AR112623A1 - Método para mejorar la eficiencia de una planta de gas de síntesis de amoníaco - Google Patents

Método para mejorar la eficiencia de una planta de gas de síntesis de amoníaco

Info

Publication number
AR112623A1
AR112623A1 ARP180102072A AR112623A1 AR 112623 A1 AR112623 A1 AR 112623A1 AR P180102072 A ARP180102072 A AR P180102072A AR 112623 A1 AR112623 A1 AR 112623A1
Authority
AR
Argentina
Prior art keywords
gas
establishing
ammonia
electrolysis
efficiency
Prior art date
Application number
Other languages
English (en)
Inventor
Jensen Annette E Krll
Pat A Han
Original Assignee
Haldor Topsoe As
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=62873362&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=AR112623(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Haldor Topsoe As filed Critical Haldor Topsoe As
Publication of AR112623A1 publication Critical patent/AR112623A1/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
    • C01B3/025—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
    • C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
    • C01B13/02—Preparation of oxygen
    • C01B13/0229—Purification or separation processes
    • 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
    • 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
    • C01B3/384—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 the catalyst being continuously externally heated
    • 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
    • C01B3/48—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 followed by reaction of water vapour with carbon monoxide
    • 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
    • C01B3/50—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification
    • C01B3/506—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification at low temperatures
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
    • C01C1/00—Ammonia; Compounds thereof
    • C01C1/02—Preparation, purification or separation of ammonia
    • C01C1/04—Preparation of ammonia by synthesis in the gas phase
    • C01C1/0405—Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00—Electrolytic production of inorganic compounds or non-metals
    • C25B1/01—Products
    • C25B1/02—Hydrogen or oxygen
    • C25B1/04—Hydrogen or oxygen by electrolysis of water
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B15/00—Operating or servicing cells
    • C25B15/08—Supplying or removing reactants or electrolytes; Regeneration of electrolytes
    • 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
    • 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
    • F25J3/04636—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 using a hybrid air separation unit, e.g. combined process by cryogenic separation and non-cryogenic separation techniques
    • 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
    • C01B2203/0283—Processes for making hydrogen or synthesis gas containing a CO-shift step, i.e. a water gas shift 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
    • 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
    • C01B2203/0475—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
    • 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
    • C01B2203/1235—Hydrocarbons
    • 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
    • F25J2205/00—Processes or apparatus using other separation and/or other processing means
    • F25J2205/86—Processes or apparatus using other separation and/or other processing means using electrical phenomena, e.g. Corona discharge, electrolysis or magnetic field
    • 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
    • F25J2245/00—Processes or apparatus involving steps for recycling of process streams
    • F25J2245/50—Processes or apparatus involving steps for recycling of process streams the recycled stream being oxygen
    • 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
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
    • 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
    • Y02P20/10—Process efficiency
    • Y02P20/133—Renewable energy sources, e.g. sunlight
    • 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

Abstract

Un método para mejorar la eficiencia de una planta de gas de síntesis de amoníaco existente o una planta de gas de síntesis de amoníaco al establecer una combinación de reformado con vapor secundario utilizando oxígeno de la electrólisis de agua para la producción de gas de síntesis de amoníaco. Reivindicación 1: Un método para mejorar la eficiencia de una planta de gas de síntesis de amoníaco, la planta de gas de síntesis de amoníaco comprende un reformador con vapor primario calentado a fuego y un reformador con vapor secundario operado con una atmósfera que contiene oxígeno, una unidad de desplazamiento de gas de agua, una unidad de remoción de dióxido de carbono, un paso de metanación y un compresor de gas de síntesis de amoníaco, el método está caracterizado porque comprende los pasos de (a) establecer una unidad de electrólisis y preparar una corriente que contiene gas de hidrógeno separada y una corriente que contiene gas de oxígeno separada por medio de la electrólisis de agua; (b) establecer un tubo de gas para transportar la corriente que contiene gas de hidrógeno separada de la unidad de electrólisis al compresor de gas de síntesis y/o al paso de metanación; y (c) establecer un tubo de gas para transportar por lo menos parte de la corriente de gas de oxígeno separada de la unidad de electrólisis a un quemador en el reformador secundario.
ARP180102072 2017-07-25 2018-07-25 Método para mejorar la eficiencia de una planta de gas de síntesis de amoníaco AR112623A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DKPA201700425 2017-07-25

Publications (1)

Publication Number Publication Date
AR112623A1 true AR112623A1 (es) 2019-11-20

Family

ID=62873362

Family Applications (7)

Application Number Title Priority Date Filing Date
ARP180102076 AR112344A1 (es) 2017-07-25 2018-07-25 Proceso para la co-producción de metanol y amoníaco
ARP180102074 AR112624A1 (es) 2017-07-25 2018-07-25 Método para la preparación de gas de síntesis
ARP180102077 AR112462A1 (es) 2017-07-25 2018-07-25 Proceso para la co-producción de metanol y amoníaco en paralelo
ARP180102075 AR112573A1 (es) 2017-07-25 2018-07-25 Método para la preparación de gas de síntesis
ARP180102072 AR112623A1 (es) 2017-07-25 2018-07-25 Método para mejorar la eficiencia de una planta de gas de síntesis de amoníaco
ARP180102073 AR112572A1 (es) 2017-07-25 2018-07-25 Método para la preparación de gas de síntesis de amoníaco
ARP180102071 AR112571A1 (es) 2017-07-25 2018-07-25 Método para la preparación de gas de síntesis de amoníaco

