EA201992148A1 - METHOD AND INSTALLATION FOR RECEIVING AND PROCESSING SYNTHESIS-GAS MIXTURE - Google Patents

METHOD AND INSTALLATION FOR RECEIVING AND PROCESSING SYNTHESIS-GAS MIXTURE

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Publication number
EA201992148A1
EA201992148A1 EA201992148A EA201992148A EA201992148A1 EA 201992148 A1 EA201992148 A1 EA 201992148A1 EA 201992148 A EA201992148 A EA 201992148A EA 201992148 A EA201992148 A EA 201992148A EA 201992148 A1 EA201992148 A1 EA 201992148A1
Authority
EA
Eurasian Patent Office
Prior art keywords
synthesis
gas mixture
reforming unit
ammonia
primary
Prior art date
Application number
EA201992148A
Other languages
Russian (ru)
Inventor
Евгений Горвал
Original Assignee
Тиссенкрупп Индастриал Солюшнз Аг
Тиссенкрупп Аг
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Publication date
Application filed by Тиссенкрупп Индастриал Солюшнз Аг, Тиссенкрупп Аг filed Critical Тиссенкрупп Индастриал Солюшнз Аг
Publication of EA201992148A1 publication Critical patent/EA201992148A1/en

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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/025Preparation or purification of gas mixtures for ammonia synthesis
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32Production 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
    • C01B3/34Production 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
    • C01B3/38Production 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
    • C01B3/382Multi-step processes
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01CAMMONIA; CYANOGEN; COMPOUNDS THEREOF
    • C01C1/00Ammonia; Compounds thereof
    • C01C1/02Preparation, purification or separation of ammonia
    • C01C1/04Preparation of ammonia by synthesis in the gas phase
    • C01C1/0405Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02Processes for making hydrogen or synthesis gas
    • C01B2203/0205Processes for making hydrogen or synthesis gas containing a reforming step
    • C01B2203/0227Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
    • C01B2203/0233Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being a steam reforming step
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02Processes for making hydrogen or synthesis gas
    • C01B2203/0205Processes for making hydrogen or synthesis gas containing a reforming step
    • C01B2203/0227Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
    • C01B2203/0244Processes 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
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02Processes for making hydrogen or synthesis gas
    • C01B2203/0283Processes for making hydrogen or synthesis gas containing a CO-shift step, i.e. a water gas shift step
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/04Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
    • C01B2203/0415Purification by absorption in liquids
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/04Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
    • C01B2203/0435Catalytic purification
    • C01B2203/0445Selective methanation
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/06Integration with other chemical processes
    • C01B2203/068Ammonia synthesis
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/14Details of the flowsheet
    • C01B2203/141At least two reforming, decomposition or partial oxidation steps in parallel
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/14Details of the flowsheet
    • C01B2203/142At least two reforming, decomposition or partial oxidation steps in series
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Analytical Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Hydrogen, Water And Hydrids (AREA)

Abstract

Настоящее изобретение относится к способу получения и обработки смеси синтез-газа для производства аммиака, в котором содержащую углеводороды и водяной пар подаваемую газовую смесь превращают с помощью кислорода в установке (49) автотермического риформинга в сырую смесь синтез-газа, которую, после последующей обработки, подают по меньшей мере на один синтез (15, 45) аммиака, причём в установку (49) автотермического риформинга подают только одну часть (48) потока подаваемой газовой смеси, вторую часть (32) потока подаваемой газовой смеси направляют в первичную установку (33) риформинга и затем во вторичную установку (20) риформинга, причем полученная в этих первичной и вторичной установках риформинга газовая смесь, при необходимости после последующей обработки, также направляется на синтез (15, 45) аммиака, при этом смесь (44) синтез-газа доводят до повышенного давления, соответствующего давлению синтеза аммиака, при этом только после повышения давления смеси синтез-газа дополнительный азот вводят по меньшей мере из одного трубопровода (14, 57) до того, как смесь синтез-газа поступит на одно- или многоступенчатый синтез аммиака. Преимущество этого способа состоит в том, что достигается существенное снижение нагрузки на все технологические узлы, расположенные между вторичной установкой риформинга и основным синтезом, включая компрессор технологического воздуха и компрессор синтез-газа. По сравнению с вариантом с наличием только одной установки автотермического риформинга при комбинации согласно изобретению с первичной установкой риформинга, наряду с прочими преимуществами, достигается, например, также преимущество, заключающееся в том, что может утилизироваться тепло в канале дымового газа первичной установки риформинга.The present invention relates to a method for producing and processing a synthesis gas mixture for the production of ammonia, in which the supplied gas mixture containing hydrocarbons and water vapor is converted using oxygen in an autothermal reforming unit (49) to a crude synthesis gas mixture, which, after further processing, at least one ammonia synthesis (15, 45) is supplied, and only one part (48) of the feed gas mixture flow is supplied to the autothermal reforming unit (49), the second part (32) of the feed gas mixture flow is sent to the primary plant (33) reforming and then to the secondary reforming unit (20), whereby the gas mixture obtained in these primary and secondary reforming units, if necessary after subsequent processing, is also sent to the synthesis of (15, 45) ammonia, while the mixture (44) of synthesis gas is adjusted to an elevated pressure corresponding to the pressure of the synthesis of ammonia, while only after increasing the pressure of the mixture of synthesis gas additional nitrogen is introduced from at least one pipeline (14, 57) before the synthesis gas mixture enters the single or multi-stage ammonia synthesis. The advantage of this method is that a significant reduction in the load on all process units located between the secondary reforming unit and the main synthesis is achieved, including a process air compressor and a synthesis gas compressor. Compared to the embodiment with only one autothermal reforming unit, when combined with the primary reforming unit according to the invention, among other advantages, for example, an advantage is also achieved that heat can be utilized in the flue gas channel of the primary reforming unit.

