Claims
- 1. In an improved method for converting methane to higher hydrocarbon products which comprises contacting a gas comprising methane at synthesizing conditions with a solid comprising at least one reducible oxide of at least one metal which oxides when contacted with methane at synthesizing conditions are, reduced and produce higher hydrocarbon products and water, the improvement which comprises conducting the contacting in the presence of a promoting amount of at least one member of the group consisting of boron and compounds thereof.
- 2. The method of claim 1 which the atomic ratio of the reducible metal oxide component (expressed as the metal) to the boron component (expressed as B) is within the range of about 0.1:1 to about 20:1.
- 3. The method of claim 1 wherein the atomic ratio of the reducible metal oxide component (expressed as the metal) to the boron component (expressed as B) is within the range of about 0.5:1 to about 5:1.
- 4. The method of claim 1 wherein the solid comprises reducible metal oxides selected from the group consisting of reducible oxides of Mn, Sn, In, Ge, Pb, Sb, Bi, Pr, Tb, Ce, Fe, Ru and mixtures thereof.
- 5. The method of claim 1 wherein the solid comprises reducible oxides of Mn.
- 6. The method of claim 1 wherein the reducible oxide and the boron promoter are associated with a support material.
- 7. The method of claim 1 wherein methane is converted to higher hydrocarbon products in a cyclic manner comprising contacting the solid alternately with a gas comprising methane and with a gaseous oxidant.
- 8. The method of claim 7 wherein the solid is contacted with a gas comprising methane at temperatures selected within the range of about 500.degree. to about 1000.degree. C.
- 9. The method of claim 1 wherein methane is converted to higher hydrocarbon products by contacting the solid concurrently with a gas comprising methane and a gaseous oxidant.
- 10. The method of claim 9 wherein said concurrent contact is conducted at temperatures selected within range of about 300.degree. to about 1200.degree. C.
- 11. The method of claim 9 wherein said concurrent contact is conducted at temperatures selected within the range of about 500.degree. to about 1000.degree. C.
- 12. The method of claim 9 wherein said concurrent contact is conducted at a temperature selected within the range of about 800.degree. to about 900.degree. C.
- 13. In an improved method for converting methane to higher hydrocarbon products which comprises contacting a gas comprising methane at synthesizing conditions with a solid comprising: (a) at least one reducible oxide of at least one metal which oxides when contacted with methane at synthesizing conditions are reduced and produce higher hydrocarbon products and water and (b) at least one member of the group consisting of alkaline earth metals and compounds thereof; the improvement which comprises conducting the contacting in the presence of a promoting amount of at least one member of the group consisting of boron and compounds thereof.
- 14. The method of claim 13 wherein the solid is a mixed oxide composition satisfying the empirical formula:
- MB.sub.b C.sub.c O.sub.x
- wherein M is selected from the group consisting of Mn, Sn, In, Ge, Pb, Sb, Bi, Pr, Tb, Ce, Fe, Ru and mixtures thereof; B is boron; and C is at least one alkaline earth metal; and wherein b is within the range of about 0.1 to about 10, c is within the range of about 0.1 to about 100, and x is the number of oxygen atoms required by the valence states of the other elements.
- 15. The method of claim 14 wherein b is within the range of about 0.1 to about 4.
- 16. The method of claim 14 wherein c is within the range of about 0.5 to about 15.
- 17. The method of claim 14 wherein c is within the range of about 1 to about 6.
- 18. The method of claim 13 wherein the solid comprises reducible oxides of Mn.
- 19. The method of claim 14 wherein the mixed oxide composition comprises reducible oxides of Mn.
- 20. The method of claim 19 wherein M is Mn.
- 21. The method of claim 13 wherein element (b) is at least one member of the group consisting of oxides of alkaline earth metals.
- 22. The method of claim 21 wherein element (b) is magnesia.
- 23. The method of claim 21 wherein element (b) is calcia.
- 24. The method of claim 14 wherein C is Mg.
- 25. The method of claim 14 wherein C is Ca.
- 26. The method of claim 13 wherein the solid further comprises at least one member of the group consisting of alkali metals and compounds thereof.
- 27. The method of claim 26 wherein the alkali metal is sodium.
- 28. The method of claim 26 wherein the alkali metal is lithium.
- 29. The method of claim 26 wherein the solid is a mixed oxide composition satisfying the empirical formula:
- MA.sub.a M.sub.b C.sub.c O.sub.x
- wherein M is selected from the group consisting of Mn, Sn, In, Ge, Pb, Sb, Bi, Pr, Tb, Ce, Fe, Ru and mixtures thereof; A is at least one alkali metal; B is boron; C is at least one alkaline earth metal; and wherein a is within the range of about 0.01 to about 10, b is within the range of about 0.1 to about 20, c is within the range of about 0.1 to about 100, and x is the number of oxygen atoms required by the valence states of the other elements.
- 30. The method of claim 29 wherein b is within the range of about 0.1 to about 10.
- 31. The method of claim 29 wherein c is within the range of about 1 to about 7.
- 32. The method of claim 29 wherein the mixed oxide composition comprises reducible oxides of Mn.
- 33. The method of claim 32 wherein M is Mn.
- 34. The method of claim 29 wherein A is sodium.
- 35. The method of claim 29 wherein A is lithium.
- 36. The method of claim 29 wherein C is Mg.
- 37. The method of claim 29 wherein C is Ca.
- 38. The method of claim 29 wherein the solid contains Mn, Na, B and Mg and the mixed oxide composition is characterized by the presence of the crystalline compound NaB.sub.2 Mg.sub.4 Mn.sub.2 O.sub.x.
- 39. The method of claim 38 wherein the mixed oxide composition is further characterized by an amount of Mn in the composition which is in excess of the stoichiometric amount relative to at least one of the other elements of said crystalline compound.
- 40. The method of claim 39 wherein a stoichiometric excess of Mn relative to boron is provided.
- 41. The method of claim 40 wherein the mixed oxide composition contains excess amounts of Na, Mg and Mn relative to the amounts required by the amount of boron present to satisfy the stoichiometry of said crystalline compound.
CROSS-REFERENCE TO RELATED APPLICATIONS
This application is a continuation-in-part of application Ser. No. 683,296 filed Dec.18, 1984, now abandoned, which in turn is a continuation-in-part of applications Ser. No. 522,937 filed Aug. 12, 1983, now U.S. Pat. No. 4,499,322, which is a continuation-in-part of application Ser. No. 522,936, filed Aug.12, 1983, now U.S. Pat. No. 4,495,374, which is a continuation-in-part of application Ser. No. 600,654 filed Apr. 16, 1984, now U.S. Pat. No. 4,547,611, which is a continuation-in-part of application Ser. No. 600,655 filed Apr. 16 1984, now abandoned.
US Referenced Citations (12)
Continuation in Parts (5)
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Number |
Date |
Country |
Parent |
683296 |
Dec 1984 |
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Parent |
522937 |
Aug 1983 |
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Parent |
522936 |
Aug 1983 |
|
Parent |
600654 |
Apr 1984 |
|
Parent |
600655 |
Apr 1984 |
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