RU2014126869A - Катализатор конверсии водяного газа, функционирующий при средней температуре, и способ его производства - Google Patents
Катализатор конверсии водяного газа, функционирующий при средней температуре, и способ его производства Download PDFInfo
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- 238000000034 method Methods 0.000 title claims abstract 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract 4
- 239000003054 catalyst Substances 0.000 title claims 3
- 238000006243 chemical reaction Methods 0.000 title claims 3
- 229960001545 hydrotalcite Drugs 0.000 claims abstract 15
- 229910001701 hydrotalcite Inorganic materials 0.000 claims abstract 15
- -1 hydrotalcite compound Chemical class 0.000 claims abstract 15
- GDVKFRBCXAPAQJ-UHFFFAOYSA-A dialuminum;hexamagnesium;carbonate;hexadecahydroxide Chemical class [OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Al+3].[Al+3].[O-]C([O-])=O GDVKFRBCXAPAQJ-UHFFFAOYSA-A 0.000 claims abstract 13
- 239000007864 aqueous solution Substances 0.000 claims abstract 4
- 239000000843 powder Substances 0.000 claims abstract 4
- 239000002244 precipitate Substances 0.000 claims abstract 4
- ONDPHDOFVYQSGI-UHFFFAOYSA-N zinc nitrate Chemical compound [Zn+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ONDPHDOFVYQSGI-UHFFFAOYSA-N 0.000 claims abstract 4
- 230000002194 synthesizing effect Effects 0.000 claims abstract 3
- BNGXYYYYKUGPPF-UHFFFAOYSA-M (3-methylphenyl)methyl-triphenylphosphanium;chloride Chemical compound [Cl-].CC1=CC=CC(C[P+](C=2C=CC=CC=2)(C=2C=CC=CC=2)C=2C=CC=CC=2)=C1 BNGXYYYYKUGPPF-UHFFFAOYSA-M 0.000 claims abstract 2
- UIIMBOGNXHQVGW-DEQYMQKBSA-M Sodium bicarbonate-14C Chemical compound [Na+].O[14C]([O-])=O UIIMBOGNXHQVGW-DEQYMQKBSA-M 0.000 claims abstract 2
- XTVVROIMIGLXTD-UHFFFAOYSA-N copper(II) nitrate Chemical compound [Cu+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O XTVVROIMIGLXTD-UHFFFAOYSA-N 0.000 claims abstract 2
- 238000001914 filtration Methods 0.000 claims abstract 2
- 150000002823 nitrates Chemical class 0.000 claims abstract 2
- 239000002245 particle Substances 0.000 claims abstract 2
- 239000000243 solution Substances 0.000 claims abstract 2
- 150000001875 compounds Chemical class 0.000 claims 7
- 239000010949 copper Substances 0.000 claims 5
- 239000011701 zinc Substances 0.000 claims 5
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims 3
- 230000015572 biosynthetic process Effects 0.000 claims 3
- 238000003786 synthesis reaction Methods 0.000 claims 3
- 239000007789 gas Substances 0.000 claims 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims 1
- 239000001257 hydrogen Substances 0.000 claims 1
- 229910052739 hydrogen Inorganic materials 0.000 claims 1
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Abstract
1. Соединение гидроталькитного типа формулы (I):[CuZnAl(OH)](A), k HO (I)где (А) означает либо карбонатный анион, либо силикатный анион,x>0, y>0, w>0, (x+y)=(1-w), 1<[(x+y)/w]<5 и1/99≤x/y≤1/1.2. Соединение гидроталькитного типа формулы (I) по п. 1, в котором атомное отношение x/y≤1/2.3. Соединение гидроталькитного типа формулы (I) по п. 2, в котором атомное отношение x/у≤1/5.4. Соединение гидроталькитного типа формулы (I) по одному из пп. 1-3, в котором атомное отношение х/у≥1/10.5. Соединение гидроталькитного типа формулы (I) по одному из пп. 1-3, в котором атомное отношение [(x+y)/w] больше или равно двум.6. Соединение гидроталькитного типа формулы (I) по одному из пп. 1-3, в котором атомное отношение [(x+y)/w] меньше или равно трем.7. Соединение гидроталькитного типа, соответствующее одной из следующих формул:[CuZnAl(OH)](CO )k HO,[CuZnAl(OH)](CO )k HO,[CuZnAl(OH)](CO )k HO,[CuZnAl(OH)](CO )k HO.8. Способ синтеза соединения гидроталькитного типа формулы (I) по одному из пп. 1-7, включающий следующие стадии:стадию A, в ходе которой водный раствор, содержащий одновременно нитрат алюминия, нитрат цинка и нитрат меди, получают путем смешивания указанных нитратов в нужном молярном соотношении с водой;стадию B, в ходе которой указанный раствор, полученный на стадии A, смешивают с водным раствором гидрокарбоната натрия, при этом pH поддерживают в интервале от 8 до 10, предпочтительно около 9 с получением осадка;стадию C, в ходе которой указанный осадок, полученный на стадии B, отделяют путем фильтрации, промывают, после чего сушат, получая заданное соединение гидроталькитного типа указанной формулы (I).9. Способ синтеза соединения гидроталькитного типа формулы (I) по п. 8, дополнительно включающий стадию D, в ходе которой указанное соединение гидроталькитного типа формулы (I), приведенной выше, полученное на стадии C, размалывают с получением порошка, состоящего из частиц ука
Claims (12)
1. Соединение гидроталькитного типа формулы (I):
[CuxZnyAlw(OH)2](2x+2y+3w-2)+(A2-)(2x+2y+3w-2)/2, k H2O (I)
где (А2-) означает либо карбонатный анион, либо силикатный анион,
x>0, y>0, w>0, (x+y)=(1-w), 1<[(x+y)/w]<5 и
1/99≤x/y≤1/1.
