Claims
- 1. Process which comprises converting a straight-chain C.sub.4 -hydrocarbon in the gaseous phase to maleic anhydride using an activated catalyst, which can be reactivated, for oxidation reactions on the basis of a mixed oxide of vanadium and phosphorus, said vanadium having an average valence of less than +3.9, said catalyst having been activated at a temperature of 300.degree. to 450.degree. C. by passing over the mixed oxide a gaseous hydrocarbon component, which has 2 to 6 carbon atoms, in the absence of molecular oxygen, said catalyst having been calcined before activation, and said catalyst having an atomic ratio of phosphorus to vanadium between 1.05 to 1 and 1.10 to 1.
- 2. Process as claimed in claim 1 wherein said mixed oxide also contains oxides of elements other than vanadium and phosphorus.
- 3. Process as claimed in claim 1 wherein said mixed oxide also contains titanium dioxide.
- 4. Process as claimed in claim 1 wherein said straight-chain C.sub.4 -hydrocarbon is gaseous n-butane.
- 5. Process as claimed in claim 1 wherein said vanadium has an average valence between +3.5 and +3.85.
- 6. Process which comprises converting a straight-chain C.sub.4 -hydrocarbon in the gaseous phase to maleic anhydride using an activated catalyst, which can be reactivated, for oxidation reactions on the basis of a mixed oxide of vanadium and phosphorus, said vanadium having an average valence of less than +3.9, said catalyst having been activated at a temperature of 300.degree. to 450.degree. C. by passing gaseous butane or a mixture of gaseous butane and a non-oxidizing inert gas over the mixed oxide in the absence of molecular oxygen, said catalyst having been calcined before activation, and said catalyst having an atomic ratio of phosphorus to vanadium between 1.05 to 1 and 1.10 to 1.
- 7. Process as claimed in claim 6 wherein said mixed oxide also contains oxides of elements other than vanadium and phosphorus.
- 8. Process as claimed in claim 6 wherein said mixed oxide also contains titanium dioxide.
- 9. Process as claimed in claim 6 wherein said straight-chain C.sub.4 -hydrocarbon is gaseous n-butane.
- 10. Process as claimed in claim 6 wherein said vanadium has an average valence between +3.5 and +3.85.
- 11. Process as claimed in claim 6 wherein said inert gas is CO.sub.2 or N.sub.2.
- 12. Process as claimed in claim 6 wherein said inert gas is N.sub.2 and said mixture contains at least 5 percent of butane.
Priority Claims (1)
Number |
Date |
Country |
Kind |
6466/76 |
May 1976 |
CHX |
|
Parent Case Info
This is a division of application Ser. No. 799,331, filed May 23, 1977.
US Referenced Citations (22)
Foreign Referenced Citations (4)
Number |
Date |
Country |
2256909 |
May 1973 |
DEX |
2328755 |
Jan 1974 |
DEX |
2353136 |
May 1974 |
DEX |
1416099 |
Dec 1975 |
GBX |
Divisions (1)
|
Number |
Date |
Country |
Parent |
799331 |
May 1977 |
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