PL423002A1 - Zinc promoted catalyst of carbon monoxide steam conversion and method for obtaining it - Google Patents
Zinc promoted catalyst of carbon monoxide steam conversion and method for obtaining itInfo
- Publication number
- PL423002A1 PL423002A1 PL423002A PL42300217A PL423002A1 PL 423002 A1 PL423002 A1 PL 423002A1 PL 423002 A PL423002 A PL 423002A PL 42300217 A PL42300217 A PL 42300217A PL 423002 A1 PL423002 A1 PL 423002A1
- Authority
- PL
- Poland
- Prior art keywords
- catalyst
- obtaining
- zinc
- precursor
- possibly
- Prior art date
Links
Classifications
-
- 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
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Przedmiotem zgłoszenia jest promotowany katalizator cynkowy parowej konwersji tlenku węgla, który charakteryzuje się tym, że prekursor katalizatora jest mieszaniną hydroksywęglanów cynku, glinu i ewentualnie miedzi, w którym to prekursorze stosunek molowy Cu/Zn mieści się w zakresie od 0 do 0,8, korzystnie od 0 do 0,2 a stosunek molowy (Cu+Zn)/Al mieści się w zakresie od 0,5 do 0,9, korzystnie od 0,6 do 0,8, zaś finalny katalizator zawiera promotory w postaci metali I grupy układu okresowego o sumarycznym stężeniu w zakresie od 0,1 do 10,0% wag. Przedmiotem zgłoszenia jest też sposób otrzymywania katalizatora, który polega na tym, że syntezę prekursora katalizatora, będącego mieszaniną hydroksywęglanów cynku, glinu i ewentualnie miedzi, prowadzi się poprzez wytrącanie a następnie filtrację wodnej zawiesiny prekursora, jego suszenie i kalcynację prowadzącą do uzyskania formy tlenkowej katalizatora, którą po rozdrobnieniu i ewentualnie zarabianiu ze środkiem zmniejszającym tarcie i z wodnym roztworem węglanu i/lub wodorotlenku metalu I grupy układu okresowego formuje się w kształtki o średnicy zewnętrznej okręgu opisanego na przekroju mieszczącej się w zakresie od 1 do 12 mm, a następnie suszy i ewentualnie impregnuje wodnym roztworem węglanów metali I grupy i suszy otrzymując produkt końcowy.The subject of the application is a promoted zinc catalyst of steam conversion of carbon monoxide, which is characterized in that the catalyst precursor is a mixture of zinc, aluminum and possibly copper hydroxycarbonates, in which precursor the Cu / Zn molar ratio ranges from 0 to 0.8, preferably from 0 to 0.2 and the molar ratio (Cu + Zn) / Al is in the range of 0.5 to 0.9, preferably 0.6 to 0.8, and the final catalyst contains promoters in the form of metals of group I of the system periodic with a total concentration in the range of 0.1 to 10.0 wt. The subject of the application is also a method of obtaining a catalyst, which consists in the fact that the synthesis of a catalyst precursor, which is a mixture of zinc, aluminum and possibly copper hydroxycarbonates, is carried out by precipitation and then filtration of the aqueous suspension of the precursor, its drying and calcination leading to obtaining the oxide form of the catalyst, which, after crushing and possibly earning with a friction reducing agent and with an aqueous solution of metal carbonate and / or hydroxide of the first group of the periodic table, is formed into shaped pieces with an outer diameter of the circle described on the cross-section in the range from 1 to 12 mm, and then dried and possibly impregnated aqueous solution of Group I metal carbonates and dried to obtain the final product.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PL423002A PL235786B1 (en) | 2017-09-29 | 2017-09-29 | Zinc promoted catalyst of carbon monoxide steam conversion and method for obtaining it |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PL423002A PL235786B1 (en) | 2017-09-29 | 2017-09-29 | Zinc promoted catalyst of carbon monoxide steam conversion and method for obtaining it |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| PL423002A1 true PL423002A1 (en) | 2019-04-08 |
| PL235786B1 PL235786B1 (en) | 2020-10-19 |
Family
ID=65992118
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PL423002A PL235786B1 (en) | 2017-09-29 | 2017-09-29 | Zinc promoted catalyst of carbon monoxide steam conversion and method for obtaining it |
Country Status (1)
| Country | Link |
|---|---|
| PL (1) | PL235786B1 (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5019547A (en) * | 1989-04-24 | 1991-05-28 | Institut Francais Du Petrole | Process for preparing precursors of catalysts containing copper, aluminum and zinc, usable for the synthesis and the decomposition of methanol and catalysts obtained from the precursors |
| US6627572B1 (en) * | 2002-03-22 | 2003-09-30 | Sud-Chemie Inc. | Water gas shift catalyst |
| WO2010000387A1 (en) * | 2008-07-03 | 2010-01-07 | Haldor Topsøe A/S | Process for operating hts reactor |
| WO2013054092A1 (en) * | 2011-10-14 | 2013-04-18 | Johnson Matthey Public Limited Company | Catalyst precursor |
-
2017
- 2017-09-29 PL PL423002A patent/PL235786B1/en unknown
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5019547A (en) * | 1989-04-24 | 1991-05-28 | Institut Francais Du Petrole | Process for preparing precursors of catalysts containing copper, aluminum and zinc, usable for the synthesis and the decomposition of methanol and catalysts obtained from the precursors |
| US6627572B1 (en) * | 2002-03-22 | 2003-09-30 | Sud-Chemie Inc. | Water gas shift catalyst |
| WO2010000387A1 (en) * | 2008-07-03 | 2010-01-07 | Haldor Topsøe A/S | Process for operating hts reactor |
| WO2013054092A1 (en) * | 2011-10-14 | 2013-04-18 | Johnson Matthey Public Limited Company | Catalyst precursor |
Also Published As
| Publication number | Publication date |
|---|---|
| PL235786B1 (en) | 2020-10-19 |
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