EA201992148A1 - METHOD AND INSTALLATION FOR RECEIVING AND PROCESSING SYNTHESIS-GAS MIXTURE - Google Patents
METHOD AND INSTALLATION FOR RECEIVING AND PROCESSING SYNTHESIS-GAS MIXTUREInfo
- 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
Links
Classifications
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- 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
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- 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
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- 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
- 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
- C01B2203/0233—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being a steam reforming step
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/02—Processes for making hydrogen or synthesis gas
- C01B2203/0205—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
- C01B2203/0415—Purification by absorption in liquids
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- 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
- C01B2203/0435—Catalytic purification
- C01B2203/0445—Selective methanation
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- 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
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- 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
- C01B2203/141—At least two reforming, decomposition or partial oxidation steps in parallel
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- 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
- C01B2203/142—At least two reforming, decomposition or partial oxidation steps in series
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- 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)
- 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.
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 |
Family
ID=61599160
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)
Country | Link |
---|---|
DE (1) | DE102017204208A1 (en) |
EA (1) | EA201992148A1 (en) |
WO (1) | WO2018166865A1 (en) |
Families Citing this family (4)
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)
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 |
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2017
- 2017-03-14 DE DE102017204208.7A patent/DE102017204208A1/en not_active Ceased
-
2018
- 2018-03-07 WO PCT/EP2018/055612 patent/WO2018166865A1/en active Application Filing
- 2018-03-07 EA EA201992148A patent/EA201992148A1/en unknown
Also Published As
Publication number | Publication date |
---|---|
WO2018166865A1 (en) | 2018-09-20 |
DE102017204208A1 (en) | 2018-09-20 |
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