WO1998051401A1 - Gold based catalyst for exhaust gas purification - Google Patents
Gold based catalyst for exhaust gas purification Download PDFInfo
- Publication number
- WO1998051401A1 WO1998051401A1 PCT/BG1998/000010 BG9800010W WO9851401A1 WO 1998051401 A1 WO1998051401 A1 WO 1998051401A1 BG 9800010 W BG9800010 W BG 9800010W WO 9851401 A1 WO9851401 A1 WO 9851401A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- catalyst
- gold
- oxides
- catalyst according
- support
- Prior art date
Links
Classifications
-
- 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
- B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
- B01D53/94—Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
- B01D53/9445—Simultaneously removing carbon monoxide, hydrocarbons or nitrogen oxides making use of three-way catalysts [TWC] or four-way-catalysts [FWC]
- B01D53/945—Simultaneously removing carbon monoxide, hydrocarbons or nitrogen oxides making use of three-way catalysts [TWC] or four-way-catalysts [FWC] 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
- B01D53/8671—Removing components of defined structure not provided for in B01D53/8603 - B01D53/8668
- B01D53/8675—Ozone
-
- 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
- B01J23/48—Silver or gold
- B01J23/52—Gold
-
- 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
- B01J23/66—Silver or gold
-
- 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
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/10—Capture or disposal of greenhouse gases of nitrous oxide (N2O)
-
- 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
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
Definitions
- the invention relates to a gold catalyst for the oxidation of carbon monoxide and hydrocarbons, reduction of nitrous oxides and the degradation of ozone.
- a reduction of the emission of noxious gases from the combustion engines may be achieved by the use of PGM-based catalysts.
- PGM-based catalysts function satisfactorily at temperatures higher than 300°C. Moisture and sulphur dioxide common for the exhaust gases, severely affect their performance at lower temperatures. It is known fact that 80% of the noxious gases from the combustion engine are emitted during the cold start of the engine, the first 3 to 5 minutes, where the conventional catalysts are not affective.
- the PGM-based catalysts are even less effective for diesel vehicles where the temperature of the emitted gases in lower than the temperature of the exhaust gases from the gasoline passenger car. Conversion of the TPM, CO, HC and NOx (4-way catalyst) is considered a major challenge for diesel vehicle application in the future. Further, the high working temperatures of the PGM catalysts make them unsuitable for air purification in buildings, aircrafts and industrial sites.
- Gold has been long regarded as far less catalytically active than the platinum group metals (PGM's). Recent publications in the literature have shown that gold, when highly dispersed on reducible oxides, can be active for low temperature oxidation of CO. However, gold containing catalysts as shown in the literature, ere either to costly, with gold concentration up to 12%, or show poor conversion at the higher flow rate of gases common for the working conditions. Thus, these catalysts are not suitable for industrial applications and do not have real commercial value.
- German patent No. 3914294 describes a catalyst in which the gold is captured on an iron oxide-containing support which includes also alumina or aluminosilicate.
- this catalyst has poor conversion of carbon monoxide at higher space velocity and is severely affected by moisture and sulphur dioxide.
- gold catalysts supported on cobalt oxide, titanium oxide and iron oxide described in the literature are:
- a catalyst for simultaneous oxidation and reduction reactions comprises a porous mixed oxides support having captured thereon a complex comprising gold and reducible oxide of a transition metal selected from chromium, copper, cobalt, manganese, iron or a combination of this metals.
- concentration of the gold is from 0.1%-2.5%, preferably less than 1.5%, when the total concentration of the metals in the active component should not exceed 10% from the total mass of the catalyst.
- the gold-reducible oxide complex contains chemical and physical bonding and is bonded to the mixed oxides support.
- the support of the catalytic composition comprises individual or mixed oxides with a large surface area typically 80 m 2 /g to 400 m 2 /g.
- Oxides composition is selected from ceria and titania oxides.
- the concentration of ceria oxide is from 30-95% and of the titania oxide from 5-25%.
