RU2011117064A - Способ получения синтез-газа для производства аммиака - Google Patents
Способ получения синтез-газа для производства аммиака Download PDFInfo
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- C01B2203/1211—Organic compounds or organic mixtures used in the process for making hydrogen or synthesis gas
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Abstract
1. Способ получения синтез-газа для производства аммиака из углеводородсодержащего сырья (10), включающий стадии паровой конверсии углеводородсодержащего сырья в установке (12) первичной конверсии с получением частично конвертированного газового потока (13) и вторичной конверсии этого потока в установке (14) вторичной конверсии, работающей в условиях избытка воздуха, способ, отличающийся тем, что: ! установки первичной и вторичной конверсии работают при давлении по меньшей мере 35 бар; ! продуктовый синтез-газ (16) на выходе из установки вторичной конверсии охлаждают и подвергают среднетемпературной каталитической конверсии с превращением СО в СО2 и H2, которую проводят на катализаторе на основе меди по существу при постоянной температуре в диапазоне 220-320°С; ! ниже по потоку после упомянутой среднетемпературной конверсии из синтез-газа удаляют СО2 посредством физической абсорбции; ! соотношение пар-углерод в установке (12) первичной конверсии составляет менее 2,7. ! 2. Способ по п.1, в котором частично конвертированный синтез-газ (13) на выходе из установки (12) первичной конверсии имеет температуру в диапазоне 650-750°С. ! 3. Способ по п.1, в котором проводят дополнительную низкотемпературную конверсию потока синтез-газа (20) ниже по потоку после упомянутой среднетемпературной каталитической конверсии. ! 4. Способ по любому из предшествующих пунктов, в котором СО2 удаляют, используя метанол в качестве растворителя или органический растворитель. ! 5. Оборудование для получения синтез-газа для производства аммиака, выполненное с возможностью осуществления способа по любому из предыдущих пунктов, включающее установку (12) первичн�
Claims (7)
1. Способ получения синтез-газа для производства аммиака из углеводородсодержащего сырья (10), включающий стадии паровой конверсии углеводородсодержащего сырья в установке (12) первичной конверсии с получением частично конвертированного газового потока (13) и вторичной конверсии этого потока в установке (14) вторичной конверсии, работающей в условиях избытка воздуха, способ, отличающийся тем, что:
установки первичной и вторичной конверсии работают при давлении по меньшей мере 35 бар;
продуктовый синтез-газ (16) на выходе из установки вторичной конверсии охлаждают и подвергают среднетемпературной каталитической конверсии с превращением СО в СО2 и H2, которую проводят на катализаторе на основе меди по существу при постоянной температуре в диапазоне 220-320°С;
ниже по потоку после упомянутой среднетемпературной конверсии из синтез-газа удаляют СО2 посредством физической абсорбции;
соотношение пар-углерод в установке (12) первичной конверсии составляет менее 2,7.
2. Способ по п.1, в котором частично конвертированный синтез-газ (13) на выходе из установки (12) первичной конверсии имеет температуру в диапазоне 650-750°С.
3. Способ по п.1, в котором проводят дополнительную низкотемпературную конверсию потока синтез-газа (20) ниже по потоку после упомянутой среднетемпературной каталитической конверсии.
4. Способ по любому из предшествующих пунктов, в котором СО2 удаляют, используя метанол в качестве растворителя или органический растворитель.
5. Оборудование для получения синтез-газа для производства аммиака, выполненное с возможностью осуществления способа по любому из предыдущих пунктов, включающее установку (12) первичной конверсии и установку (14) вторичной конверсии для конверсии углеводородного сырья (10) и дополнительно включающее по меньшей мере реактор (19) среднетемпературной конверсии для конверсии монооксида углерода, содержащегося в продуктовом газе (16) из установки (14) вторичной конверсии, в СО2 и Н2, и устройство (24) для удаления СО2 ниже по потоку от реактора (19) среднетемпературной конверсии, осуществляемого посредством физической абсорбции.
6. Оборудование по п.5, дополнительно включающее реактор (21) низкотемпературной конверсии ниже по потоку от реактора (19) среднетемпературной конверсии.
