US2019299198A1PendingUtilityA1

ZEOLITE PROMOTED V/TiW CATALYSTS

Assignee: JOHNSON MATTHEY PLCPriority: Aug 17, 2012Filed: Apr 5, 2019Published: Oct 3, 2019
Est. expiryAug 17, 2032(~6.1 yrs left)· nominal 20-yr term from priority
B01J 29/69B01J 37/00B01J 37/02B01D 53/9436B01D 2255/20776B01D 53/9468B01J 29/46B01D 53/9477B01J 29/70B01J 23/22B01J 29/68B01J 37/04B01D 2258/012B01J 2229/42B01J 29/88B01J 29/7615B01D 2255/915B01J 29/076B01J 37/0246B01D 2255/20738B01D 2251/2062B01J 37/0009B01J 29/65B01J 29/76B01J 29/40B01D 2255/20723B01D 2255/50B01J 29/48B01J 2229/186B01J 29/7007B01J 29/7815B01D 2255/20707B01D 2255/502B01J 23/30B01J 23/8472B01D 2255/102B01D 2255/9155B01D 2255/504B01D 53/9418B01J 23/847B01J 23/40B01D 53/86B01J 35/0006B01J 35/04Y02T10/24B01J 29/00B01J 2235/15B01J 35/56B01J 29/67B01J 21/06B01D 53/94Y02T10/12B01J 35/19
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Claims

Abstract

Provided is a catalyst composition for treating exhaust gas comprising a blend of a first component and second component, wherein the first component is an aluminosilicate or ferrosilicate molecular sieve component wherein the molecular sieve is either in H+ form or is ion exchanged with one or more transition metals, and the second component is a vanadium oxide supported on a metal oxide support selected from alumina, titania, zirconia, ceria, silica, and combinations thereof. Also provided are methods, systems, and catalytic articles incorporating or utilizing such catalyst blends.

Claims

exact text as granted — not AI-modified
1 . A catalyst composition for treating exhaust gas comprising a blend of a first component and second component, wherein the first component is an aluminosilicate or ferrosilicate molecular sieve component wherein the molecular sieve is in H+ form, and the second component is a vanadium oxide supported on a metal oxide support selected from alumina, titania, zirconia, ceria, silica, and combinations thereof. 
     
     
         2 . The catalyst of  claim 1 , wherein the molecular sieve has a framework selected from MFI, BEA, and FER. 
     
     
         3 . The catalyst of  claim 2 , wherein the molecular sieve is H+/MFI aluminosilicate. 
     
     
         4 . The catalyst of  claim 1 , wherein the molecular sieve is a BEA ferrosilicate. 
     
     
         5 . The catalyst of  claim 1 , wherein the metal oxide support is titanium oxide. 
     
     
         6 . The catalyst composition of  claim 1 , wherein the second component further comprises tungsten oxide. 
     
     
         7 . The catalyst composition of  claim 1 , wherein the second component further comprises iron vanadate. 
     
     
         8 . The catalyst composition of  claim 1 , wherein the first component and second component are present in the blend in a respective weight ratio of about 5:95 to about 40:60. 
     
     
         9 . The catalyst composition of  claim 1 , wherein the blend comprises about 0.5 to about 5 weight percent the vanadium oxide based on the weight of the first and second components. 
     
     
         10 . A catalytic washcoat comprising a catalyst according to  claim 1 , further comprising one or more fillers, binders, processing aides, water, and dopants. 
     
     
         11 . A catalytic article comprising a substrate coated with or incorporating a catalyst according to  claim 1 , wherein the substrate is selected from a metal flow-through substrate, a ceramic flow-through substrate, a wall-flow filter, a sintered metal filter, a partial filter, and an extruded catalyst honeycomb. 
     
     
         12 . The catalytic article of  claim 11 , further comprising a washcoat having a second catalyst composition for selectively reducing NO x  and/or for oxidizing NH 3 . 
     
     
         13 . The catalytic article of  claim 12 , wherein said second catalyst composition is selected from (a) catalyst blends according to  claim 1 , (b) a transition metal promoted molecular sieve, (c) a platinum group metal catalyst, or (d) a vanadium-based catalyst. 
     
     
         14 . The catalyst article of  claim 11 , wherein the substrate comprises a first layer containing a platinum group metal for oxidizing ammonia and a second layer comprising the catalyst of  claim 1 , wherein the first layer is disposed directly on or within the substrate and the second layer covers the first layer. 
     
     
         15 . A system for treating exhaust gas comprising a selective catalytic reduction (SCR) catalyst upstream of an ammonia slip catalyst (ASC), wherein in at least one of said SCR and ASC catalysts comprise a catalyst according to  claim 1 . 
     
     
         16 . The system of  claim 14 , further comprising a diesel oxidation catalyst having a platinum group metal disposed upstream of said selective catalytic reduction catalyst. 
     
     
         17 . A method for treating an exhaust gas comprising the steps of:
 a. contacting an exhaust gas stream containing NO x  and/or NH 3  in the presence of a catalyst according to  claim 1 ; and   b. converting at least a portion of said NO x  to N 2  and/or converting at least a portion of NH 3  to at least one of N 2  and NO 2 .   
     
     
         18 . The method of  claim 17 , wherein said exhaust gas comprises a ratio of NO to NO 2  from about 4:1 to about 1:3 by volume.

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