- the catalyst may be in the form of powder, pellets, molded or deposited on a suitable carrier as foams, honeycombs (ceramics or metals).
- the gold-transition metal oxide particles are deposited on the mixed oxides support by the methods of the known art: impregnation, precipitation, co- precipitation, wet incipient dryness, or a combination of these techniques.
- the particles of the active component are finely dispersed throughout the support and should be of a size less than 40 nm, preferably less than 20 nm.
- the pH of the process of preparation of gold-metal oxide catalyst is of significance and should be in the range of 7.0 to 12.0, preferably 8.0 to 10.5. The adjustment of the pH value in the prescribed range is achieved by the use of alkaline compound, for example, sodium or potassium carbonates, hydroxides or ammonia.
- the catalyst is heated to a temperature in the range of 100°C to 500°C, to form fine cluster particles, immobilized on the surface of the support. The heating of the catalyst is maintained on oxidizing atmosphere or air.
- the catalyst working temperature is from 0°C to 500°C.
- the catalyst will have application also in the fuel cells technology.
- the catalyst of the invention is more effective than similar catalyst of the prior art in the oxidation of carbon monoxide and hydrocarbons at law temperatures and in presence of moisture and sulphur dioxide;
- the catalyst tolerates presence of sulphur dioxide
- the catalyst has the ability for simultaneous reduction of nitrous oxides and oxidation of carbon monoxide and hydrocarbons at low and high temperature;
- the catalyst is highly effective in the degradation of ozone at ambient temperature
- the catalyst has high catalytic activities in the simultaneous oxidation of carbon monoxide, hydrocarbons and degradation of ozone at ambient temperature and presence of moisture; 7.
- the catalyst could be used concurrently with the PGM catalysts to deal with their deficiency during the cold start of the combustion engine.
- Figure 1 shows the bonding between gold and the reducible oxide of the transition metal, Co 2 0 3 in the active cluster, while Figure 2 shows the binding between the cluster and the oxides of the support.
- Example 2 shows the bonding between gold and the reducible oxide of the transition metal, Co 2 0 3 in the active cluster, while Figure 2 shows the binding between the cluster and the oxides of the support.
- Example 1 The catalyst obtained in Example 1 and a catalyst obtained in the same way, but with A1 2 0 3 support, are tested at various temperatures in a reactor containing 1 g of the catalyst, gas flow rate 45 000 h 1 and gas composition 1% CO, 0.9% 0 2 , 350 ppm C 3 H 6 , 350 ppm C 3 H 8 , 15 ppm S0 2 , humidity 95% and balance N 2 .
- the results in Table 1 show the effect of the support on the activity of the gold catalyst in the oxidation of carbon monoxide and hydrocarbons.
- the catalyst obtained by the method described in Example 1 is tested in a reactor containing 1 g of the catalyst at a temperature of 25°C, gas flow rate 360 000 h "1 and composition of the gas 25 ppm CO, the balance dry air and air with humidity 95%.
- the catalyst obtained by the method described in Example 1 on the support of the invention and PGM catalyst on A1 2 0 3 support are tested in a reactor containing 1 g of the catalyst at temperature of 25°C, gas flow rate 60 000 h 1 and composition of the gas 1% CO, 0.9% 0 2 , 350 ppm C 3 H 6 , 350 ppm C 3 H 8 , 1000 ppm NOx, 15 ppm S0 2 , humidity 95% and the balance N 2 .
- the catalyst obtained by the method described in Example 1 on the support of the invention is tested on a reactor containing 1 g of the catalyst at various temperatures, gas flow rate 60 000 h 1 and composition of the gas l%CO, 0.7- 0.9% 0 2 , 350 ppm C 3 H 6 , 350 ppm C 3 H 8 , 1000 ppm NOx, 15 ppm S0 2 , humidity 95% and the balance N 2 .
- Table 4 are demonstrating the high activity of the catalyst of the invention, specifically at the cold start of the combustion engine.