7. Способ реконструкции головной части комплекса оборудования для производства аммиака, отличающийся тем, что обеспечивают по меньшей мере реактор (19) среднетемпературной конверсии и устройство (24) для удаления СО2, размещаемое ниже по потоку от этого реактора (19) и работающее с использованием физической абсорбции.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP08017372.7 | 2008-10-02 | ||
EP08017372A EP2172417A1 (en) | 2008-10-02 | 2008-10-02 | Process for the production of ammonia synthesis gas |
PCT/EP2009/060970 WO2010037598A1 (en) | 2008-10-02 | 2009-08-26 | Process for producing ammonia synthesis gas |
Publications (2)
Publication Number | Publication Date |
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RU2011117064A true RU2011117064A (ru) | 2012-11-10 |
RU2510883C2 RU2510883C2 (ru) | 2014-04-10 |
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Application Number | Title | Priority Date | Filing Date |
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RU2011117064/05A RU2510883C2 (ru) | 2008-10-02 | 2009-08-26 | Способ получения синтез-газа для производства аммиака |
Country Status (13)
Country | Link |
---|---|
US (1) | US8545727B2 (ru) |
EP (2) | EP2172417A1 (ru) |
CN (1) | CN102171135B (ru) |
AR (1) | AR075281A1 (ru) |
AU (1) | AU2009299990B2 (ru) |
BR (1) | BRPI0920435B1 (ru) |
CA (1) | CA2737649C (ru) |
CL (1) | CL2011000725A1 (ru) |
DK (1) | DK2334591T4 (ru) |
MX (1) | MX2011002860A (ru) |
MY (1) | MY154901A (ru) |
RU (1) | RU2510883C2 (ru) |
WO (1) | WO2010037598A1 (ru) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2404869A1 (en) * | 2010-07-06 | 2012-01-11 | Ammonia Casale S.A. | Process for producing ammonia synthesis gas |
CA2875696C (en) | 2012-06-27 | 2020-09-01 | Grannus, Llc | Polygeneration production of power and fertilizer through emissions capture |
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 |
EP3050849A1 (en) * | 2015-01-27 | 2016-08-03 | Casale SA | A process for the synthesis of ammonia |
DE102015210801A1 (de) | 2015-06-12 | 2016-12-15 | Thyssenkrupp Ag | Mehrdruckverfahren zur Herstellung von Ammoniak ohne Anreicherung von Inertgas |
WO2017096337A1 (en) | 2015-12-04 | 2017-06-08 | Grannus, Llc | Polygeneration production of hydrogen for use in various industrial processes |
CA3069493A1 (en) | 2017-07-13 | 2019-01-17 | Haldor Topsoe A/S | Method and catalysts for the production of ammonia synthesis gas |
Family Cites Families (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SU327764A1 (ru) * | 1969-06-11 | 1977-04-25 | Способ производства аммиака | |
EP0031209B1 (en) * | 1979-12-19 | 1986-01-29 | Imperial Chemical Industries Plc | Purification of hydrogen |
FR2473032A1 (fr) * | 1980-01-07 | 1981-07-10 | Banquy David | Procede de production d'ammoniac et du gaz de synthese correspondant |
EP0157480B1 (en) * | 1984-03-02 | 1989-07-26 | Imperial Chemical Industries Plc | Process for producing ammonia synthesis gas |
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 |
US6232352B1 (en) * | 1999-11-01 | 2001-05-15 | Acetex Limited | Methanol plant retrofit for acetic acid manufacture |
US7220505B2 (en) * | 2003-03-18 | 2007-05-22 | Kellogg Brown & Root Llc | Autothermal reformer-reforming exchanger arrangement for hydrogen production |
DE10334590B4 (de) * | 2003-07-28 | 2006-10-26 | Uhde Gmbh | Verfahren zur Gewinnung von Wasserstoff aus einem methanhaltigen Gas, insbesondere Erdgas und Anlage zur Durchführung des Verfahrens |
US20100015039A1 (en) * | 2004-05-28 | 2010-01-21 | Hyradix, Inc. | Hydrogen generation process using partial oxidation/steam reforming |
EP1698588A1 (en) * | 2005-03-04 | 2006-09-06 | Ammonia Casale S.A. | Ammonia synthesis process |
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Publication number | Publication date |
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CA2737649C (en) | 2017-03-28 |
MX2011002860A (es) | 2011-06-16 |
CN102171135B (zh) | 2014-05-28 |
MY154901A (en) | 2015-08-28 |
DK2334591T4 (da) | 2019-06-03 |
DK2334591T3 (en) | 2015-01-19 |
CL2011000725A1 (es) | 2011-08-26 |
CA2737649A1 (en) | 2010-04-08 |
EP2334591B2 (en) | 2019-03-06 |
EP2334591A1 (en) | 2011-06-22 |
AU2009299990A1 (en) | 2010-04-08 |
US8545727B2 (en) | 2013-10-01 |
US20110168948A1 (en) | 2011-07-14 |
AR075281A1 (es) | 2011-03-23 |
EP2172417A1 (en) | 2010-04-07 |
EP2334591B1 (en) | 2014-10-15 |
BRPI0920435B1 (pt) | 2019-05-28 |
BRPI0920435A2 (pt) | 2015-12-22 |
WO2010037598A1 (en) | 2010-04-08 |
CN102171135A (zh) | 2011-08-31 |
RU2510883C2 (ru) | 2014-04-10 |
AU2009299990B2 (en) | 2015-04-09 |
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