Methods for producing C2 to C5 paraffins using a hybrid catalyst comprising gallium metal oxide
US-12030036-B2 · Jul 9, 2024 · US
US2016107150A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016107150-A1 |
| Application number | US-201414516632-A |
| Country | US |
| Kind code | A1 |
| Filing date | Oct 17, 2014 |
| Priority date | Oct 17, 2014 |
| Publication date | Apr 21, 2016 |
| Grant date | — |
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An aftertreatment system utilizes chemical reactions to treat an exhaust gas flow. A device for use within an aftertreatment system includes a platinum-free ammonia oxidation catalyst comprising palladium to treat ammonia slip in the exhaust gas flow. In one embodiment, the catalyst includes a Pd/Cu/SAPO-34 catalyst used within a selective catalytic reduction device or in a device downstream of the selective catalytic reduction device.
Opening claim text (preview).
1 . A device for aftertreatment of an exhaust gas flow, the device comprising: a platinum-free ammonia oxidation catalyst comprising palladium. 2 . The device of claim 1 , wherein the device further comprises a selective-catalytic reduction device. 3 . The device of claim 2 , wherein the catalyst comprises a catalyst brick within the selective-catalytic reduction device. 4 . The device of claim 2 , wherein the catalyst is dispersed as a separate layer under a selective catalytic reduction catalyst applied within the device. 5 . The device of claim 2 , wherein the catalyst is dispersed as a separate layer on top a selective catalytic reduction catalyst applied within the device. 6 . The device of claim 2 , wherein the catalyst is dispersed uniformly within a washcoat with selective catalytic reduction catalysts applied within the device 7 . The device of claim 1 , wherein the device further comprises a diesel oxidation catalyst. 8 . The device of claim 7 , wherein the catalyst comprises a catalyst brick within the diesel oxidation catalyst device. 9 . The device of claim 1 , wherein the catalyst is applied as a washcoat upon a flow thorough substrate. 10 . The device of claim 1 , wherein the catalyst is applied as a wall flow substrate. 11 . The device of claim 1 , wherein the catalyst is applied as zone coatings within one of a selective catalytic reduction catalyst and a selective catalytic reduction-on-filter catalysts. 12 . The device of claim 1 , wherein the catalyst further comprises a zeolite selected from the group consisting of Beta, ZSM-5, SSZ-13, Y, SAPO-5, SAPO-11, and SAPO-34. 13 . The device of claim 1 , wherein the catalyst further comprises a Pd/Cu/SAPO-34 catalyst. 14 . The device of claim 1 , wherein the catalyst includes palladium loading values between 2 g/ft 3 and 20 g/ft 3 . 15 . The device of claim 1 , wherein the catalyst includes a palladium loading value of 15 g/ft 3 . 16 . The device of claim 1 , wherein the catalyst further comprises a metal selected from iron, cobalt, nickel, and manganese. 17 . A system for aftertreatment of an exhaust gas flow, the system comprising: at least one device including a platinum-free ammonia oxidation catalyst comprising palladium. 18 . The system of claim 17 , wherein the catalyst is located within a selective catalytic reduction device utilizing ammonia to treat the exhaust gas flow. 19 . The system of claim 18 , further comprising a diesel oxidation catalyst device using a second platinum-free palladium catalyst.
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