RU2007108655A - Способ получения мочевины из аммиака диоксида углерода - Google Patents

Способ получения мочевины из аммиака диоксида углерода Download PDF

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RU2007108655A
RU2007108655A RU2007108655/04A RU2007108655A RU2007108655A RU 2007108655 A RU2007108655 A RU 2007108655A RU 2007108655/04 A RU2007108655/04 A RU 2007108655/04A RU 2007108655 A RU2007108655 A RU 2007108655A RU 2007108655 A RU2007108655 A RU 2007108655A
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urea
carbon dioxide
ammonia
stage
ammonium carbamate
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RU2007108655/04A
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RU2394813C2 (ru
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Доминико РОМИТИ (CH)
Доминико РОМИТИ
Паоло СТИККИ (CH)
Паоло Стикки
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Уреа Касале С.А. (Ch)
Уреа Касале С.А.
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C273/00Preparation of urea or its derivatives, i.e. compounds containing any of the groups, the nitrogen atoms not being part of nitro or nitroso groups
    • C07C273/02Preparation of urea or its derivatives, i.e. compounds containing any of the groups, the nitrogen atoms not being part of nitro or nitroso groups of urea, its salts, complexes or addition compounds
    • C07C273/10Preparation of urea or its derivatives, i.e. compounds containing any of the groups, the nitrogen atoms not being part of nitro or nitroso groups of urea, its salts, complexes or addition compounds combined with the synthesis of ammonia
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    • 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
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    • 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
    • C01B3/384Production 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
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    • 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
    • C01B3/386Catalytic partial combustion
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    • 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
    • C01B3/50Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification
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    • 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
    • C01C1/0488Processes integrated with preparations of other compounds, e.g. methanol, urea or with processes for power generation
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    • 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
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    • C01B2203/02Processes for making hydrogen or synthesis gas
    • C01B2203/025Processes for making hydrogen or synthesis gas containing a partial oxidation step
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    • C01B2203/0465Composition of the impurity
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    • C01B2203/08Methods of heating or cooling
    • C01B2203/0805Methods of heating the process for making hydrogen or synthesis gas
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    • C01B2203/0816Heating by flames
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    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/12Feeding the process for making hydrogen or synthesis gas
    • C01B2203/1205Composition of the feed
    • C01B2203/1211Organic compounds or organic mixtures used in the process for making hydrogen or synthesis gas
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    • C01B2203/1241Natural gas or methane
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    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/12Feeding the process for making hydrogen or synthesis gas
    • C01B2203/1258Pre-treatment of the feed
    • C01B2203/1264Catalytic pre-treatment of the feed
    • C01B2203/127Catalytic desulfurisation
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    • 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)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Claims (7)

1. Способ получения мочевины из аммиака и диоксида углерода, на первой стадии которого из природного газа (2) путем его конверсии (12, 14) получают аммиак (7) и диоксид углерода (6), а на второй стадии из аммиака (7) и диоксида углерода в реакторе (20) синтеза мочевины получают содержащий мочевину и карбамат аммония раствор, из которого затем после разложения карбамата аммония выделяют мочевину (8а), отличающийся тем, что образующийся при сгорании топлива дым (5), содержащий диоксид углерода, обрабатывают водным раствором (9а), содержащим часть (7b) полученного аммиака (7), с получением водного раствора (9с) карбамата аммония и этот раствор (9с) подают на вторую стадию.
2. Способ по п.1, отличающийся тем, что водный раствор (9с) карбамата аммония подают в реактор (20) синтеза мочевины.
3. Способ по п.1, отличающийся тем, что водный раствор (9с) карбамата аммония подают в реактор (20) синтеза мочевины после прохождения через аппарат (34) для очистки воды и блок (22) разложения карбамата и выделения мочевины на второй стадии получения мочевины.
4. Способ по п.1, отличающийся тем, что образующийся при сгорании топлива дым, содержащий диоксид углерода, до обработки водным раствором (9а) аммиака, обрабатывают для удаления из него возможно содержащихся в нем оксидов азота.
5. Способ по п.1, отличающийся тем, что водный раствор (9а) аммиака получают смешением части (7b) аммиака (7) с водным раствором (9b) карбамата аммония, отбираемым из концентратора (24) на второй стадии получения мочевины.
6. Способ по п.1, отличающийся тем, что содержащий диоксид углерода дым (5) образуется в процессе конверсии (12) природного газа.
7. Способ по п.1, отличающийся тем, что содержащий диоксид углерода дым (5) образуется при выполнении первой и/или второй стадии получения мочевины.
RU2007108655/02A 2004-08-10 2005-07-22 Способ получения мочевины из аммиака и диоксида углерода RU2394813C2 (ru)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP04018981A EP1626042A1 (en) 2004-08-10 2004-08-10 Process for urea production from ammonia and carbon dioxide
EP04018981.3 2004-08-10