EA201992148A 2017-03-14 2018-03-07 METHOD AND INSTALLATION FOR RECEIVING AND PROCESSING SYNTHESIS-GAS MIXTURE EA201992148A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102017204208.7A DE102017204208A1 (en) 2017-03-14 2017-03-14 Process and plant for the production and preparation of a synthesis gas mixture
PCT/EP2018/055612 WO2018166865A1 (en) 2017-03-14 2018-03-07 Method and installation for creating and preparing a synthesis gas mixture

Publications (1)

Publication Number Publication Date
EA201992148A1 true EA201992148A1 (en) 2020-02-28

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Family Applications (1)

Application Number Title Priority Date Filing Date
EA201992148A EA201992148A1 (en) 2017-03-14 2018-03-07 METHOD AND INSTALLATION FOR RECEIVING AND PROCESSING SYNTHESIS-GAS MIXTURE

Country Status (3)

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DE (1) DE102017204208A1 (en)
EA (1) EA201992148A1 (en)
WO (1) WO2018166865A1 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102019005452B4 (en) 2019-08-02 2023-01-19 Hans-Jürgen Maaß Process for generating synthesis gas for the production of ammonia
DE102020200905A1 (en) 2020-01-27 2021-07-29 Thyssenkrupp Ag Process for ammonia synthesis and plant for the production of ammonia
DE102022205453A1 (en) 2022-05-31 2023-11-30 Siemens Energy Global GmbH & Co. KG Plant and process for producing ammonia
CN115385362A (en) * 2022-08-29 2022-11-25 贵州开阳化工有限公司 Method for shortening start time of synthetic ammonia production line

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ATE156778T1 (en) * 1991-07-09 1997-08-15 Ici Plc SYNTHESIS GAS GENERATION
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
EP0999178B1 (en) * 1998-11-03 2006-07-26 Ammonia Casale S.A. Process for the production of synthesis gas
DE10055818A1 (en) 2000-11-10 2002-05-23 Ammonia Casale Sa Catalytic production of ammonia, especially for direct conversion into urea, using nitrogen-hydrogen starting gas mixture obtained from natural gas by autothermal reforming and catalytic conversion
DE10057863C2 (en) 2000-11-21 2002-10-24 Uhde Gmbh Multi-pressure process for the production of ammonia
EP2199253A1 (en) * 2008-12-18 2010-06-23 Ammonia Casale S.A. Process and equipment for the production of ammonia make-up syngas with an air separation unit as nitrogen source
EP2662327A1 (en) * 2012-05-07 2013-11-13 Ammonia Casale S.A. Method of revamping of an ammonia plant fed with natural gas
EP2805914B1 (en) * 2013-05-23 2017-09-13 Haldor Topsøe A/S A process for co-production of ammonia, urea and methanol
EP2930141A1 (en) * 2014-04-08 2015-10-14 Casale Sa A method for revamping a front-end of an ammonia plant
DE102015210801A1 (en) 2015-06-12 2016-12-15 Thyssenkrupp Ag Multi-pressure process for the production of ammonia without enrichment of inert gas

Also Published As

Publication number Publication date
WO2018166865A1 (en) 2018-09-20
DE102017204208A1 (en) 2018-09-20

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