Complex oxide, method for producing same and exhaust gas purifying catalyst
Disclosed are a silicon-containing cerium composite oxide which is capable of maintaining a large specific surface area even used in a high temperature environment, and which has excellent heat resistance and reducibility, as well as a method for producing the composite oxide and a catalyst for exhaust gas purification employing the composite oxide. The composite oxide contains 2 to 20 mass % silicon in terms of SiO 2 , has properties of exhibiting a specific surface area of not less than 40 m 2 /g as measured by the BET method after calcination at 1000° C. for 5 hours, and a reducibility of not lower than 30% as calculated from measurement of temperature-programmed reduction from 50° C. to 900° C. after calcination at 1000° C. for 5 hours, and is suitable for a co-catalyst for a catalyst for exhaust gas purification.
1. A silicon-containing cerium composite oxide comprising 2 to 20 mass % silicon in terms of SiO 2 , and having properties of exhibiting a specific surface area of not less than 40 m 2 /g as measured by BET method after calcination at 1000° C. for 5 hours, and a reducibility of not lower than 30% as calculated from measurement of temperature-programmed reduction from 50° C. to 900° C. after calcination at 1000° C. for 5 hours.
2. The silicon-containing cerium composite oxide according to claim 1 having a property of exhibiting a specific surface area of not less than 45 m 2 /g as measured by BET method after calcination at 1000° C. for 5 hours.
3. The silicon-containing cerium composite oxide according to claim 1 having a property of exhibiting a specific surface area of not less than 60 m 2 /g as measured by BET method after calcination at 900° C. for 5 hours.
4. The silicon-containing cerium composite oxide according to claim 1 having a property of exhibiting a reducibility of not lower than 35% as calculated from measurement of temperature-programmed reduction from 50° C. to 900° C. after calcination at 1000° C. for 5 hours.
5. The silicon-containing cerium composite oxide according to claim 1 comprising 5 to 20 mass % silicon in terms of SiO 2 .
6. A method for producing a silicon-containing cerium composite oxide according to claim 1 comprising the steps of:
(a) providing a cerium solution not less than 90 mol % of which cerium ions are tetravalent,
(b) heating and maintaining said cerium solution obtained from step (a) up to and at not lower than 60° C.,
(c) adding a precipitant to a cerium suspension obtained through said heating and maintaining to obtain a precipitate,
(d) calcining said precipitate to obtain a cerium oxide,
(e) impregnating said cerium oxide thus obtained through calcination with a solution of a silicon oxide precursor, and
(f) calcining said cerium oxide thus impregnated with said solution of a silicon oxide precursor to obtain the silicon-containing cerium composite oxide.
7. A method for producing a silicon-containing cerium composite oxide according to claim 1 comprising the steps of:
(A) providing a cerium solution not less than 90 mol % of which cerium ions are tetravalent,
(B) heating and maintaining said cerium solution obtained from step (A) up to and at not lower than 60° C.,
(C) adding a silicon oxide precursor to a cerium suspension obtained through said heating and maintaining,
(D) heating and maintaining said cerium suspension containing said silicon oxide precursor up to and at not lower than 100° C.,
(E) adding a precipitant to the cerium suspension containing the silicon oxide precursor obtained through said heating and maintaining to obtain a precipitate, and
(F) calcining the precipitate thus obtained to give the silicon-containing cerium composite oxide.
8. The method according to claim 6 , wherein a cerium content of the cerium solution in step (a) is 5 to 100 g/L in terms of CeO 2 .
9. A catalyst for exhaust gas purification comprising a silicon-containing cerium composite oxide according to claim 1 .
10. The method according to claim 7 , wherein a cerium content of the cerium solution in step (A) is 5 to 100 g/L in terms of CeO 2 .