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RU2007108655A true RU2007108655A (ru) 2008-09-20
RU2394813C2 RU2394813C2 (ru) 2010-07-20

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US (1) US7732640B2 (ru)
EP (2) EP1626042A1 (ru)
CN (1) CN100509768C (ru)
CA (1) CA2575537C (ru)
EG (1) EG24453A (ru)
RU (1) RU2394813C2 (ru)
WO (1) WO2006015709A1 (ru)

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CN101624355B (zh) * 2009-08-10 2012-05-23 四川金象赛瑞化工股份有限公司 一种低水碳比-三段吸收-蒸发式氨冷的尿素生产中压回收工艺
CN102753518B (zh) * 2010-02-12 2015-03-11 斯塔米卡邦有限公司 尿素后处理中氨的除去
AU2011383480B2 (en) * 2011-12-15 2015-02-05 Mitsubishi Heavy Industries Engineering, Ltd. Operating method for urea manufacturing plant formed from multiple systems
EP2617708B1 (en) * 2012-01-17 2017-08-16 General Electric Technology GmbH A method of forming urea by integration of an ammonia production process in a urea production process and a system therefor
JP6306571B2 (ja) 2012-05-03 2018-04-04 スタミカーボン・ベー・フェー 尿素製造プラント
EP2690089A1 (en) * 2012-07-25 2014-01-29 Urea Casale SA Use of urea synthesis purge gas in an integrated ammonia-urea process and related plant.
US9428449B2 (en) 2013-01-16 2016-08-30 Alstom Technology Ltd Method of forming urea by integration of an ammonia production process in a urea production process and a system therefor
DE102015015524A1 (de) * 2015-12-01 2017-06-01 Linde Aktiengesellschaft Verfahren zur Erzeugung von Harnstoff
CN109070047A (zh) * 2016-02-03 2018-12-21 伊桑·诺维克 捕获二氧化碳的综合方法
DE102017222030A1 (de) * 2017-12-06 2019-06-06 Thyssenkrupp Ag Verfahren zur Bereitstellung von CO2 für die Harnstoffsynthese aus Rauch- und Synthesegas
WO2019221925A1 (en) * 2018-05-18 2019-11-21 Novomer, Inc. Integrated systems and processes for chemical production

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GB2051757B (en) * 1979-07-03 1983-01-12 Humphreys & Glasgow Ltd Co2 recovery process
EP1188710A3 (en) * 2000-09-15 2003-10-29 Haldor Topsoe A/S Process for the integrated preparation of ammonia and urea
US6448441B1 (en) * 2001-05-07 2002-09-10 Texaco, Inc. Gasification process for ammonia/urea production

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EP1776335A1 (en) 2007-04-25
RU2394813C2 (ru) 2010-07-20
EG24453A (en) 2009-07-14
WO2006015709A1 (en) 2006-02-16
EP1626042A1 (en) 2006-02-15
CA2575537A1 (en) 2006-02-16
CA2575537C (en) 2013-09-10
US20070287863A1 (en) 2007-12-13
US7732640B2 (en) 2010-06-08
CN1993317A (zh) 2007-07-04
CN100509768C (zh) 2009-07-08

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