Claims
- 1. A process for the fluorination of pyrimidines, said process consisting essentially of reacting, in a solvent of the formula:
- Cx".sub.2 y"--(cy".sub.2).sub.n --COOH
- or
- Cx.sub.2 y--(cy.sub.2).sub.n --CH.sub.2 OH,
- wherein X and Y are independently hydrogen, bromine, chlorine or fluorine, X" and Y" are independently bromine, chlorine, or fluorine, and n is an integer from 0 to 6,
- at a temperature of about the solvent freezing point to about the solvent boiling point, a pyrimidine of the formula ##STR24## with at least about a stoichiometric amount of gaseous fluorine to produce a compound of the formula: ##STR25## wherein R.sub.1 is hydrogen, fluorine, chlorine, bromine or lower alkyl, R.sub.2 is hydrogen or lower alkyl, R.sub.3 is R.sub.1 or, taken with R.sub.5, a 5,6-double bond, R.sub.4 is hydrogen or lower alkyl, R.sub.5 is
- Cx.sub.2 y--(cy.sub.2).sub.n --CH.sub.2 O--,
- Cx".sub.2 y"--(cy".sub.2).sub.n --COO--,
- a 5,6-double bond when taken with R.sub.3, or a 1,6-double bond when taken with R.sub.6, R.sub.6 is hydrogen or a 1,6-double bond when taken with R.sub.5, Y.sup.1 is -NH.sub.2 and Z and Z.sup.1 together are a 3,4-double bond or else Y.sup.1 and Z taken with the 4-carbon atom, are carbonyl and Z.sup.1 is hydrogen.
- 2. Process as claimed in claim 1 wherein said solvent is of the formula:
- Cx".sub.2 y"--(cy".sub.2).sub.n --COOH--.
- 3. Process as claimed in claim 2 wherein said solvent is trifluoroacetic acid.
- 4. Process as claimed in claim 1, wherein the reaction solvent has the formula:
- Cx.sub.2 y--(cy.sub.2).sub.n --CH.sub.2 OH.
- 5. Process as claimed in claim 4 wherein X and Y are halogen.
- 6. Process as claimed in claim 5 wherein said halogen is fluorine.
- 7. Process as claimed in claim 1, wherein Y is --NH.sub.2 and Z and Z' together are a 3,4-double bond.
- 8. Process as claimed in claim 1 wherein the molar ratio of fluorine to said pyrimidine is from about 1:1 to about 2:1.
- 9. Process as claimed in claim 1 wherein an effluent gas stream is discharged from the reaction zone and the reaction is continued at least until fluorine is detected in the effluent gas.
- 10. Process as claimed in claim 1, wherein X" and Y" are fluorine.
- 11. A process for the fluorination of uracil and derivatives thereof consisting essentially of reacting in a solvent at a temperature of about 0.degree. C. to about the solvent boiling point, a uracil derivative of the formula: ##STR26## with at least about a stoichiometric amount of gaseous fluorine to prepare a compound of the formula: ##STR27## wherein R.sub.1 is a hydrogen, fluorine, chlorine, bromine or lower alkyl,
- R.sub.2 is hydrogen or lower alkyl,
- R.sub.3 is hydrogen, fluorine, chlorine, bromine, lower alkyl or taken with R.sub.5 a 5,6-double bond,
- R.sub.4 is hydrogen or lower alkyl,
- R.sub.5 is a 5,6-double bond when taken with R.sub.3 or a 1,6-double bond when taken with R.sub.6 and
- R.sub.6 is hydrogen or a 1,6-double bond when taken with R.sub.5,
- the reaction conducted in a solvent which is
- Cx".sub.2 y"(cy".sub.2).sub.n --COOH
- wherein X" and Y" are independently bromine, chlorine or fluorine, and n is an integer from 0 to 6, and heating the resulting product to produce said compound.
- 12. The process of claim 11, wherein each X" and Y" is fluorine.
- 13. A process for the fluorination of uracil and derivatives thereof consisting essentially of reacting in a solvent at a temperature of about 0.degree. C to about the solvent boiling point, a uracil derivative of the formula: ##STR28## with at least about a stoichiometric amount of gaseous fluorine to prepare a compound of the formula: ##STR29## wherein R.sub.1 is hydrogen, fluorine, chlorine, bromine or lower alkyl,
- R.sub.2 is hydrogen or lower alkyl,
- R.sub.3 is hydrogen, fluorine, chlorine, bromine, or lower alkyl,
- R.sub.4 is hydrogen or lower alkyl,
- R.sub.5 is CX.sub.2 Y(CY.sub.2).sub.n --CH.sub.2 O--, wherein X, Y and n are defined below,
- R.sub.6 is hydrogen,
- the reaction conducted in a solvent which is
- Cx.sub.2 y--(cy.sub.2).sub.n --CH.sub.2 OH
- wherein X and Y are independently hydrogen, bromine, chlorine or fluorine, and n is an integer from 0 to 6.
- 14. The process of claim 13 wherein the reaction is conducted at a temperature of about 52.degree. to about 75.degree. C.
- 15. The process of claim 13 wherein the reaction solvent is trifluoroethanol.
- 16. The process of claim 11, wherein the molar ratio of fluorine to said uracil derivative is from about 1:1 to about 2:1.
- 17. The process of claim 11, wherein the reaction is continued at least until fluorine is detected in the effluent gas.
- 18. The process of claim 11, wherein the reaction solvent is selected from the group consisting of trifluoroacetic acid, and trichloroacetic acid.
- 19. A method for producing 5-fluorouracil comprising reacting uracil with fluorine in trifluoroacetic acid at a temperature from about 14.degree. to about 58.degree. C in an inert gas atmosphere.
- 20. The method of claim 19, wherein said inert gas is nitrogen.
- 21. The process of claim 13 wherein the molar ratio of fluorine to said uracil derivative is from about 1:1 to about 2:1.
- 22. The process of claim 13 wherein the reaction is continued at least until fluorine is detected in the effluent gas.
- 23. The process of claim 14, wherein X and Y are halogen.
- 24. The process of claim 23, wherein said halogen is fluorine.
CROSS-REFERENCE TO RELATED APPLICATION
This application is a continuation-in-part of our copending application Ser. No. 186,443, filed Oct. 4, 1971.
US Referenced Citations (2)
Number |
Name |
Date |
Kind |
3682917 |
Knuniants |
Aug 1972 |
|
3846429 |
Giller et al. |
Nov 1974 |
|
Continuation in Parts (1)
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Number |
Date |
Country |
Parent |
186443 |
Oct 1971 |
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