporation Production of cleaned and purified synthesis gas and carbon monoxide
GB1577069A (en) 1977-07-27 1980-10-15 British Petroleum Co Process for the production of synthesis gas by the catalysed decomposition of methanol
DE2918405A1 (de) 1979-05-08 1980-11-20 Metallgesellschaft Ag Verfahren zur erzeugung von kohlenmonoxid und wasserstoff aus methanol
NL8102840A (nl) 1981-06-12 1983-01-03 Stamicarbon Werkwijze voor de bereiding van methanol.
US4522894A (en) 1982-09-30 1985-06-11 Engelhard Corporation Fuel cell electric power production
AU4695985A (en) 1984-09-04 1986-03-13 Mitsubishi Jukogyo Kabushiki Kaisha Process for reforming methanol
JPH0761843B2 (ja) * 1985-08-13 1995-07-05 三菱重工業株式会社 メタノ−ル分解装置の圧力スイング式ガス分離器
CA1263671A (en) 1986-02-10 1989-12-05 David Leon Banquy Process for the production of synthesis gas
US5155261A (en) 1987-02-05 1992-10-13 Reilly Industries, Inc. Process for acetic acid preparation and heterogenous catalyst for same
SU1465410A1 (ru) * 1987-04-30 1989-03-15 Предприятие П/Я Р-6603 Способ получени аммиака и метанола
DE4130718A1 (de) 1991-09-14 1993-03-18 Metallgesellschaft Ag Verfahren zur erzeugung eins synthesegases fuer die methanolsynthese
JP3337718B2 (ja) * 1992-08-21 2002-10-21 三井化学株式会社 メタノールの部分酸化物の製造方法
US5672743A (en) 1993-09-10 1997-09-30 Bp Chemicals Limited Process for the production of acetic acid
JPH07126201A (ja) 1993-10-27 1995-05-16 Mitsubishi Gas Chem Co Inc メタノール製造方法
FR2725443B1 (fr) 1994-10-05 1996-12-20 Rhone Poulenc Chimie Preparation d'acides carboxyliques ou des esters correspondants par carbonylation en presence d'iridium
US5472986A (en) 1994-11-08 1995-12-05 Starchem, Inc. Methanol production process using a high nitrogen content synthesis gas with a hydrogen recycle
US5817869A (en) 1995-10-03 1998-10-06 Quantum Chemical Corporation Use of pentavalent Group VA oxides in acetic acid processing
DK40796A (da) 1996-04-10 1997-10-11 Haldor Topsoe As Fremgangsmåde til fremstilling af eddikesyre
US6171574B1 (en) 1996-09-24 2001-01-09 Walter Juda Associates, Inc. Method of linking membrane purification of hydrogen to its generation by steam reforming of a methanol-like fuel
GB9626428D0 (en) 1996-12-19 1997-02-05 Bp Chem Int Ltd Process
GB9626317D0 (en) 1996-12-19 1997-02-05 Bp Chem Int Ltd Process
GB9626429D0 (en) 1996-12-19 1997-02-05 Bp Chem Int Ltd Process
JP4226684B2 (ja) * 1997-04-11 2009-02-18 千代田化工建設株式会社 部分酸化法による合成ガスの製造方法
DE19746251C2 (de) * 1997-10-20 1999-09-09 Dbb Fuel Cell Engines Gmbh Anlage zur Wasserdampfreformierung eines Kohlenwasserstoffs und Betriebsverfahren hierfür
US6168765B1 (en) 1998-09-08 2001-01-02 Uop Llc Process and apparatus for interbed injection in plate reactor arrangement
DK173897B1 (da) 1998-09-25 2002-02-04 Topsoe Haldor As Fremgangsmåde til autotermisk reforming af et carbonhydridfødemateriale indeholdende højere carbonhydrider
EP1063011B1 (de) * 1999-05-22 2001-12-12 OMG AG & Co. KG Verwendung eines Katalysators für die Dampfreformierung von Methanol
US6211254B1 (en) 1999-06-07 2001-04-03 John P. Whitney Process for recycling heterogeneous waste
US6274096B1 (en) * 1999-11-01 2001-08-14 Acetex (Cyprus) Limited Methanol plant retrofit
US6232352B1 (en) * 1999-11-01 2001-05-15 Acetex Limited Methanol plant retrofit for acetic acid manufacture
JP4830197B2 (ja) 2000-09-13 2011-12-07 トヨタ自動車株式会社 燃料改質装置
US6531630B2 (en) * 2000-12-29 2003-03-11 Kenneth Ebenes Vidalin Bimodal acetic acid manufacture
US6599491B2 (en) 2001-01-22 2003-07-29 Kenneth Ebenes Vidalin Bimodal hydrogen manufacture
JP2004530272A (ja) * 2001-04-18 2004-09-30 テキサコ ディベラップメント コーポレイション 二酸化炭素除去と一体化した燃料処理装置、燃料電池スタック及び廃ガス酸化装置
DE10136769A1 (de) * 2001-07-27 2003-02-13 Bosch Gmbh Robert Reformereinheit zur Erzeugung eines Reformats
RU2213691C1 (ru) * 2002-01-21 2003-10-10 Институт катализа им. Г.К. Борескова СО РАН Способ получения синтез-газа или обогащенной водородом газовой смеси из водно-спиртовых смесей
DE10214003B4 (de) * 2002-03-27 2005-12-22 Lurgi Ag Verfahren zur Erzeugung von Kohlenmonoxid und Methanol
US6723756B2 (en) * 2002-04-29 2004-04-20 Chevron U.S.A. Inc. Aqueous separation of syngas components
EA008283B1 (ru) * 2002-05-20 2007-04-27 Асетэкс (Кипр) Лимитед Интегрированный способ производства уксусной кислоты и метанола
JP4329116B2 (ja) * 2002-12-02 2009-09-09 トヨタ自動車株式会社 燃料改質装置及び燃料電池システム
JP2004196611A (ja) * 2002-12-19 2004-07-15 Toyota Motor Corp 燃料改質装置及び燃料電池システム
RU2225805C1 (ru) * 2003-01-08 2004-03-20 Открытое акционерное общество "Ракетно-космическая корпорация "Энергия" им. С.П. Королева" Энергоустановка плавательного средства
JP2004339007A (ja) * 2003-05-16 2004-12-02 Toyota Motor Corp 燃料改質システム
JP2005200266A (ja) * 2004-01-15 2005-07-28 Casio Comput Co Ltd 改質方法、改質器、発電装置及び燃料容器
NZ548230A (en) * 2004-01-22 2009-08-28 Acetex Cyprus Ltd Integrated process for making acetic acid and methanol from natural gas

