US2018297016A1PendingUtilityA1

Catalyst blends

Assignee: JOHNSON MATTHEY PLCPriority: Jan 31, 2012Filed: Jun 18, 2018Published: Oct 18, 2018
Est. expiryJan 31, 2032(~5.5 yrs left)· nominal 20-yr term from priority
B01D 2255/91B01D 2251/2062B01J 29/763Y02T10/24B01D 53/9418F01N 3/035B01D 2257/404B01J 29/005F01N 3/0814B01D 2255/1021B01J 29/85B01D 2255/20761B01D 2255/20738B01J 23/44B01D 2255/2092B01J 23/42F01N 2610/02B01J 35/04F01N 3/2066B01J 29/7015F01N 3/0842B01J 35/0006B01D 2255/30F01N 3/2842B01D 2255/50B01D 2255/1023B01D 2255/9155B01J 35/56B01D 53/8628Y02T10/12B01J 29/76B01J 29/00B01D 53/94B01J 35/19
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Claims

Abstract

Provided is a catalyst for the selective reduction of NOx comprising a two molecular sieve materials having a CHA structure, wherein the first molecular sieve has a mean crystal size of about 0.01 to 1 μm and the second molecular sieve has a mean crystal size of about 1-5 μm, and wherein the first molecular sieve contains a first extra-framework metal, the second molecular sieve contains a second extra-framework metal, and wherein said first and second extra-framework metals are independently selected from the group consisting of cesium, copper, nickel, zinc, iron, tin, tungsten, molybdenum, cobalt, bismuth, titanium, zirconium, antimony, manganese, chromium, vanadium, niobium, and combinations thereof.

Claims

exact text as granted — not AI-modified
What is claimed is: 
     
         1 . A catalyst composition comprising a blend of two molecular sieve materials each having a CHA structure, wherein the first molecular sieve has a first silica-to-alumina ratio (SAR) of about 10-25 and contains a first extra-framework metal, the second molecular sieve has second SAR of about 20-35 and contains a second extra-framework metal, and wherein said first and second SAR are different and said first and second extra-framework metals are independently selected from the group consisting of cesium, copper, nickel, zinc, iron, tin, tungsten, molybdenum, cobalt, bismuth, titanium, zirconium, antimony, manganese, chromium, vanadium, niobium, and combinations thereof,
 and wherein at least one of the first and second extra-framework metals comprises manganese.   
     
     
         2 . The catalyst of  claim 1 , wherein the two molecular sieve materials are aluminosilicates. 
     
     
         3 . The catalyst of  claim 1 , wherein said first and second extra-framework metals are independently selected from the group consisting of copper, iron, and manganese, and wherein at least one of the first and second extra-framework metals comprises manganese. 
     
     
         4 . The catalyst of  claim 1 , wherein at least one of the first molecular sieve and the second molecular sieve is an extrudate. 
     
     
         5 . The catalyst of  claim 1 , wherein the first extra-framework metal is present in an amount of about 1 to about 5 wt % based on the total weight of the molecular sieve, and the second extra-framework metal is present in amount sufficient to achieve a weight ratio of the first extra-framework metal and the second extra-framework metal of about 0.4:1.0 to about 1.5:1.0. 
     
     
         6 . The catalyst of  claim 1 , wherein the first molecular sieve and the second molecular sieve are present in a mole ratio of about 0.5:1:0 to about 1.5:1.0. 
     
     
         7 . The catalyst of  claim 1 , wherein the catalyst composition is washcoated on a wall-flow filter. 
     
     
         8 . The catalyst of  claim 7 , wherein the filter contains inlet and outlet channels and the washcoat is on outlet channels. 
     
     
         9 . The catalyst of  claim 1 , wherein the catalyst composition is washcoated on a flow-through honeycomb monolith. 
     
     
         10 . The catalyst of  claim 9 , wherein the flow-through honeycomb monolith further comprises an oxidative underlayer. 
     
     
         11 . The catalyst of  claim 10 , wherein said underlayer comprises a platinum group metal. 
     
     
         12 . The catalyst of  claim 7 , further comprising an ammonia oxidation catalyst disposed downstream of the wall-flow filter. 
     
     
         13 . The catalyst of  claim 9 , further comprising an ammonia oxidation catalyst disposed downstream of the flow-through honeycomb monolith. 
     
     
         14 . The catalyst of  claim 7 , further comprising a NO x  adsorber catalyst (NAC), a lean NO x  trap (LNT), or a NO x  storage/reduction catalyst (NSRC) located upstream of the wall-flow filter. 
     
     
         15 . The catalyst of  claim 7 , further comprising an oxidation zone comprising a platinum group metal. 
     
     
         16 . The catalyst of  claim 15 , wherein the platinum group metal comprises Pd and/or Pt. 
     
     
         17 . A catalyst composition comprising a blend of two molecular sieve materials having a CHA structure, wherein the first molecular sieve has a mean crystal size of about 0.01 to 1 μm and the second molecular sieve has a mean crystal size of about 1-5 μm, and wherein the first molecular sieve contains a first extra-framework metal, the second molecular sieve contains a second extra-framework metal, and wherein said first and second extra-framework metals are independently selected from the group consisting of cesium, copper, nickel, zinc, iron, tin, tungsten, molybdenum, cobalt, bismuth, titanium, zirconium, antimony, manganese, chromium, vanadium, niobium, and combinations thereof, and wherein at least one of the first and second extra-framework metals comprises manganese. 
     
     
         18 . The catalyst of  claim 17 , wherein said first and second extra-framework metals are independently selected from the group consisting of copper, iron, and manganese, and wherein at least one of the first and second extra-framework metals comprises manganese. 
     
     
         19 . A catalyst composition comprising a blend of an aluminosilicate molecular sieve having a CHA framework and a silicoaluminophosphate molecular sieve having a CHA framework, wherein
 a. the aluminosilicate molecular sieve and the silicoaluminophosphate molecular sieve are present an aluminosilicate:silicoaluminophosphate mole ratio of about 0.8:1.0 to about 1.2:1.0; and   b. said aluminosilicate molecular sieve contains a first extra-framework metal, said silicoaluminophosphate molecular sieve contains a second extra-framework metal, wherein said first and second extra-framework metals are independently selected from the group consisting of cesium, copper, nickel, zinc, iron, tin, tungsten, molybdenum, cobalt, bismuth, titanium, zirconium, antimony, manganese, chromium, vanadium, niobium, and combinations thereof, wherein said first extra-framework metal is present in about 2 to about 4 weight percent, based on the weight of the aluminosilicate, and wherein the weight ratio of said first extra-framework metal and said second extra-framework metal is about 0.4:1.0 to about 1.5:1.0,   and wherein at least one of the first and second extra-framework metals comprises manganese.   
     
     
         20 . The catalyst of  claim 19 , wherein said first and second extra-framework metals are independently selected from the group consisting of copper, iron, and manganese, and wherein at least one of the first and second extra-framework metals comprises manganese.

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