Method and system for the removal of noxious compounds from engine exhaust gas

Abstract

Method and system for the removal of nitrogen oxides, volatile organic compounds and particulate matter from engine exhaust gas at cold start conditions.

Claims

1. A method for the removal of nitrogen oxides, volatile organic compounds and particulate matter from engine exhaust gas, comprising the steps of passing the engine exhaust gas in series through an exhaust gas channel oxidation catalyst, through a particle filter and a catalyst for selective reduction of nitrogen oxides in presence of ammonia added to the engine exhaust gas either as such or in form of a precursor thereof; at an engine exhaust gas temperature of below 250° C. injecting an effluent gas containing nitrogen dioxide into the engine exhaust gas upstream the catalyst for selective reduction of nitrogen oxides; providing the effluent gas containing nitrogen dioxide by steps of catalytically oxidizing ammonia or a precursor thereof with an oxygen containing atmosphere to an effluent gas comprising nitrogen monoxide and oxygen in presence of an ammonia oxidation catalyst; cooling the effluent gas to ambient temperature and oxidizing the nitrogen monoxide in the cooled effluent gas to nitrogen dioxide.

2. The method of claim 1, wherein the oxygen containing atmosphere comprises engine exhaust gas.

3. The method of claim 1, wherein the oxygen atmosphere is ambient air.

4. The method according to claim 1, wherein effluent gas containing nitrogen dioxide is injected upstream of the particle filter.

5. The method according to claim 1, wherein the effluent gas containing nitrogen dioxide is injected into the engine exhaust gas in an amount resulting in 45 to 55% by volume of the nitrogen oxides is nitrogen dioxide at inlet to the catalyst for selective reduction of nitrogen oxides.

6. The method according to claim 1, wherein the oxidation of the nitrogen monoxide in the cooled effluent gas to nitrogen dioxide is performed in presence of an NO to NO2 oxidation catalyst.

7. The method according to claim 1, wherein the particle filter is catalysed with a catalyst active in burning off soot.

8. A system comprising, within an engine exhaust gas channel in series, an engine exhaust gas channel oxidation catalyst unit for the oxidation of volatile organic compounds and carbon monoxide to carbon dioxide and water and nitrogen oxide to nitrogen dioxide; a particle filter; a catalyst for selective reduction of nitrogen oxides; a first injector that is positioned upstream of the catalyst for selective reduction of nitrogen oxides and injects ammonia or a urea solution into the engine exhaust gas channel; a second injector that is also positioned upstream of the catalyst for selective reduction of nitrogen oxides and that injects into the engine exhaust gas channel nitrogen dioxide containing effluent gas; and arranged outside the exhaust gas channel, an ammonia oxidation catalyst; and means for cooling and oxidizing nitrogen monoxide containing effluent gas from the ammonia oxidation catalyst and which is connected at an outlet end to the second injector.

9. The system of claim 8, wherein the second injector is arranged upstream of the particle filter.

10. The system of claim 8, wherein the means for the cooling and oxidizing nitrogen monoxide containing effluent gas is in form of a spirally wound tube.

11. The system of claim 8, wherein the means for the cooling and oxidizing nitrogen monoxide containing effluent gas is provided with an NO to NO2 oxidation catalyst.

12. The system of claim 8, wherein the particle filter is catalysed with catalyst active in burning off soot.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) FIG. 1 shows a schematic view of a conventional SCR reactor model.

(2) FIG. 2 shows, schematically, an example of a method/system in accordance with the present invention.

(3) FIG. 3 shows, schematically, an example of method/system for NO2 generation.

(4) Thus, the invention provides in a first aspect a method for the removal of nitrogen oxides, volatile organic compounds and particulate matter from engine exhaust gas comprising the steps of

(5) passing the engine exhaust gas in series through an oxidation catalyst, through a particle filter and a catalyst for selective reduction of nitrogen oxides in presence of ammonia added to the engine exhaust gas either as such or in form of a precursor thereof;

(6) at an engine exhaust gas temperature of below 250° C. injecting an effluent gas containing nitrogen dioxide into the engine exhaust gas upstream the catalyst for selective reduction of nitrogen oxides;

(7) providing the effluent gas containing nitrogen dioxide by steps of

(8) catalytically oxidizing ammonia with an oxygen containing atmosphere to an effluent gas comprising nitrogen monoxide and oxygen in presence of an oxidation catalyst;

(9) cooling the effluent gas to ambient temperature and oxidizing the nitrogen monoxide in the cooled effluent gas to nitrogen dioxide.

(10) Cleaning methods and systems for use in the cleaning of engine exhaust gas from a compression ignition engine comprising passing the engine exhaust gas in series through an oxidation catalyst (DOC), through a particle filter (PDF) and a catalyst for selective catalytic reduction of nitrogen oxides (SCR) in presence of ammonia added to the engine exhaust gas either as such or in form of urea precursor are per se known in the art.

(11) The problem with the known methods and systems is the relatively low efficiency of the SCR catalyst at cold start conditions below exhaust gas temperatures at 250° C., as mentioned hereinbefore. This problem is solved by the invention with injection of NO.sub.2 into the engine exhaust gas during cold start temperatures to promote the “fast” SCR reaction. This reaction is responsible for the promotion of low temperature SCR by NO.sub.2.

