SE7506286L - CATALYST JEMTE WAS TO PRODUCE THE SAME AS EVEN, TO TAKE COMBUSTION IN THE PRESENCE OF THE SAID CATALYST. - Google Patents
CATALYST JEMTE WAS TO PRODUCE THE SAME AS EVEN, TO TAKE COMBUSTION IN THE PRESENCE OF THE SAID CATALYST.Info
- Publication number
- SE7506286L SE7506286L SE7506286A SE7506286A SE7506286L SE 7506286 L SE7506286 L SE 7506286L SE 7506286 A SE7506286 A SE 7506286A SE 7506286 A SE7506286 A SE 7506286A SE 7506286 L SE7506286 L SE 7506286L
- Authority
- SE
- Sweden
- Prior art keywords
- oxide
- metal
- alumina
- catalyst
- rare earths
- Prior art date
Links
- 239000003054 catalyst Substances 0.000 title abstract 4
- 238000002485 combustion reaction Methods 0.000 title abstract 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 abstract 5
- 229910052751 metal Inorganic materials 0.000 abstract 5
- 239000002184 metal Substances 0.000 abstract 5
- WGLPBDUCMAPZCE-UHFFFAOYSA-N Trioxochromium Chemical compound O=[Cr](=O)=O WGLPBDUCMAPZCE-UHFFFAOYSA-N 0.000 abstract 4
- 229910000423 chromium oxide Inorganic materials 0.000 abstract 4
- QGLKJKCYBOYXKC-UHFFFAOYSA-N nonaoxidotritungsten Chemical compound O=[W]1(=O)O[W](=O)(=O)O[W](=O)(=O)O1 QGLKJKCYBOYXKC-UHFFFAOYSA-N 0.000 abstract 4
- 229910001930 tungsten oxide Inorganic materials 0.000 abstract 4
- 238000001354 calcination Methods 0.000 abstract 2
- 229910044991 metal oxide Inorganic materials 0.000 abstract 2
- 150000004706 metal oxides Chemical class 0.000 abstract 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 abstract 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 abstract 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 abstract 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 abstract 1
- 150000001399 aluminium compounds Chemical class 0.000 abstract 1
- 229910052788 barium Inorganic materials 0.000 abstract 1
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 abstract 1
- 229910052791 calcium Inorganic materials 0.000 abstract 1
- 239000011575 calcium Substances 0.000 abstract 1
- 229910052799 carbon Inorganic materials 0.000 abstract 1
- 230000003197 catalytic effect Effects 0.000 abstract 1
- 239000000446 fuel Substances 0.000 abstract 1
- 239000011872 intimate mixture Substances 0.000 abstract 1
- 239000000463 material Substances 0.000 abstract 1
- 150000002736 metal compounds Chemical class 0.000 abstract 1
- 229910052697 platinum Inorganic materials 0.000 abstract 1
- 238000002360 preparation method Methods 0.000 abstract 1
- 229910052710 silicon Inorganic materials 0.000 abstract 1
- 239000010703 silicon Substances 0.000 abstract 1
- 230000003019 stabilising effect Effects 0.000 abstract 1
- 229910052712 strontium Inorganic materials 0.000 abstract 1
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium atom Chemical compound [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 0.000 abstract 1
- 229910052718 tin Inorganic materials 0.000 abstract 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/8621—Removing nitrogen compounds
- B01D53/8625—Nitrogen oxides
- B01D53/8628—Processes characterised by a specific catalyst
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/864—Removing carbon monoxide or hydrocarbons
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/10—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of rare earths
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/24—Chromium, molybdenum or tungsten
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/54—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/56—Platinum group metals
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/61—Surface area