Family Applications Before (4)

Application Number Title Priority Date Filing Date
ARP180102076 AR112344A1 (es) 2017-07-25 2018-07-25 Proceso para la co-producción de metanol y amoníaco
ARP180102074 AR112624A1 (es) 2017-07-25 2018-07-25 Método para la preparación de gas de síntesis
ARP180102077 AR112462A1 (es) 2017-07-25 2018-07-25 Proceso para la co-producción de metanol y amoníaco en paralelo
ARP180102075 AR112573A1 (es) 2017-07-25 2018-07-25 Método para la preparación de gas de síntesis

Family Applications After (2)

Application Number Title Priority Date Filing Date
ARP180102073 AR112572A1 (es) 2017-07-25 2018-07-25 Método para la preparación de gas de síntesis de amoníaco
ARP180102071 AR112571A1 (es) 2017-07-25 2018-07-25 Método para la preparación de gas de síntesis de amoníaco

Country Status (15)

Country Link
US (1) US11370658B2 (es)
EP (1) EP3658489B1 (es)
KR (1) KR102446845B1 (es)
CN (1) CN110869314A (es)
AR (7) AR112344A1 (es)
AU (1) AU2018308586A1 (es)
BR (1) BR112020001487A2 (es)
CA (1) CA3069240C (es)
CL (1) CL2020000151A1 (es)
EA (1) EA039782B1 (es)
IL (1) IL271937B2 (es)
PE (1) PE20200525A1 (es)
UA (1) UA126346C2 (es)
WO (1) WO2019020376A1 (es)
ZA (1) ZA201908075B (es)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102019214812A1 (de) 2019-09-27 2020-06-18 Thyssenkrupp Ag Verfahren und Anlage zur Erzeugung von Synthesegas
MX2023008603A (es) 2021-01-21 2023-08-10 Casale Sa Metodo de preparacion de un gas de sintesis.
CN113401920B (zh) * 2021-06-25 2022-04-22 国能经济技术研究院有限责任公司 基于碘硫半开式循环制氢的co2零排放合成氨系统、方法及应用
WO2023046860A1 (de) * 2021-09-22 2023-03-30 Thyssenkrupp Industrial Solutions Ag Verfahren zur ammoniaksynthese und anlage zur herstellung von ammoniak
BE1029787B1 (de) * 2021-09-22 2023-04-24 Thyssenkrupp Ind Solutions Ag Verfahren zur Ammoniaksynthese und Anlage zur Herstellung von Ammoniak
US20230183083A1 (en) * 2021-12-14 2023-06-15 Saudi Arabian Oil Company Ammonia production from carbon- and water-derived hydrogen
US20230264956A1 (en) * 2022-02-18 2023-08-24 Gti Energy Integrated partial oxidation and electrolysis process
WO2023176921A1 (ja) * 2022-03-16 2023-09-21 東洋エンジニアリング株式会社 尿素製造方法及び尿素製造装置
GB2619949A (en) * 2022-06-22 2023-12-27 Equinor Energy As Process

Family Cites Families (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4197281A (en) * 1975-12-17 1980-04-08 Texaco Development Corporation Production of ammonia synthesis gas from solid carbonaceous fuels
US5736116A (en) 1995-10-25 1998-04-07 The M. W. Kellogg Company Ammonia production with enriched air reforming and nitrogen injection into the synthesis loop
KR100514178B1 (ko) * 2004-01-17 2005-09-13 한국과학기술연구원 고온 메탄 개질형 하이브리드 수전해 시스템
EP1657409A1 (en) * 2004-11-15 2006-05-17 Elsam A/S A method of and an apparatus for producing electrical power
US20070122339A1 (en) 2005-11-28 2007-05-31 General Electric Company Methods and apparatus for hydrogen production
EP2166064A1 (en) 2008-09-19 2010-03-24 Siemens Aktiengesellschaft A chemical product providing system and method for providing a chemical product
CN101880046A (zh) * 2009-05-05 2010-11-10 中村德彦 复合设备
DK2467354T3 (en) * 2009-08-20 2014-03-10 Saudi Basic Ind Corp Process for simultaneous production of methanol and ammonia
FR2971789B1 (fr) 2011-02-22 2013-02-22 Areva Methode de production de methanol ou d'hydrocarbures a partir d'une matiere carbonee, avec une etape de reformage dont les conditions de fontionnement sont ajustees selectivement
EP2589574B1 (en) 2011-11-02 2015-10-21 Casale Sa Method for load regulation of an ammonia plant
EP2631213A1 (en) 2012-02-24 2013-08-28 Ammonia Casale S.A. Process for producing ammonia synthesis gas and a related front-end of an ammonia plant
EP2818447A1 (en) 2013-06-26 2014-12-31 Ammonia Casale S.A. A process for purification of a synthesis gas containing hydrogen and impurities
US20150129806A1 (en) 2013-11-08 2015-05-14 Ammonia Casale Sa Process for Producing Ammonia Synthesis Gas and a Method for Revamping a Front-End of an Ammonia Plant
MX2018006784A (es) 2015-12-04 2018-11-09 Grannus Llc Produccion de poligeneracion de hidrogeno para usarse en diversos procesos industriales.
AU2017100018A4 (en) 2017-01-07 2017-03-02 Cooper, James MR Using renewable ammonia as a strategic energy reserve for Australia's defence