(12) Above 250° C. NO contained in the engine exhaust gas, when leaving the engine is oxidised to NO.sub.2 by contact with the DOC. Thus, above temperatures of 250° C. all the amount of formed NO.sub.2 can be used for passive soot regeneration of the filter and the fast SCR reaction.

(13) Consequently, injection of NO.sub.2 into the engine exhaust gas can be disrupted when the gas temperature reaches 250° C.

(14) Ammonia oxidation to NO, is usually performed in a reactor with a noble metal catalyst, typically platinum or an alloy of platinum with other precious metals as minor components at reaction temperatures of between 250 and 800° C. in presence of oxygen containing atmosphere, like air.

(15) To provide the required reaction temperature, the oxidation reactor can be heated by e.g. electrical heating or induction heating.

(16) In an embodiment, the oxygen containing atmosphere includes hot recirculated engine exhaust gas which provides than additionally part of the oxidation reactor heating duty.

(17) NO formed from NH.sub.3 by oxidation of the NH.sub.3 in contact with a precious metal containing catalyst in a first step, is subsequently oxidized to NO.sub.2 in the NO containing effluent gas from the first step by cooling the gas to ambient temperature to push the equilibrium reaction 2NO+O.sub.2⇄2NO.sub.2 towards formation of NO.sub.2 in the above reaction scheme.

(18) The term “ambient temperature” as used herein, shall mean any temperature prevailing in the surroundings of a vehicle or stationary engine employing the method and system of the invention. Typically, the ambient temperature will be between −20° C. and 40° C.

(19) Cooling and oxidation of the NO containing effluent gas can be performed in an aging reactor sized so that the residence time of the gas is about 1 minute or longer.

(20) In an embodiment the oxidation reaction is performed in presence of a catalyst promoting the oxidation of NO to NO.sub.2. Those catalysts are known in the art and include Pt on TiO.sub.2, Pt on SiO.sub.2 and activated carbon.

(21) As mentioned hereinbefore the desired fast SCR reaction requires equal amounts of NO and NO.sub.2. Consequently, the amount of NO.sub.2 injected into the engine exhaust gas at cold start conditions with a temperature below 250° C. is controlled to result in 45 to 55% by volume of the nitrogen oxides content in the engine exhaust gas is NO.sub.2 at inlet to the SCR catalyst unit.

(22) NO.sub.2 can be used to oxidize soot particles captured on the DPF and is useful in the passive regeneration of the DPF.

(23) Thus, in an embodiment of the invention, effluent gas containing nitrogen dioxide is injected upstream the particle filter.

(24) In order to facilitate a reliable DPF regeneration by combustion of accumulated soot and simultaneously remove hydrocarbons and carbon monoxide, the DPF is preferably provided with a catalytic coating.

(25) Catalysts active in soot combustion are per se known in the art. An example of such a catalyst is palladium combined with CeO.sub.2 stabilized with ZrO.sub.2 or platinum on alumina.

(26) Above 250° C. the NO in the exhaust gas is oxidised to NO.sub.2 by contact with the DOC. The formed NO.sub.2 is used in the passive regeneration of the DPF. Thus, above temperatures of 250° C. all the amount of formed NO.sub.2 can be used for passive soot regeneration of the filter and to promote the fast SCR and injection of NO.sub.2 containing gas is disrupted.

(27) In a further aspect, the invention provides a system for use in the method according to the invention.

(28) The system comprises within an engine exhaust gas channel in series,

(29) an oxidation catalyst unit for the oxidation of volatile organic compounds and carbon monoxide to carbon dioxide and water and nitrogen oxide to nitrogen dioxide;

(30) a particle filter;

(31) a catalyst for selective reduction of nitrogen oxides;

(32) upstream the catalyst for selective reduction of nitrogen oxides, injection means for injection of ammonia or a urea solution into the engine exhaust gas channel;

(33) upstream the catalyst for selective reduction of nitrogen oxides, injection means for injection of nitrogen dioxide containing effluent gas; and

(34) outside the exhaust gas channel,

(35) an ammonia oxidation catalyst; and

(36) means for cooling and oxidizing nitrogen monoxide containing effluent gas from the ammonia oxidation catalyst connected at its outlet end to the injection means for injection of nitrogen dioxide containing effluent gas.

(37) In an embodiment of the invention, the injection means for injection of nitrogen dioxide containing effluent gas is arranged upstream the particle filter. With this embodiment passive regeneration of the particle filter is possible at lower temperatures, before the engine exhaust gas reaches a temperature at which the upstream oxidation catalyst generates sufficient amounts of NO.sub.2.

(38) As mentioned above, the oxidation reaction of NO to NO.sub.2 needs a residence time of the NO containing gas of about 1 minute. Typically, 1-2 minutes.

(39) This can be achieved, preferably when shaping the cooling and oxidizing means as a spirally wound tube with a length resulting in the desired residence time of the gas passing through the tube.

(40) In another embodiment, the means for cooling and oxidizing nitrogen monoxide containing effluent gas is provided with an oxidation catalyst promoting the oxidation of NO to NO2.

(41) In further an embodiment, the particle filter is catalysed with catalyst active in burning off soot. Listing of Reference Nos. 1: Exhaust gas flow direction 2: Oxidation catalyst 3. Particle filter 4. SCR catalyst 5. NH.sub.3 injection 6. NO.sub.2 injection 7. NH.sub.3+oxygen containing atmosphere 8. AMOX 9. Means for cooling an oxidizing the NO to NO.sub.2 10. Catalysed Particle Filter (CPF)