Claims
- 1. A process for producing trialkali metal aluminum hexahydride which comprises:
- reacting
- 2. alkali metal
- 2. aluminum and
- 3. hydrogen
- in the presence of a catalytic amount of at least about 0.001 percent by weight of alkali metal aluminum dihydrocarbon dihydride, based on the alkali metal fed to the process, and of an inert aromatic hydrocarbon solvent for alkali metal aluminum dihydrocarbon dihydride, under conditions suitable to form trialkali metal aluminum hexahydride, thereby producing trialkali metal aluminum hexahydride.
- 2. The process of claim 1 wherein the catalyst is sodium aluminum diethyl dihydride.
- 3. The process of claim 1 for producing trisodium aluminum hexahydride wherein sodium is reacted
- 4. The process of claim 1 for producing tripotassium aluminum hexahydride wherein potassium is reacted.
- 5. The process of claim 1 for producing trilithium aluminum hexahydride wherein lithium is reacted.
- 6. The process of claim 1 wherein the solvent is toluene.
- 7. The process of claim 1 wherein the solvent is xylene.
- 8. The process of claim 1 wherein the solvent is benzene.
- 9. The process of claim 1 wherein the pressure of step A is from about 100 to about 2000 pounds per square inch gage.
- 10. The process of claim 1 wherein the pressure is from about 500 to about 1250 pounds per square inch gage.
- 11. The process of claim 1 wherein the temperature is from about 110.degree. C to about 170.degree. C.
- 12. The process of claim 1 wherein the temperature is from about 125.degree. C to about 160.degree. C.
- 13. The process of claim 1 wherein the temperature is about 170.degree. C.
- 14. The process of claim 1 wherein the amount of catalyst is from about 0.1 percent to about 50 percent by weight based on the alkali metal fed to the process.
- 15. The process of claim 1 wherin the amount of catalyst is from about 1 percent to about 20 percent by weight based on the alkali metal fed to the process.
- 16. The process of claim 1 wherein the amount of catalyst is from about 10 to about 15 percent by weight based on the alkali metal fed to the process.
- 17. The process of claim 1 for producing trisodium aluminum hexahydride wherein sodium is reacted, the temperature is from about 110.degree. C to about 170.degree. C, the pressure of step A is from about 500 to about 1250 pounds per square inch gage and wherein the amount of catalyst is from about 10 to about 15 percent by weight based on the sodium reactant fed to the process.
- 18. The process of claim 1 wherein the amount of aluminum fed is in a molar excess ranging from about stoichiometric to about 50 percent excess about stoichiometric based on the alkali metal fed to the reaction.
CROSS-REFERENCE TO RELATED APPLICATIONS
This application is a containuation-in-part of application Ser. No. 512,120, filed Oct. 4, 1974.
US Referenced Citations (5)
Foreign Referenced Citations (4)
Number |
Date |
Country |
1,515,581 |
Mar 1968 |
FR |
1,116,664 |
Nov 1961 |
DT |
1,080,019 |
Aug 1967 |
UK |
223,788 |
Nov 1968 |
SU |
Non-Patent Literature Citations (4)
Entry |
Chemical Abstracts, v67, 70140c (1967). |
Ashby et al., Inorganic Chemistry v2 pp. 499-504 (1963). |
Ashby et al., Inorganic Chemitry v5, pp. 1615-1617 (1966). |
Chemical Abstracts, v64, 13803b (1966). |
Continuation in Parts (1)
|
Number |
Date |
Country |
Parent |
512120 |
Oct 1974 |
|