2. Соединение гидроталькитного типа формулы (I) по п. 1, в котором атомное отношение x/y≤1/2.
3. Соединение гидроталькитного типа формулы (I) по п. 2, в котором атомное отношение x/у≤1/5.
4. Соединение гидроталькитного типа формулы (I) по одному из пп. 1-3, в котором атомное отношение х/у≥1/10.
5. Соединение гидроталькитного типа формулы (I) по одному из пп. 1-3, в котором атомное отношение [(x+y)/w] больше или равно двум.
6. Соединение гидроталькитного типа формулы (I) по одному из пп. 1-3, в котором атомное отношение [(x+y)/w] меньше или равно трем.
7. Соединение гидроталькитного типа, соответствующее одной из следующих формул:
[Cu0,075Zn0,675Al0,25(OH)2]0,25+(CO3 2-)0,125 k H2O,
[Cu0,150Zn0,600Al0,25(OH)2]0,25+(CO3 2-)0,125 k H2O,
[Cu0,066Zn0,600Al0,333(OH)2]0,25+(CO3 2-)0,125 k H2O,
[Cu0,134Zn0,532Al0,333(OH)2]0,31+(CO3 2-)0,155 k H2O.
8. Способ синтеза соединения гидроталькитного типа формулы (I) по одному из пп. 1-7, включающий следующие стадии:
стадию A, в ходе которой водный раствор, содержащий одновременно нитрат алюминия, нитрат цинка и нитрат меди, получают путем смешивания указанных нитратов в нужном молярном соотношении с водой;
стадию B, в ходе которой указанный раствор, полученный на стадии A, смешивают с водным раствором гидрокарбоната натрия, при этом pH поддерживают в интервале от 8 до 10, предпочтительно около 9 с получением осадка;
стадию C, в ходе которой указанный осадок, полученный на стадии B, отделяют путем фильтрации, промывают, после чего сушат, получая заданное соединение гидроталькитного типа указанной формулы (I).
9. Способ синтеза соединения гидроталькитного типа формулы (I) по п. 8, дополнительно включающий стадию D, в ходе которой указанное соединение гидроталькитного типа формулы (I), приведенной выше, полученное на стадии C, размалывают с получением порошка, состоящего из частиц указанного соединения гидроталькитного типа указанной формулы (I).
10. Соединение, отличающееся тем, что оно получено способом, включающим следующие стадии:
стадию F, в ходе которой порошок соединения гидроталькитного типа формулы (I) по одному из.п. 1-7 подвергают обжигу;
стадию G, в ходе которой обожженный порошок, полученный на стадии F, восстанавливают водородом при температуре менее 230°C.
11. Применение соединения, полученного способом по п. 10, в качестве катализатора реакции конверсии водяного газа для получения синтез-газа.
12. Применение соединения, полученного способом по п. 10, в качестве катализатора синтеза метанола.