- the catalyst obtained by the method described in Example 1 is tested in a reactor containing 1 g of the catalyst at temperature 25°C, , gas flow rate 120 000 h "1 and gas composition 0.01% ozone and the balance air.
- the catalyst obtained by the method described in Example 1 is tested in a reactor containing 1 g of the catalyst at temperature 25°C, , gas flow rate 120 000 h "1 and gas composition 0.01% ozone, 0.1% CO and the balance air.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Environmental & Geological Engineering (AREA)
- Health & Medical Sciences (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Combustion & Propulsion (AREA)
- Catalysts (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP98918997A EP0981402A1 (en) | 1997-05-15 | 1998-05-15 | Gold based catalyst for exhaust gas purification |
AU72013/98A AU7201398A (en) | 1997-05-15 | 1998-05-15 | Gold based catalyst for exhaust gas purification |
JP54862498A JP2001524030A (en) | 1997-05-15 | 1998-05-15 | Gold-containing catalyst for exhaust gas purification |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BG101490 | 1997-05-15 | ||
BG101490A BG62687B1 (en) | 1997-05-15 | 1997-05-15 | Gold catalyst for the oxidation of carbon oxide and hydrocarbons, reduction of nitrogen oxides and ozone decomposition |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1998051401A1 true WO1998051401A1 (en) | 1998-11-19 |
Family
ID=3927016
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/BG1998/000010 WO1998051401A1 (en) | 1997-05-15 | 1998-05-15 | Gold based catalyst for exhaust gas purification |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP0981402A1 (en) |
JP (1) | JP2001524030A (en) |
AU (1) | AU7201398A (en) |
BG (1) | BG62687B1 (en) |
WO (1) | WO1998051401A1 (en) |
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1999016546A1 (en) * | 1997-09-29 | 1999-04-08 | Laman Consultancy Limited | Gold catalyst for fuel cells |
WO2000013791A1 (en) * | 1998-09-07 | 2000-03-16 | Anglo American Research Laboratories (Proprietary) Limited | Gold catalyst for fuel cell |
WO2000059631A1 (en) * | 1999-04-01 | 2000-10-12 | Anglo American Research Laboratories (Proprietary) Limited | Selective catalytic oxidation of co in presence of h2 |
US7152609B2 (en) | 2003-06-13 | 2006-12-26 | Philip Morris Usa Inc. | Catalyst to reduce carbon monoxide and nitric oxide from the mainstream smoke of a cigarette |
US7165553B2 (en) | 2003-06-13 | 2007-01-23 | Philip Morris Usa Inc. | Nanoscale catalyst particles/aluminosilicate to reduce carbon monoxide in the mainstream smoke of a cigarette |
US7243658B2 (en) | 2003-06-13 | 2007-07-17 | Philip Morris Usa Inc. | Nanoscale composite catalyst to reduce carbon monoxide in the mainstream smoke of a cigarette |
US7569510B2 (en) * | 2006-02-27 | 2009-08-04 | Philip Morris Usa Inc. | Catalysts to reduce carbon monoxide such as in the mainstream smoke of a cigarette |
US7677254B2 (en) | 2003-10-27 | 2010-03-16 | Philip Morris Usa Inc. | Reduction of carbon monoxide and nitric oxide in smoking articles using iron oxynitride |
US7712471B2 (en) | 2003-10-27 | 2010-05-11 | Philip Morris Usa Inc. | Methods for forming transition metal oxide clusters and smoking articles comprising transition metal oxide clusters |
