US2016367939A1PendingUtilityA1
Transition metal/zeolite scr catalysts
Est. expiryApr 26, 2027(~0.8 yrs left)· nominal 20-yr term from priority
Inventors:Joseph Michael FedeykoRodney FooPaul Joseph AndersenJillian Elaine CollierJohn Leonello CasciHai-Ying ChenRaj Rao Rajaram
B01J 29/83B01J 29/56B01J 29/7615C01B 39/46C01B 39/54B01J 29/763B01J 29/46B01J 29/005B01D 53/565B01D 53/945C01B 39/38B01D 2255/502B01J 29/87B01D 2255/20761B01J 29/85B01J 29/70B01D 2255/50B01J 29/76B01J 2029/062B01J 2229/183B01D 2255/2065B01J 29/072Y02C20/10B01J 2229/36B01D 2255/2092B01D 2251/2062B01D 53/9418B01J 29/80B01J 29/72B01D 2255/20738B01J 2229/18B01J 29/064B01D 2251/2067B01D 53/8628B01D 53/56B01D 53/9431B01J 29/076B01J 29/061B01J 23/72B01D 2255/30B01D 2255/504B01J 35/56B01J 35/04Y02A50/20Y02T10/12
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Claims
Abstract
A method of converting nitrogen oxides in a gas to nitrogen by contacting the nitrogen oxides with a nitrogenous reducing agent in the presence of a zeolite catalyst containing at least one transition metal, wherein the zeolite is a small pore zeolite containing a maximum ring size of eight tetrahedral atoms, wherein the at least one transition metal is selected from the group consisting of Cr, Mn, Fe, Co, Ce, Ni, Cu, Zn, Ga, Mo, Ru, Rh, Pd, Ag, In, Sn, Re, Ir and Pt.
Claims
exact text as granted — not AI-modified1 . A catalytic article comprising:
a. catalyst for treating exhaust gas comprising a small pore molecular sieve comprising an ERI framework and containing from 0.01 to 20 weight percent Cu based on the total weight of the zeolite, wherein said zeolite comprises a second framework and wherein said molecular sieve is an aluminosilicate, wherein the catalyst is effective to promote the reaction of NH 3 to form nitrogen and water, selectively; and b. a substrate selected from a flow-through substrate or a wall-flow filter, wherein the catalyst is coated on the flow-through substrate or a wall-flow filter or is extruded as part of the flow-through substrate or a wall-flow filter.
2 . The catalytic article of claim 1 , wherein said aluminosilicate is a ZSM-34 isotype.
3 . The catalytic article of claim 2 , wherein said aluminosilicate has an SAR of 2 to 300.
4 . The catalytic article of claim 2 , wherein said aluminosilicate has an SAR of 8 to 150.
5 . The catalytic article of claim 2 , wherein said copper is present in an amount of 0.5 to 5 wt. % based on the total weight of the zeolite.
6 . The catalytic article of claim 5 , wherein said copper is added to the zeolite by one of incipient wetness, ion exchange, and during zeolite synthesis.
7 . The catalytic article of claim 2 , wherein the molecular sieve has an alkali content of about 0.7 to about 1.5 weight percent based on the total weight of the zeolite.
8 . The catalytic article of claim 2 , wherein the molecular sieve has an alkali content of about 1 weight percent based on the total weight of the zeolite.
9 . The catalytic article of claim 2 , wherein the catalyst further comprises a medium, large, or meso-pore zeolite.
10 . The catalytic article of claim 2 , wherein the catalyst further comprises a Cu or Fe promoted zeolite having a chabazite framework.
11 . The catalytic article of claim 2 , wherein the catalyst is coating on the substrate.
12 . The catalytic article of claim 11 , wherein the coating further comprises at least one binder selected from alumina, silica, non-zeolite silica-alumina, natural clay, TiO2, ZrO2, and SnO2.
13 . The catalytic article of claim 11 , wherein the substrate is a flow-through substrate.
14 . The catalytic article of claim 11 , wherein the substrate is a wall-flow filter.
15 . The catalytic article of claim 2 , wherein the substrate is formed from an extrudate comprising the catalyst.Join the waitlist — get patent alerts
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