- B01J35/612—Surface area less than 10 m2/g
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/61—Surface area
- B01J35/613—10-100 m2/g
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Catalysts (AREA)
- Gas Burners (AREA)
Abstract
The temperature stability of platinum-alumina catalysts is increased by adding to the alumina metal oxide stabilising components, specifically a) chromium oxide and/or tungsten oxide together with at least one oxide of a metal of the group IVB or b) an oxide of a material of the rare earths and at least one metal of the group IVB or c) an oxide of a metal of the rare earths and chromium oxide and/or tungsten oxide or d) an oxide of a metal of the rare earths, chromium oxide and/or tungsten oxide together with at least one oxide of the group IVB or e) an oxide of a metal of the rare earths, chromium oxide and/or tungsten oxide and additionally one or more oxides of calcium, strontium, barium, silicon and tin. For the purpose of the preparation, an intimate mixture of alumina or alumina-forming aluminium compound and the corresponding metal compounds which form metal oxides upon calcination, are calcined at a temperature of at least 850 DEG C, or 500 DEG C in the case of e), respectively, and a catalytic amount of platinum is intercalated. The stabilised alumina after calcining at 1200 DEG C for 2 hours has a surface of 20 m<2>/g. Said platinum-alumina catalysts are particularly suitable for the combustion of carbon-containing fuels.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US05/423,114 US3956188A (en) | 1973-12-10 | 1973-12-10 | Compositions and methods for high temperature stable catalysts |
| US05/423,095 US3945946A (en) | 1973-12-10 | 1973-12-10 | Compositions and methods for high temperature stable catalysts |
| US05/423,093 US3966391A (en) | 1973-12-10 | 1973-12-10 | Method of combustion using high temperature stable catalysts |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| SE7506286L true SE7506286L (en) | 1975-06-02 |
| SE443727B SE443727B (en) | 1986-03-10 |
Family
ID=27411393
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SE7506286A SE443727B (en) | 1973-12-10 | 1975-06-02 | CATALYST COMPOSITION AND SET FOR PREPARATION |
Country Status (9)
| Country | Link |
|---|---|
| JP (1) | JPS5099988A (en) |
| AU (1) | AU500079B2 (en) |
| BR (1) | BR7410291A (en) |
| CH (1) | CH614391A5 (en) |
| DE (1) | DE2458122A1 (en) |
| ES (2) | ES432719A1 (en) |
| FR (1) | FR2253560B1 (en) |
| IT (1) | IT1024367B (en) |
| SE (1) | SE443727B (en) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2647702A1 (en) * | 1975-10-22 | 1977-04-28 | Atomic Energy Authority Uk | CATALYSTS AND METHOD FOR THE PRODUCTION THEREOF |
| MX3874E (en) * | 1975-12-29 | 1981-08-26 | Engelhard Min & Chem | IMPROVEMENTS IN METHOD TO INITIATE A COMBUSTION SYSTEM USING A CATALYST |
| JPS59199042A (en) * | 1983-04-28 | 1984-11-12 | Nissan Motor Co Ltd | Catalyst for reforming methanol |
| EP0130835B1 (en) * | 1983-07-01 | 1990-05-02 | Hitachi, Ltd. | High temperature stable catalyst, process for preparing same and process for conducting chemical reaction using same |
| FR2697831B1 (en) * | 1992-11-12 | 1994-12-09 | Rhone Poulenc Chimie | Alumina stabilized by barium and its preparation process. |
| JP4982241B2 (en) * | 2007-04-27 | 2012-07-25 | エヌ・イーケムキャット株式会社 | Exhaust gas purification catalyst for automobile, exhaust gas purification catalyst system, and exhaust gas purification method |
| US10921665B2 (en) * | 2018-11-27 | 2021-02-16 | HKC Corporation Limited | Display panel and repair method for the display panel |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3694348A (en) * | 1969-09-15 | 1972-09-26 | Natalia Robertovna Bursian | Process for the aromatization of hydrocarbons |
