Claims
- 1. A process which comprises
- (1) reacting pinacolone, of the formula
- (CH.sub.3).sub.3 C--CO--CH.sub.3 (IV),
- with a sulfur chloride of the general formula
- S.sub.n Cl.sub.2 (XII),
- wherein
- n is 1 or 2,
- at a temperature between 0.degree. and 80.degree. C.,
- (2) reacting the reaction mixture directly, without further purification, with an aqueous solution of an amine of the general formula ##STR12## in which R and R' which may be identical or different, are each hydrogen, alkyl of from 1 to 8 carbon atoms, cycloalkyl of from 5 to 6 carbon atoms or aryl of from 6 to 10 carbon atoms and which is optionally substituted by methyl or chlorine, or
- R and R' conjointly form a radical --(CH.sub.2).sub.m -- (where m=4, 5, or 6) or --(CH.sub.2).sub.2 --O--(CH.sub.2).sub.2 --,
- (3) hydrolyzing the thus-formed tert.-butyl-glyoxylthioamide of the general formula ##STR13## wherein R and R' identified as above without intermediate isolation by adding at least 2 moles of alkali metal hydroxide of the formula MOH per mole of pinacolone (IV) and heating for from 2 to 10 hours at 80.degree. to 150.degree. C., to give an alkali metal salt of 3,3-dimethyl-2-oxo-butyric acid of the formula
- (CH.sub.3).sub.3 C--CO--COO.sup..crclbar. M.sup..sym. (Ia),
- wherein
- M is an alkali metal,
- (4) liberating the 3,3-dimethyl-2-oxo-butyric acid of the formula
- (CH.sub.3).sub.3 C--CO--COOH (I),
- from the salt (Ia) by acidifying with a mineral acid, and
- (5) reacting the aqueous solution of 3,3-dimethyl-2-oxo-butyric acid, after filtering off any sulfur precipitated on acidifying, with thiocarbohydrazide of the formula
- H.sub.2 N--NH--CS--NH--NH.sub.2 (II).
- 2. a process as claimed in claim 1 wherein step (1) is effected at a temperature of from 20.degree. to 60.degree. C.
- 3. A process as claimed in claim 1 wherein the sulfur chloride is S.sub.2 Cl.sub.2.
- 4. A process as claimed in claim 1 wherein the sulfur chloride is used in an amount of from 0.5 to 2 moles per mole of pinacolone.
- 5. A process as claimed in claim 3 wherein the sulfur chloride is used in an amount of from 0.5 to 2 moles per mole of pinacolone.
- 6. A process as claimed in claim 3 wherein the sulfur chloride is used in an amount of from 1.0 to 1.2 moles per mole of pinacolone.
- 7. A process as claimed in claim 1 wherein the sulfur chloride is SCl.sub.2.
- 8. A process as claimed in claim 7 wherein the sulfur chloride is used in an amount of from 0.5 to 3 moles per mole of pinacolone.
- 9. A process as claimed in claim 7 wherein the sulfur chloride is used in an amount of from 1.5 to 2.0 moles per mole of pinacolone.
- 10. A process as claimed in claim 1 wherein step (1) is carried out in the presence of a diluent.
- 11. A process as claimed in claim 10 wherein said diluent is carbon tetrachloride or tetrachloroethylene.
- 12. A process as claimed in claim 10 wherein said diluent is excess pinacolone.
- 13. A process as claimed in claim 1 wherein the amine (XIII) as added in step (2) is an aqueous solution having an amine concentration of from 1 to 80% by weight.
- 14. A process as claimed in claim 13 wherein the amine (XIII) as added in step (2) is an aqueous solution having an amine concentration of 20 to 60% by weight.
- 15. A process as claimed in claim 1 wherein from 1 to 5 moles of the amine (XIII) are employed per mole of the reacted pinacolone.
- 16. A process as claimed in claim 15 wherein from 1.5 to 3 moles of the amine (XIII) are employed per mole of the reacted pinacolone.
- 17. A process as claimed in claim 15 wherein from 2.0 to 3.5 moles of the amine (XIII) are employed per mole of the reacted pinacolone.