Also Published As

Publication number Publication date
IL271937B1 (en) 2023-04-01
EA039782B1 (ru) 2022-03-14
UA126346C2 (uk) 2022-09-21
PE20200525A1 (es) 2020-03-09
BR112020001487A2 (pt) 2020-09-08
ZA201908075B (en) 2023-04-26
CA3069240A1 (en) 2019-01-31
US11370658B2 (en) 2022-06-28
KR102446845B1 (ko) 2022-09-23
US20210198104A1 (en) 2021-07-01
CN110869314A (zh) 2020-03-06
AR112572A1 (es) 2019-11-13
AR112344A1 (es) 2019-10-16
KR20200032671A (ko) 2020-03-26
EP3658489A1 (en) 2020-06-03
AR112571A1 (es) 2019-11-13
AR112573A1 (es) 2019-11-13
AU2018308586A1 (en) 2020-01-23
AR112462A1 (es) 2019-10-30
CA3069240C (en) 2024-03-05
IL271937B2 (en) 2023-08-01
CL2020000151A1 (es) 2020-07-31
IL271937A (en) 2020-02-27
AR112624A1 (es) 2019-11-20
EP3658489B1 (en) 2022-01-19
WO2019020376A1 (en) 2019-01-31
EA202090324A1 (ru) 2020-05-15

Similar Documents

Publication Publication Date Title
AR112623A1 (es) Método para mejorar la eficiencia de una planta de gas de síntesis de amoníaco
CO7310535A2 (es) Procedimiento e instalación para la generación de gas síntesis
CL2008003512A1 (es) Proceso para producir gas de sintesis de amoniaco mediante reformado combinado, en que el gas que sale del reformador primario pasa a un reformador secundario junto con aire enriquecido en oxigeno con una razon n2/o2 adecuada para reformar todo el hidrocarburo en el gas y obtener una razon h2/n2 adecuada para dicha sintesis.
AR089633A1 (es) Co-produccion de metanol y urea
RU2014138380A (ru) Способ получения синтез-газа для синтеза аммиака и соответствующая внешняя секция установки для получения аммиака
RU2016132971A (ru) Способ и система получения диоксида углерода и электроэнергии из газообразного углеводородного сырья
ES2615892T3 (es) Producción eficaz y autosuficiente de metanol a partir de una fuente de metano a través de bi-reformado oxidativo
EA201300013A1 (ru) Реактивная двигательная установка с улавливанием углерода
EA201991739A1 (ru) Системы и способы повышения эффективности использования природного газа в установках парового риформинга метана
CL2020000152A1 (es) Método para mejorar la eficiencia de una planta de gas de síntesis de amoníaco.
CL2015003260A1 (es) Un proceso de producción de gas de síntesis de amoníaco con conversión a alta temperatura y baja relación de vapor a carbono.
ATE528070T1 (de) Sauerstoffentfernung
CL2020000476A1 (es) Reactor de conversión y administración del método.
BR112017017593A2 (pt) processo para a produção de ureia estabilizada por formaldeído.
CL2020002819A1 (es) Proceso para sintetizar metanol
MX2022013763A (es) Proceso para capturar dioxido de carbono del aire y la conversion directa de dioxido de carbono en combustibles y quimicos.
CL2018000105A1 (es) Dispositivo y método para producir gas sintético
MY195274A (en) Process for Methanol Production
CL2023001043A1 (es) Conversión de co2 y h2 en combustibles sintéticos
CL2022001639A1 (es) Aparato y método para utilizar los gases de escape de una planta power-to-x
CL2009000866A1 (es) Proceso , planta y metodo para reacondicionar planta para producir metanol por reformado con vapor de agua y alimentacion del gas de sintesis reformado a un bucle de sintesis de metanol, en que el gas de sintesis reformado se mezcla con una corriente adicional de gas que contiene una relacion hidrogeno a carbono menor a la de dicho gas de sintesis reformado.
ES2243146B1 (es) Procedimiento para la obtencion de hidrogeno a partir de gas natural
CL2023001742A1 (es) Método para recuperar calor residual creado en la producción de amoníaco verde
AR055743A1 (es) Proceso de sintesis de amoniaco
CL2023002160A1 (es) Producción de gas de síntesis a partir de co2 y vapor para síntesis de combustibles

Legal Events

Date Code Title Description
FG Grant, registration