REDUCTION OF NITROGEN OXIDE

Abstract: The invention provides a method of reducing nitrogen oxide which includes the steps of contacting the nitrogen oxide with a catalyst which comprises an oxide support having captured thereon gold and a transition metal, the gold being complexed with the transition metal. The catalyst is preferably a catalyst as described in either WO 94/19092 or WO 96/14153.

Description: REDUCTION OF NITROGEN OXIDE BACKGROUND OF THE INVENTION This invention relates to the reduction of nitrogen oxide and to the use of a catalyst for the reduction of nitrogen oxide and the oxidation of carbon monoxide and hydrocarbons. The reduction of pollution from industrial processes and the protection of the environment is one of the major issues facing the world today. The internal combustion engine contributes significantly to the pollution levels in the atmosphere. Many countries of the world now have laws directed at reducing the emission of noxious gases from internal combustion engines. A reduction in the emission of noxious gases from internal combustion engines may be achieved by the use of suitable catalysts. By way of example, some of the noxious exhaust gases of an internal combustion engine are carbon monoxide and hydrocarbons. Platinum or palladium may be used to catalyse oxidation of these gases. Rhodium may be used for reduction of the toxic nitrogen oxides. Gold-containing catalysts consisting of gold supported on an oxide such as cobalt oxide, iron oxide, manganese oxide or the like are also known to have utility in the oxidation of carbon monoxide and hydrocarbons. EP-A-602 602 describes a catalyst for the catalytic reduction of nitrogen oxide using hydrocarbon as a reducing agent. The catalyst comprises at least one element of the platinum group and gold. The catalyst may also comprise a metallic oxide selected from the group of cerium oxide, lanthanum oxide, neodymium oxide, germanium oxide and gallium oxide. The carrier for the catalyst may be alumina, silica, silica-alumina, titania, zirconia and H-type zeolite. The gold and platinum group element are captured on the carrier by ion exchange. SUMMARY OF THE INVENTION According to a first aspect of the invention, a method of reducing a nitrogen oxide includes the steps of contacting the nitrogen oxide with a catalyst which comprises an oxide support having captured thereon gold and a transition metal, the gold being complexed with the transition metal. The nitrogen oxide will have the formula NO x . Examples of such oxides are nitrous oxide, nitric oxide, nitrogen trioxide, dinitrogen tetroxide, nitrogen dioxide, dinitrogen pentoxide and trinitrogen tetroxide and mixtures containing two or more such oxides. The reduction of the nitrogen oxide will generally be to nitrogen and oxygen. The invention has particular application to the purification of noxious gases from the exhaust gases of internal combustion engines. Such noxious gases include nitrogen oxides, hydrocarbons and carbon monoxide. The catalysts may be used to reduce the nitrogen oxides producing oxygen which will enhance the ability of the same catalyst to oxidise the hydrocarbons and carbon monoxide. According to a second aspect of the invention, there is provided the use of a catalyst comprising an oxide support having captured thereon gold and a transition metal, the gold being complexed with the transition metal, in a method for the reduction of a nitrogen oxide and the oxidation of carbon monoxide and hydrocarbons. DESCRIPTION OF EMBODIMENTS The oxide support in the catalyst used in the method of the invention will generally be a porous support and may be selected from aluminium oxide, zirconium oxide, cerium oxide, titanium oxide, silicon oxide and mixtures thereof. Generally, the oxide will be present in the catalyst in an amount of at least 50 percent by mass of the catalyst and preferably at least 60 percent by mass of the catalyst. The preferred oxide support is a mixture of zirconium oxide and cerium oxide. With such a mixture, the cerium oxide will typically constitute at least 50 percent by mass of the mixture. The oxide support will preferably have a large surface area, typically 60 to 200m 2 /g. The support may take the form of a monolith, extrudate, pellets, rings or pearls, but is preferably a powder. In the catalyst which is used in the method of the invention, the gold is complexed with the transition metal. This transition metal, which is preferably cobalt, iron or manganese, is preferably captured on the support as an oxide which has a spinel structure. Complexing thus takes place between the gold and the oxide having the spinel structure. The gold is not in metallic form. The concentration of gold on the oxide support will be low and generally less than 2 percent by mass of the catalyst. The atomic ratio of gold to transition metal will typically be in the range 1 :5 to 1 :200. The catalyst may contain a dopant capable of improving the thermal stability thereof. Suitable dopants are alkaline earth metal oxides, and oxides of metals of the lanthanide series. Particularly suitable catalysts for use in the method of the invention are those disclosed in WO 94/19092 and WO 96/14153. The disclosure of both of these publications is incorporated herein by reference. The catalyst disclosed in WO 94/19092 comprises a porous alumina support having captured thereon a complex comprising gold, a transition metal selected from cobalt and manganese, and the alumina, the concentration of gold on the support being less than 2 percent by mass of the catalyst and the atomic ratio of gold to transition metal being in the range 1 :30 to 1 :200. The gold concentration of this catalyst is typically in the range 0,1 to 0,5 percent by mass of the catalyst. The transition metal is generally in the form of an oxide and the gold is complexed therewith. The catalyst disclosed in WO 96/14153 is one which utilises zirconium oxide, cerium oxide or a mixture thereof as the oxide support. Preferably the oxide support is a mixture of zirconium oxide and cerium oxide with cerium oxide typically constituting at least 50 percent by mass of the mixture. In the catalyst of WO 96/14153, the transition metal is generally in oxide form, the oxide having a spinel structure. Complexing takes place between the gold and the transition metal oxide. The catalysts described above are preferably made by a method which involves impregnating the oxide support with a solution of the transition metal, optionally drying the product, exposing the impregnated product to a reducing atmosphere such as hydrogen or carbon monoxide at a temperature exceeding 300°C, contacting the thus treated product with a solution of the noble metal and drying the impregnated product. The catalyst may be activated by exposing it to a temperature of at least 300°C, typically 300 to 500°C, in the presence of oxygen. The oxygen may be air or oxygen mixed with another gas. The catalysts described above have been found to be particularly suitable in the reduction of nitrogen oxide alone or mixed with carbon monoxide and/or a hydrocarbon. Thus, the catalysts are particularly useful in catalysing the reduction of a nitrogen oxide and the oxidation of carbon monoxide and hydrocarbons in the exhaust gas of an internal combustion engine. Catalysts of the type disclosed in WO 94/19092 (Au/Co 3 O 4 /Al 2 O 3 ) and WO 96/14153 (Au/Co 3 O 4 /ZrO 2 CeO 2 TiO 2 ) were compared with a commercially available platinum group metal (PGM) auto-catalyst in the oxidation of carbon monoxide and hydrocarbons and the reduction of nitrogen oxide. The tests were carried out in conditions simulating the exhaust gas of an internal combustion engine, to evaluate the suitability of the catalyst for conversion of exhaust gases from a combustion engine. The results obtained are set out in Tables I and II. Table III sets out the data obtained in tests carried out at a gas flow simulating conditions of exhaust gases from a combustion engine, using catalysts identified as PI to P4. All these catalysts use a mixture of zirconium oxide and cerium oxide as the support and have gold and cobalt oxide captured thereon. The cobalt oxide had a spinel structure and the gold was complexed therewith. The catalysts PI and P2 had no stabilisers, whilst the catalyst P3 had lanthanum oxide as a stabiliser and P4 had barium oxide as a stabiliser. The tests