-
1974
- 1974-12-06 AU AU76161/74A patent/AU500079B2/en not_active Expired
- 1974-12-09 IT IT54425/74A patent/IT1024367B/en active
- 1974-12-09 DE DE19742458122 patent/DE2458122A1/en not_active Withdrawn
- 1974-12-09 CH CH1629674A patent/CH614391A5/en not_active IP Right Cessation
- 1974-12-09 BR BR10291/74A patent/BR7410291A/en unknown
- 1974-12-09 ES ES432719A patent/ES432719A1/en not_active Expired
- 1974-12-10 FR FR7440501A patent/FR2253560B1/fr not_active Expired
- 1974-12-10 JP JP49141944A patent/JPS5099988A/ja active Pending
-
1975
- 1975-06-02 SE SE7506286A patent/SE443727B/en not_active IP Right Cessation
-
1976
- 1976-09-09 ES ES451362A patent/ES451362A1/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| DE2458122A1 (en) | 1975-06-12 |
| ES432719A1 (en) | 1977-02-16 |
| CH614391A5 (en) | 1979-11-30 |
| FR2253560B1 (en) | 1981-08-07 |
| FR2253560A1 (en) | 1975-07-04 |
| JPS5099988A (en) | 1975-08-08 |
| IT1024367B (en) | 1978-06-20 |
| SE443727B (en) | 1986-03-10 |
| BR7410291A (en) | 1976-06-29 |
| AU7616174A (en) | 1976-06-10 |
| AU500079B2 (en) | 1979-05-10 |
| ES451362A1 (en) | 1977-12-01 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| ES448041A1 (en) | Compositions and methods for high temperature stable catalysts | |
| ATE134360T1 (en) | PRODUCTION OF CEMENT CLINKER IN LONG ROTARY KILN BY ADDING VOLATILE FUEL ELEMENTS DIRECTLY INTO THE CALCINATION ZONE OF THE ROTARY KULLEN | |
| KR940013602A (en) | Mixed oxide base composition of cerium and zirconium, preparation method and use thereof | |
| GB1523141A (en) | Process for the oxidation of olefins using catalysts containing various promoter elements | |
| GB913832A (en) | A process for the production of unsaturated nitriles | |
| SE7506286L (en) | CATALYST JEMTE WAS TO PRODUCE THE SAME AS EVEN, TO TAKE COMBUSTION IN THE PRESENCE OF THE SAID CATALYST. | |
| KR870010895A (en) | Selective Catalytic Reduction Catalyst | |
| ES417553A1 (en) | Oxidation of carbonaceous material | |
| KR890003268A (en) | Manufacturing method of anodite sintered body | |
| US4375571A (en) | Process for the preparation of ethylbenzene from 4-vinylcyclohexene-1 | |
| IT1022322B (en) | CATALYTIC COMPOSITION FOR THE CONVERSION OF HYDROCARBONS | |
| JPS57127446A (en) | Catalyst for gas purification | |
| KR840001848A (en) | Catalyst body for flue gas purification and its manufacturing method | |
| US3216952A (en) | Supported nickel catalyst and preparation thereof | |
| KR910018079A (en) | Phenol production catalyst and phenol production method | |
| JPS52123999A (en) | Production of synthetic zeolite | |
| SU426968A1 (en) | METHOD OF OBTAINING SPINELS BASED ON ALUMINUM OXIDE | |
| NL7505135A (en) | PROCESS FOR PREPARING STABILIZED, BONDABLE CALCIUM SULPHATE BY CONVERSION OF CALCIUM COMPOUNDS WITH SULFURIC ACID. | |
| KR930000426A (en) | Method of manufacturing bead-type far infrared radiation ceramics | |
| SU563379A1 (en) | Method of producing the cement clinker | |
| SU528275A1 (en) | Raw mix for aluminate calcium cement | |
| SU381633A1 (en) | REFRACTORY CONCRETE MIXTURE | |
| GB1461425A (en) | Pigment and preparation thereof | |
| KR910014471A (en) | Modified bismuth vanadate pigment in monoclinic crystalline form and preparation method thereof | |
| SU1724579A2 (en) | Method of producing lanthanum chromite |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| NUG | Patent has lapsed |
Ref document number: 7506286-9 Effective date: 19891128 Format of ref document f/p: F |