- 18. A process as claimed in claim 1 wherein the amine (XIII) is selected from ammonia, methylamine, ethylamine, propylamine, isopropylamine, butylamine, pentylamine, hexylamine, octylamine, dimethylamine, diethylamine, dipropylamine, dibutylamine dipentylamine, dihexylamine, dioctylamine, methylethylamine, methylbutylamine, methyloctylamine, cyclohexylamine, dicyclohexylamine, aniline, N-methylaniline, pyrrolidine, piperidene and morpholine.
- 19. A process which comprises
- (a) reacting pinacolone, of the formula
- (CH.sub.3).sub.3 C--CO--CH.sub.3 (IV),
- with a sulfur chloride of the general formula
- S.sub.n Cl.sub.2 (XII),
- wherein
- n is 1 or 2, at a temperature between 0.degree. and 80.degree. C.,
- (b) hydrolyzing the resulting reaction product without intermediate isolation by adding at least 2 moles of alkali metal hydroxide of the formula MOH per mole of pinacolone (IV) and heating for from 2 to 10 hours at 80.degree. C. to 150.degree. C. to give an alkali metal salt of 3,3-dimethyl-2-oxo-butyric acid of the formula
- (CH.sub.3).sub.3 C--CO--COO.sup..crclbar. M.sup..sym. (Ia),
- wherein
- M is an alkali metal,
- (c) liberating the 3,3-dimethyl-2-oxo-butyric acid of the formula
- (CH.sub.3).sub.3 C--CO--COOH (I),
- from the salt (Ia) by acidifying with a mineral acid, and (d) reacting the aqueous solution of 3,3-dimethyl-2-oxo-butyric acid, after filtering off any sulfur precipitated on acidifying, with thiocarbohydrazide of the formula
- H.sub.2 N--NH--CS--NH--NH.sub.2 (II).
- 20. a process as claimed in claim 1 wherein from 2 to 5 moles of the alkali metal hydroxide are used, in step (3) per mole of the tert.-butyl-glyoxyl-thioamide (XIV).
- 21. A process as claimed in claim 20 wherein from 3 to 4 moles of the alkali metal hydroxide are used, in step (3), per mole of the tert.-butyl-glyoxyl-thioamide (XIV).
- 22. A process as claimed in claim 1 wherein the alkali metal hydroxide is sodium or potassium hydroxide.
- 23. A process as claimed in claim 1 wherein step (3) is effected at from 100.degree. to 130.degree. C.
- 24. A process as claimed in claim 23 wherein step (3) is effected at from 110.degree. to 120.degree. C.
- 25. A process as claimed in claim 1 wherein step (3) is effected in the presence, as a diluent, of water.
- 26. A process as claimed in claim 1 wherein steps (1), (2), and (3) are effected continuously.
- 27. A process as claimed in claim 1 wherein the mineral acid in step (4) is hydrochloric acid or sulfuric acid.
- 28. A process for the preparation of 6-tert.-butyl-3-mercapto-4-amino-1,2,4-triazin-5(4H)-one which process comprises reacting pinacolone with sulfur dichloride at a temperature of from 0.degree. to 80.degree. C., adding an aqueous solution of dimethylamine, adding a solution of an alkali metal hydroxide in an amount to provide at least 2 moles of alkali metal hydroxide per mole of pinacolone, heating the resulting mixture to release dimethylamine, adding a mineral acid and filtering off the precipitating elemental sulfur, adding thiocarbohydrazide to give the desired 6-tert.-butyl-3-mercapto-4-amino-1,2,4-triazine-5(4H)-one.
Priority Claims (1)
Number |
Date |
Country |
Kind |
2460889 |
Dec 1974 |
DEX |
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Parent Case Info
This is a division of Application Ser. No. 640,830, filed Dec. 15, 1975, now U.S. Pat. No. 4,113,767.
US Referenced Citations (2)
Number |
Name |
Date |
Kind |
4058526 |
Merz et al. |
Nov 1977 |
|
4113767 |
Merz |
Sep 1978 |
|
Foreign Referenced Citations (1)
Number |
Date |
Country |
2460889 |
Dec 1974 |
DEX |
Divisions (1)
|
Number |
Date |
Country |
Parent |
640830 |
Dec 1975 |
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