Claims
- 1. A process providing a secondary amine of the general formula, R—NH—R′, comprising:providing an organic electrophile, R—X, and a primary amine R′—NH2, wherein R and R′ each comprises the same or a different hydrocarbon having one or more carbon atoms and X comprises a leaving group, provided that the carbon atom covalently bonded to said leaving group and the carbon atom covalently bonded to said amine nitrogen atom are both saturated, and reacting said organic electrophile with said primary amine in an anhydrous solvent containing a cesium base in an amount sufficient to preferentially promote mono-N-alkylation of said primary amine by said organic electrophile, to provide a secondary amine.
- 2. The process as in claim 1, wherein said leaving group X is selected from the group consisting of chloride, bromide, iodide, O-Ms and O-Ts.
- 3. The process as in claim 1, wherein said solvent comprises a polar aprotic solvent.
- 4. The process of claim 1, wherein said solvent is selected from the group consisting of dimethyl sulfoxide, N,N-dimethylformamide, NMP, DMAC and mixtures thereof.
- 5. The process as in claim 1, further comprising removing water produced by said reaction of said organic electrophile with said primary amine.
- 6. The process as in claim 5, wherein removing water further comprises adding a molecular sieve having a pore size of about 3-5 Å.
- 7. The process as in claim 1, further comprising adding a halide-exchange promoting agent.
- 8. The process as in claim 7, wherein the halide-exchange promoting agent comprises tetrabutylammonium iodide.
- 9. The process as in claim 8, wherein about 0.1 to 2.0 moles of tetrabutylammonium iodide is added per mole of said primary amine.
- 10. The process as in claim 1, wherein said organic electrophile is covalently attached to an insoluble support matrix during reaction of said organic electrophile with said primary amine.
- 11. The process as in claim 10, wherein said insoluble support matrix comprises a Merrifield resin or Wang resin.
- 12. The process as in claim 1, wherein said primary amine is covalently bonded to an insoluble support matrix during reaction of said organic electrophile with said primary amine.
- 13. The process as in claim 12, wherein said insoluble support matrix comprises a Merrifield resin or a Wang resin.
- 14. The process as in claim 1, wherein said organic electrophile further comprises at least one chiral center, wherein each said chiral center is preserved during reaction of said organic electrophile with said primary amine.
- 15. The process as in claim 1, wherein said primary amine further comprises at least one chiral center, wherein each said chiral center is preserved during reaction of said organic electrophile with said primary amine.
- 16. The process as in claim 1, wherein said cesium base is selected from the group consisting of cesium carbonate, cesium bicarbonate, cesium hydroxide, and a mixture thereof.
- 17. A process for providing polyamines, comprising;providing an organic electrophile R—X wherein X is selected from the group consisting of chloride, bromide, iodide, O-Ts and O-Ms, and R comprises a hydrocarbon having 1-50 carbon atoms, provided that the carbon atom covalently bonded to X is saturated, and a primary amine R′—NH2, wherein R′ comprises a hydrocarbon having 1-50 carbon atoms, provided that the carbon atom covalently bonded to the amine nitrogen atom is saturated, and R′ further comprises a thiol substituent, and reacting said organic electrophile with said primary amine in an anhydrous solvent comprising a cesium base in an amount sufficient to preferentially provide N-alkylated polyamine.
- 18. The process as in claim 17, wherein said primary amine is 2-aminoethanethiol hydrochloride.
- 19. The process as in claim 17, wherein said organic electrophile is 2-bromoethylamine hydrobromide.
- 20. The process as in claim 17, wherein said reaction further comprises adding a reaction-promoting amount of a molecular sieve with a pore size of about 3-5 Å.
- 21. The process as in claim 17, wherein said N-alkylated polyamine is N-(2-(2-aminoethylthio)ethyl)ethylenediamine.
- 22. The process as in claim 17, wherein said cesium base is selected from the group consisting of cesium carbonate, cesium bicarbonate, cesium bromide, cesium hydroxide, and mixtures thereof.
RELATED APPLICATIONS
The present application claims priority to U.S. Provisional application 60/121,867, filed Feb. 26, 1999, U.S. Provisional application 60/126,108, filed Mar. 25, 1999, and U.S. Provisional application 60/138,655, filed Jun. 14, 1999 each of which is incorporated herein by reference in its respective entirety.
Foreign Referenced Citations (1)
Number |
Date |
Country |
02202855 |
Aug 1990 |
JP |
Provisional Applications (3)
|
Number |
Date |
Country |
|
60/121867 |
Feb 1999 |
US |
|
60/126108 |
Mar 1999 |
US |
|
60/138655 |
Jun 1999 |
US |