Also Published As

Publication number Publication date
RS20060554A (sr) 2008-09-29
RU2393108C2 (ru) 2010-06-27
US20070225384A1 (en) 2007-09-27
AU2005262160A1 (en) 2006-01-19
NO20070185L (no) 2007-01-25
US7498016B2 (en) 2009-03-03
PL211115B1 (pl) 2012-04-30
ZA200610629B (en) 2008-10-29
AU2005262160B2 (en) 2011-03-03
NZ549991A (en) 2010-10-29
UA86079C2 (ru) 2009-03-25
JP2008505047A (ja) 2008-02-21
MY146697A (en) 2012-09-14
WO2006005269A2 (en) 2006-01-19
US20090143492A1 (en) 2009-06-04
EP1776315A2 (en) 2007-04-25
PL381266A1 (pl) 2007-05-14
MXPA06011400A (es) 2007-03-15
CA2563220A1 (en) 2006-01-19
CN1942394A (zh) 2007-04-04
WO2006005269A3 (en) 2006-07-06
RU2006139769A (ru) 2008-08-20
CN1942394B (zh) 2010-09-29
JP4914351B2 (ja) 2012-04-11
US7732499B2 (en) 2010-06-08

Similar Documents

Publication Publication Date Title
US20190337876A1 (en) Integrated system and method for producing methanol product
NO20070185L (no) Fremstilling av syngass for eddiksyresyntese ved partiell desidasjon av metanol-rastoff
CN101705115B (zh) 一种催化气化煤基能源化工产品多联产系统及方法
ATE528274T1 (de) Verfahren und anlage zur herstellung von methanol
JP4938920B2 (ja) バイオマスガス化炉及びバイオマスのガス化システム
JPH0472044B2 (pt)
RU2012142686A (ru) Применение ископаемых топлив для увеличения преимуществ синтетических топлив на основе биомассы
WO2007142739A3 (en) Synthesis gas production and use
DE69916890D1 (de) Verfahren zur herstellung eines wasserstoffreichen gases und eines kohlendioxidreichen gases mit hohen drücken
AU2018207831B2 (en) Method and device for producing organic compounds from biogas
MX2023008632A (es) Conversion de biogas en alcoholes mixtos.
AU2025217260A1 (en) Electrolysis and pyrolytic natural gas conversion systems for hydrogen and liquid fuel production
WO2010118022A3 (en) System and method for conditioning biomass-derived synthesis gas
AU2008298095B2 (en) Combined production of hydrocarbons and electrical power
GB2485923A (en) Process for increasing the hydrogen content in a synthesis gas
CN118851094A (zh) 一种厌氧耦合气化联产氢醇的方法
CN105861070A (zh) 一种生物质气化合成甲醇二甲醚的工艺
MY165497A (en) Process for producing synthesis gas
Martín et al. Superstructure optimization of Lignocellulosic Bioethanol plants
EP2505574A1 (en) Methanol manufacturing system and method
JP2015105238A (ja) 化学品製造装置及び化学品製造方法
JP2013170086A (ja) 肥料製造システム及び方法
CN102056885B (zh) 乙酸和氨的制造方法
CN119327384A (zh) 一种绿电耦合生物质化学链定向气化制天然气和甲醇系统
MX2025012653A (es) Proceso para la preparacion de metanol

Legal Events

Date Code Title Description
B08F Application dismissed because of non-payment of annual fees [chapter 8.6 patent gazette]

Free format text: REFERENTE A 9A ANUIDADE.

B08K Patent lapsed as no evidence of payment of the annual fee has been furnished to inpi [chapter 8.11 patent gazette]

Free format text: REFERENTE AO DESPACHO 8.6 PUBLICADO NA RPI 2260 DE 29/04/2014.