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EP11306604.7 | 2011-12-02 | ||
EP11306604.7A EP2599541B1 (en) | 2011-12-02 | 2011-12-02 | Process for preparing a water gas shift catalyst operating at medium temperatures |
PCT/EP2012/072595 WO2013079323A1 (en) | 2011-12-02 | 2012-11-14 | Water gas shift catalyst operating at medium temperatures and a process for its preparation |
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US (1) | US20140309102A1 (ru) |
EP (1) | EP2599541B1 (ru) |
JP (1) | JP6165759B2 (ru) |
KR (1) | KR20140098823A (ru) |
CN (1) | CN104080528A (ru) |
BR (1) | BR112014013331A2 (ru) |
CA (1) | CA2856445A1 (ru) |
ES (1) | ES2628881T3 (ru) |
PT (1) | PT2599541T (ru) |
RU (1) | RU2014126869A (ru) |
WO (1) | WO2013079323A1 (ru) |
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GB201519133D0 (en) | 2015-10-29 | 2015-12-16 | Johnson Matthey Plc | Process |
GB201519139D0 (en) | 2015-10-29 | 2015-12-16 | Johnson Matthey Plc | Process |
GB2546131B (en) | 2015-10-29 | 2019-04-10 | Johnson Matthey Plc | Water-gas shift catalyst |
EP3254760A1 (en) | 2016-06-07 | 2017-12-13 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Process to synthesize a catalyst performing water-gas shift reaction at a high temperature |
WO2018015824A1 (en) * | 2016-07-18 | 2018-01-25 | Sabic Global Technologies B.V. | Process for high-pressure hydrogenation of carbon dioxide to syngas in the presence of a copper/zinc/zirconium mixed metal oxide catalyst |
GB201701382D0 (en) * | 2017-01-27 | 2017-03-15 | Turner Rhodri | Catalyst suitable for methonal synthesis |
GB201703558D0 (en) | 2017-03-06 | 2017-04-19 | Univ Oxford Innovation Ltd | catalysts |
WO2018175452A1 (en) * | 2017-03-20 | 2018-09-27 | Ryan David K | Catalytic hydrogen production |
CN109833858B (zh) * | 2017-11-28 | 2022-01-25 | 中国石油天然气股份有限公司 | 烯烃催化剂用载体硅胶的制备方法 |
CN109621967B (zh) * | 2018-12-26 | 2022-03-11 | 西安向阳航天材料股份有限公司 | 一种铜系低温变换催化剂的制备方法 |
GB2614844A (en) * | 2020-09-24 | 2023-07-19 | Dastur Energy Inc | System and method for conditioning syngas and capturing carbon dioxide from conditioned syngas for production of power, chemicals, and other value added |
CN115246955B (zh) * | 2021-04-28 | 2024-02-13 | 中国石油化工股份有限公司 | 一种层状结构吸酸剂及其制备方法和应用 |
KR20240019237A (ko) * | 2022-01-14 | 2024-02-14 | 세토라스 홀딩스 가부시키가이샤 | 아연 함유 하이드로탈사이트 |
CN114824320A (zh) * | 2022-03-07 | 2022-07-29 | 国网综合能源服务集团有限公司 | 一种具有铜包覆氧化锌界面的铜基催化剂的制备方法及其低温催化水煤气变换反应的应用 |
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DE2056612C3 (de) * | 1970-11-18 | 1979-09-13 | Basf Ag, 6700 Ludwigshafen | Verfahren zur Herstellung von Methanol |
DE2846614C3 (de) * | 1978-10-26 | 1982-05-19 | Basf Ag, 6700 Ludwigshafen | Verfahren zur Herstellung von Methanol |
EP0234745B1 (en) | 1986-01-29 | 1991-06-12 | Dyson Refractories Limited | Catalysts |
DK167146B1 (da) * | 1990-09-11 | 1993-09-06 | Topsoe Haldor As | Fremgangsmaade og katalysator til fremstilling af aromatiske forbindelser |
JP3482459B2 (ja) * | 2000-03-06 | 2003-12-22 | 独立行政法人産業技術総合研究所 | メタノールの部分酸化反応による水素製造触媒及びその製造法 |
JP3496051B2 (ja) * | 2000-06-07 | 2004-02-09 | 独立行政法人産業技術総合研究所 | メタノールの酸化的水蒸気改質反応による水素ガス製造触媒及びその製造法 |
US6693057B1 (en) | 2002-03-22 | 2004-02-17 | Sud-Chemie Inc. | Water gas shift catalyst |
US7749376B2 (en) * | 2005-08-15 | 2010-07-06 | Sud-Chemie Inc. | Process for sulfur adsorption using copper-containing catalyst |
KR101484793B1 (ko) * | 2007-04-10 | 2015-01-20 | 이데미쓰 고산 가부시키가이샤 | 촉매 전구체 물질 및 그것을 이용한 촉매 |
US20090149324A1 (en) | 2007-12-05 | 2009-06-11 | Basf Catalysts Llc | Low temperature water gas shift catalyst |
EP2141118B1 (en) | 2008-07-03 | 2013-08-07 | Haldor Topsoe A/S | Chromium-free water gas shift catalyst |
-
2011
- 2011-12-02 PT PT113066047T patent/PT2599541T/pt unknown
- 2011-12-02 ES ES11306604.7T patent/ES2628881T3/es active Active
- 2011-12-02 EP EP11306604.7A patent/EP2599541B1/en not_active Not-in-force
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- 2012-11-14 CA CA2856445A patent/CA2856445A1/en not_active Abandoned
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- 2012-11-14 WO PCT/EP2012/072595 patent/WO2013079323A1/en active Application Filing
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ES2628881T3 (es) | 2017-08-04 |
JP6165759B2 (ja) | 2017-07-19 |
JP2015505799A (ja) | 2015-02-26 |
EP2599541A1 (en) | 2013-06-05 |
KR20140098823A (ko) | 2014-08-08 |
CN104080528A (zh) | 2014-10-01 |
US20140309102A1 (en) | 2014-10-16 |
PT2599541T (pt) | 2017-06-30 |
EP2599541B1 (en) | 2017-05-03 |
WO2013079323A1 (en) | 2013-06-06 |
CA2856445A1 (en) | 2013-06-06 |
BR112014013331A2 (pt) | 2017-06-13 |
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