CZ301720B6 (en) * | 2008-10-17 | 2010-06-02 | Univerzita Karlova V Praze | Metal-CeO2 based catalyst for use particularly in fuel elements and process for preparing thereof |
US7824639B2 (en) * | 2004-03-05 | 2010-11-02 | Umicore Ag & Co. Kg | Exhaust treatment system and catalyst system |
WO2013163536A1 (en) * | 2012-04-26 | 2013-10-31 | Basf Corporation | Base metal catalyst composition and methods of treating exhaust from a motorcycle |
US8765085B2 (en) | 2012-04-26 | 2014-07-01 | Basf Corporation | Base metal catalyst and method of using same |
US9107452B2 (en) | 2003-06-13 | 2015-08-18 | Philip Morris Usa Inc. | Catalyst to reduce carbon monoxide in the mainstream smoke of a cigarette |
US9358527B2 (en) | 2012-07-09 | 2016-06-07 | Toyota Jidosha Kabushiki Kaisha | Exhaust gas purification catalyst and production method thereof |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5821254B2 (en) * | 2011-04-13 | 2015-11-24 | トヨタ自動車株式会社 | Exhaust gas purification catalyst |
JP6107487B2 (en) * | 2013-07-09 | 2017-04-05 | 株式会社豊田中央研究所 | N2O decomposition catalyst and N2O-containing gas decomposition method using the same |
JP6154409B2 (en) * | 2015-01-27 | 2017-06-28 | トヨタ自動車株式会社 | Method for producing heterometallic multinuclear complex containing Ni and Au |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2344323A1 (en) * | 1976-03-18 | 1977-10-14 | Johnson Matthey Co Ltd | CATALYTIC GAS PURIFICATION PROCESS |
JPH02290251A (en) * | 1989-01-24 | 1990-11-30 | Nkk Corp | Gold-containing catalyst for contact combustion |
WO1994019092A1 (en) * | 1993-02-18 | 1994-09-01 | Bojidara Grigorova | Catalyst for use in oxidation |
WO1995019843A1 (en) * | 1994-01-25 | 1995-07-27 | Anglo American Research Laboratories (Proprietary) Limited | Method of making a catalyst |
WO1995035151A1 (en) * | 1994-06-17 | 1995-12-28 | Bojidara Grigorova | Oxidation catalyst |
WO1996014153A1 (en) * | 1994-11-02 | 1996-05-17 | Bojidara Grigorova | Catalyst with zirconia/ceria support |
-
1997
- 1997-05-15 BG BG101490A patent/BG62687B1/en unknown
-
1998
- 1998-05-15 AU AU72013/98A patent/AU7201398A/en not_active Abandoned
- 1998-05-15 EP EP98918997A patent/EP0981402A1/en not_active Withdrawn
- 1998-05-15 JP JP54862498A patent/JP2001524030A/en active Pending
- 1998-05-15 WO PCT/BG1998/000010 patent/WO1998051401A1/en not_active Application Discontinuation
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2344323A1 (en) * | 1976-03-18 | 1977-10-14 | Johnson Matthey Co Ltd | CATALYTIC GAS PURIFICATION PROCESS |
JPH02290251A (en) * | 1989-01-24 | 1990-11-30 | Nkk Corp | Gold-containing catalyst for contact combustion |
WO1994019092A1 (en) * | 1993-02-18 | 1994-09-01 | Bojidara Grigorova | Catalyst for use in oxidation |
WO1995019843A1 (en) * | 1994-01-25 | 1995-07-27 | Anglo American Research Laboratories (Proprietary) Limited | Method of making a catalyst |
WO1995035151A1 (en) * | 1994-06-17 | 1995-12-28 | Bojidara Grigorova | Oxidation catalyst |
WO1996014153A1 (en) * | 1994-11-02 | 1996-05-17 | Bojidara Grigorova | Catalyst with zirconia/ceria support |
Non-Patent Citations (1)
Title |
---|
DATABASE WPI Section Ch Week 9103, Derwent World Patents Index; Class E36, AN 91-018457, XP002079781 * |
Cited By (21)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1999016546A1 (en) * | 1997-09-29 | 1999-04-08 | Laman Consultancy Limited | Gold catalyst for fuel cells |
