US2004234438A1PendingUtilityA1

Ceric oxide and method for production thereof, and catalyst for exhaust gas clarification

Priority: Sep 7, 2001Filed: Sep 5, 2002Published: Nov 25, 2004
Est. expirySep 7, 2021(expired)· nominal 20-yr term from priority
B01D 53/94B01J 20/28057C01P 2006/14B01J 37/031C01P 2006/90B01J 20/0207C01P 2006/13B01J 20/06B01D 2255/206B01D 53/945B01J 23/10Y02A50/20B01J 35/32B01J 35/615B01J 35/633B01J 35/612C01F 17/235B01J 35/30C01F 17/206Y02T10/12B01J 35/613
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Claims

Abstract

The present invention relates to ceric oxide that has excellent heat resistance and oxygen absorbing and desorbing capability useful as a co-catalyst material suitable for a catalyst for purifying exhaust gas, that is capable of maintaining a large specific surface area even in use in a high temperature environment, and that is suitable for use in a high temperature environment, yet capable of exhibiting high oxygen absorbing and desorbing capability also in a lower temperature range, a method for preparing such ceric oxide, and a catalyst for purifying exhaust gas utilizing such ceric oxide. The ceric oxide is an oxide composed essentially of ceric oxide, and has a specific surface area of not smaller than 30.0 m 2 /g after calcination at 900° C. for 5 hours.

Claims

exact text as granted — not AI-modified
What is claimed is:  
     
         1 . A ceric oxide which is an oxide consisting essentially of ceric oxide, and has a specific surface area of not smaller than 30.0 m 2 /g after calcination at 900° C. for 5 hours.  
     
     
         2 . The ceric oxide of  claim 1 , wherein said ceric oxide has an S1/S2 ratio of not lower than 0.120 taken after calcination at 1000° C. for 5 hours, said S1/S2 ratio is a ratio of an area (S 1 ) defined by a baseline and a TPR curve in a temperature range of 200 to 600° C. to an area (S 2 ) defined by said baseline and said TPR curve in a temperature range of 600 to 1000° C.  
     
     
         3 . The ceric oxide of  claim 1 , wherein said ceric oxide has OSC of not smaller than 0.60 mlO 2 /g/s at 400° C., after calcination at 900° C. for 5 hours.  
     
     
         4 . The ceric oxide of  claim 1 , wherein said ceric oxide has a tap density of not higher than 1.3 g/ml, after calcination at 300° C. for 10 hours.  
     
     
         5 . The ceric oxide of  claim 1 , wherein said ceric oxide has a total pore volume of not smaller than 0.50 ml/g, after calcination at 300° C. for 10 hours.  
     
     
         6 . A method for preparing a ceric oxide of  claim 1 , comprising the steps of: 
 (a) providing a cerium solution not less than 90 mol % of which cerium ions are tetravalent;    (b) holding said cerium solution prepared in step (a) at 60 to 220° C. under heating;    (c) cooling said heated cerium solution;    (d) adding a precipitant to said cooled cerium solution to obtain a precipitate; and    (e) calcining said precipitate.    
     
     
         7 . The method of  claim 6 , wherein said cerium solution in step (a) has a cerium concentration of 5 to 150 g/L in terms of cerium oxide, and wherein said calcining in step (e) is carried out at 250 to 900° C.  
     
     
         8 . The method of  claim 6 , further comprising, after step (d) and before step (e), step (d 1 ) of heat-treating said precipitate obtained in step (d) in a solvent at 60 to 220° C. to obtain a precipitate.  
     
     
         9 . A catalyst for purifying exhaust gas comprising a co-catalyst, wherein said co-catalyst comprises ceric oxide of  claim 1.

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