were carried out in the presence and absence of sulphur dioxide. It will be noted from the data set out in Tables I to III that the catalysts were effective in reducing nitrogen oxide and oxidising carbon monoxide and hydrocarbons. TABLE I Test conditions: 60 000 space velocity Gas composition: 1% CO, 0,9% 0 2 700 ppm mixture of paraffins and olefms, 1500 ppm NO balance N, The test was repeated in the presence of sulphur species to evaluate the tolerance of the catalysts towards sulphur poisoning. Results from this test are given in Table II. -J TABLE II 0 - Test conditions: 60 000 space velocity Gas composition: 1% CO, 0,9% 0 2 700 ppm mixture of paraffins and olefms, 1500 ppm NO x 15 ppm S0 2 balance N, TABLE III 100,000 Space Velocity

Claims: CLAIMS 1. A method of reducing nitrogen oxide which includes the step of contacting the nitrogen oxide with a catalyst which comprises an oxide support having captured thereon gold and a transition metal, the gold being complexed with the transition metal. 2. A method according to claim 1 wherein the oxide support is a porous support. 3. A method according to claim 1 or claim 2 wherein the transition metal is captured on the support as an oxide which has a spinel structure. 4. A method according to claim 3 wherein the transition metal is selected from cobalt, iron and manganese. 5. A method according to any one of the preceding claims wherein the concentration of gold on the support is less than 2 percent by mass of the catalyst. 6. A method according to any one of the preceding claims wherein the atomic ratio of gold to transition metal is in the range 1 :5 to 1 :200. 7. A method according to any one of the preceding claims wherein the oxide support is selected from alumimum oxide, zirconium oxide, cerium oxide, titanium oxide, silicon oxide and mixtures thereof. 8. A method according to any one of the preceding claims wherein the oxide support is present in the catalyst in an amount of at least 60 percent by mass of the catalyst. 9. A method according to any one of the preceding claims wherein the oxide support is a mixture of zirconium oxide and cerium oxide. 10. A method according to claim 9 wherein the cerium oxide constitutes at least 50 percent by mass of the mixture. 11. A method according to any one of the preceding claims wherein the catalyst also contains a dopant capable of improving the thermal stability thereof. 12. A method according to claim 1 1 wherein the dopant is selected from alkaline earth metal oxides, and oxides of metals of the lanthanide series. 13. A method according to any one of the preceding claims wherein the nitrogen oxide is nitrous oxide, nitric oxide, nitrogen trioxide, dinitrogen tetroxide, nitrogen dioxide, dinitrogen pentoxide, trinitrogen tetroxide or a mixture containing two or more of such oxides. 14. A method according to any one of the preceding claims wherein the nitrogen oxide is mixed with a hydrocarbon and/or carbon monoxide. 15. A method according to any one of the preceding claims wherein the nitrogen oxide is present in the exhaust gas of an internal combustion engine. 16. Use of a catalyst comprising an oxide support having captured thereon gold and a transition metal, the gold being complexed with the transition metal, in a method for the reduction of nitrogen oxide and the oxidation of carbon monoxide and a hydrocarbon. 17. Use according to claim 16 in a method wherein the nitrogen oxide is mixed with the carbon monoxide and the hydrocarbon. 18. Use according to claim 17 wherein the nitrogen oxide is nitrous oxide, nitric oxide, nitrogen trioxide, dinitrogen tetroxide, nitrogen dioxide, dinitrogen pentoxide, trinitrogen tetroxide or a mixture containing two or more of such oxides. 19. Use according to claim 18 wherein the nitrogen oxide is present in the exhaust gas of an internal combustion engine.

Inventors: GAFIN ANTHONY HAROLD, TUMILTY JAMES ANTHONY JUDE, GAFIN, ANTHONY, HAROLD, TUMILTY, JAMES, ANTHONY, JUDE
Applicants: ANGLO AMERICAN RES LAB PTY LTD, TUMILTY JAMES ANTHONY JUDE, ANGLO AMERICAN RESEARCH LABORATORIES (PROPRIETARY) LIMITED, TUMILTY, JAMES, ANTHONY, JUDE
Application year: 1997
Main classification: B01D53
IPC codes: B01D53, B01J23, F01N3