WO2000013791A1 (en) * | 1998-09-07 | 2000-03-16 | Anglo American Research Laboratories (Proprietary) Limited | Gold catalyst for fuel cell |
GB2357628A (en) * | 1998-09-07 | 2001-06-27 | Anglo American Res Lab | Gold catalyst for fuel cell |
WO2000059631A1 (en) * | 1999-04-01 | 2000-10-12 | Anglo American Research Laboratories (Proprietary) Limited | Selective catalytic oxidation of co in presence of h2 |
AU767170B2 (en) * | 1999-04-01 | 2003-11-06 | Anglo American Research Laboratories (Proprietary) Limited | Selective catalytic oxidation of CO in presence of H2 |
US7152609B2 (en) | 2003-06-13 | 2006-12-26 | Philip Morris Usa Inc. | Catalyst to reduce carbon monoxide and nitric oxide from the mainstream smoke of a cigarette |
US7165553B2 (en) | 2003-06-13 | 2007-01-23 | Philip Morris Usa Inc. | Nanoscale catalyst particles/aluminosilicate to reduce carbon monoxide in the mainstream smoke of a cigarette |
US7243658B2 (en) | 2003-06-13 | 2007-07-17 | Philip Morris Usa Inc. | Nanoscale composite catalyst to reduce carbon monoxide in the mainstream smoke of a cigarette |
US9107452B2 (en) | 2003-06-13 | 2015-08-18 | Philip Morris Usa Inc. | Catalyst to reduce carbon monoxide in the mainstream smoke of a cigarette |
US7712471B2 (en) | 2003-10-27 | 2010-05-11 | Philip Morris Usa Inc. | Methods for forming transition metal oxide clusters and smoking articles comprising transition metal oxide clusters |
US7677254B2 (en) | 2003-10-27 | 2010-03-16 | Philip Morris Usa Inc. | Reduction of carbon monoxide and nitric oxide in smoking articles using iron oxynitride |
US7997281B2 (en) | 2003-10-27 | 2011-08-16 | Philip Morris Usa Inc. | Reduction of carbon monoxide and nitric oxide in smoking articles using nanoscale particles and/or clusters of nitrided transition metal oxides |
US7824639B2 (en) * | 2004-03-05 | 2010-11-02 | Umicore Ag & Co. Kg | Exhaust treatment system and catalyst system |
US7569510B2 (en) * | 2006-02-27 | 2009-08-04 | Philip Morris Usa Inc. | Catalysts to reduce carbon monoxide such as in the mainstream smoke of a cigarette |
CZ301720B6 (en) * | 2008-10-17 | 2010-06-02 | Univerzita Karlova V Praze | Metal-CeO2 based catalyst for use particularly in fuel elements and process for preparing thereof |
WO2013163536A1 (en) * | 2012-04-26 | 2013-10-31 | Basf Corporation | Base metal catalyst composition and methods of treating exhaust from a motorcycle |
US8668890B2 (en) | 2012-04-26 | 2014-03-11 | Basf Corporation | Base metal catalyst composition and methods of treating exhaust from a motorcycle |
US8765085B2 (en) | 2012-04-26 | 2014-07-01 | Basf Corporation | Base metal catalyst and method of using same |
KR20150008887A (en) * | 2012-04-26 | 2015-01-23 | 바스프 코포레이션 | Base metal catalyst composition and methods of treating exhaust from a motorcycle |
KR102222867B1 (en) * | 2012-04-26 | 2021-03-04 | 바스프 코포레이션 | Base metal catalyst composition and methods of treating exhaust from a motorcycle |
US9358527B2 (en) | 2012-07-09 | 2016-06-07 | Toyota Jidosha Kabushiki Kaisha | Exhaust gas purification catalyst and production method thereof |
Also Published As
Publication number | Publication date |
---|---|
BG62687B1 (en) | 2000-05-31 |
AU7201398A (en) | 1998-12-08 |
EP0981402A1 (en) | 2000-03-01 |
BG101490A (en) | 1999-04-30 |
JP2001524030A (en) | 2001-11-27 |
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