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The present invention relates to an apparatus and method for vaporizing a fluid to improve performance of a selective catalytic reduction catalyst. A vaporizer including a plurality of flow channels having an increased surface area may facilitate vaporization and mixing of the fluid in, e.g., an eng

The present invention relates to an apparatus and method for vaporizing a fluid to improve performance of a selective catalytic reduction catalyst. A vaporizer including a plurality of flow channels having an increased surface area may facilitate vaporization and mixing of the fluid in, e.g., an engine exhaust or gas containing nitrous oxides. The vaporizer may be located in an exhaust system downstream of a fluid injection site and upstream of a selective catalytic reduction catalyst. The exhaust discharged from the selective catalytic reduction catalyst may have a reduced concentration of nitrogen oxides.

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1. An apparatus to assist catalytic reduction of a flow of exhaust gas from an engine comprising: an inlet to provide droplets of a fluid having a first average diameter D1, said fluid comprising a reducing agent and/or a precursor thereof;said apparatus to mix said fluid with a compound to be chemi

1. An apparatus to assist catalytic reduction of a flow of exhaust gas from an engine comprising: an inlet to provide droplets of a fluid having a first average diameter D1, said fluid comprising a reducing agent and/or a precursor thereof;said apparatus to mix said fluid with a compound to be chemically reduced in said flow of exhaust gas and to receive said droplets of said fluid of said first average diameter D1 and to convert said droplets to a second average diameter D2 wherein D2< D1;wherein D1 is greater than or equal to about 100 microns and D2 is less than 100 microns; andwherein said apparatus comprises a plurality of internal flow channels with a surface area of about 250 m2/m3 to convert said droplets to the second average diameter D2, and said apparatus to convert said droplets to said second average diameter D2 without said apparatus heating said fluid and while maintaining a volumetric flow rate of exhaust gas from the engine through the apparatus from the inlet to an outlet of the apparatus; andwherein the plurality of internal flow channels are arranged such that flow of the fluid through each of the channels is parallel to the channel as the fluid passes through the channel which guides the flow from the inlet to the outlet; andwherein the apparatus is provided in the form of two separate units with a first unit located in an inlet exhaust pipe and a second unit located in an inlet cone upstream of a catalyst chamber. 2. The apparatus of claim 1 wherein said apparatus functions in an absence of a catalyst coating. 3. The apparatus of claim 1 wherein said reducing agent precursor is present in said fluid at a level of about 0.01-50% (wt.). 4. The apparatus of claim 1 wherein said reducing agent precursor comprises urea. 5. The apparatus of claim 1 wherein said fluid comprises a hydrocarbon. 6. The apparatus of claim 1 wherein said reducing agent comprises ammonia. 7. The apparatus of claim 1 wherein said apparatus outputs to a catalyst reduction device containing a catalyst capable of reducing nitrogen oxide compounds. 8. The apparatus of claim 7 wherein said catalytic reduction device includes a catalyst comprising a metal selected from the group consisting of vanadium, zeolite, molybdenum, tungsten, and mixtures thereof. 9. An exhaust gas treatment system to treat a flow of exhaust gas from an engine comprising: an apparatus to assist catalytic reduction of engine exhaust wherein said apparatus comprises a plurality of internal flow channels with a surface area of about 250 m2/m3 and is configured to receive engine exhaust including a compound to be chemically reduced and a fluid comprising a reducing agent and/or a precursor thereof, said apparatus to receive droplets of said fluid having a first average diameter D1 and to convert said droplets to a second average diameter D2 wherein D2< D1 and D1 is greater than or equal to about 100 microns and D2 is less than 100 microns and to mix said fluid with said exhaust without said apparatus heating said fluid and while maintaining a volumetric flow rate of exhaust gas from the engine through the apparatus from the inlet to an outlet of the apparatus; andwherein the plurality of internal flow channels are arranged such that flow of the fluid through each of the channels is parallel to the channel as the fluid passes through the channel which guides the flow from an inlet to the outlet; andwherein the apparatus is provided in the form of two separate units with a first unit located in an inlet exhaust pipe and a second unit located in an inlet cone upstream of a catalyst chamber. 10. The system of claim 9 wherein said reducing agent precursor comprises urea. 11. The system of claim 9 wherein said reducing agent comprises ammonia. 12. The system of claim 9, wherein said apparatus outputs to a catalytic reduction device containing a catalyst to reduce nitrogen oxide compounds. 13. The system of claim 12 wherein said catalyst comprises a metal selected from the group consisting of vanadium, zeolite, molybdenum, tungsten and mixtures thereof. 14. A gas treatment process to treat a flow of exhaust gas from an engine comprising: providing a fluid comprising a reducing agent and/or a precursor thereof;forming droplets of the fluid comprising a reducing agent and/or a precursor thereof of a first average diameter D1;receiving said droplets of said fluid by an apparatus to assist catalytic reduction of engine exhaust, wherein said apparatus comprises a plurality of internal flow channels with a surface area of about 250 m2/m3, and wherein the plurality of internal flow channels are arranged such that flow of the fluid through each of the channels is parallel to the channel as the fluid passes through the channel which guides the flow from an inlet to an outlet, and wherein the apparatus is provided in the form of two separate units with a first unit located in an inlet exhaust pipe and a second unit located in an inlet cone upstream of a catalyst chamber;converting said first average diameter D1 into a second average diameter D2 with said apparatus wherein D2< D1, and wherein D1 is greater than or equal to about 100 microns and D2 is less than 100 microns without said apparatus heating said fluid and while maintaining a volumetric flow rate of the flow of exhaust gas from the engine through the apparatus from the inlet to the outlet of the apparatus;mixing a gas containing NOx with said droplets having said second average diameter D2 to form a mixture and exposing said mixture to a reduction catalyst. 15. The gas treatment process of claim 14 wherein said reducing agent precursor comprises urea.