Claims
- 1. A method for producing a sulfoxide (II) represented by the following formula (II): (wherein R1, R2, R3 and R4 have the same meanings as defined below), which comprises the step of oxidizing a thioether (I) represented by the following formula (I): (wherein R1 represents hydrogen atom, methoxy group or difluoromethoxy group; R2 represents methyl group or methoxy group; R3 represents 3-methoxypropoxy group, methoxy group or 2,2,2-trifluoroethoxy group; and R4 represents hydrogen atom or methyl group) with a) a perborate in the presence of an acid anhydride or a metal catalyst or b) an N-halosuccinimide, a 1,3-dihalo-5,5-dimethylhydantoin or dichloroisocyanurate in the presence of a base.
- 2. The method as claimed in claim 1, which comprises the step of oxidizing with a) a perborate in the presence of an acid anhydride or a metal catalyst.
- 3. The method as claimed in claim 2, wherein the perborate is sodium perborate.
- 4. The method as claimed in claim 2, wherein the perborate is sodium perborate tetrahydrate or sodium perborate monohydrate.
- 5. The method as claimed in claim 2, wherein the perborate is used in an amount of 0.9 to 1.5 equivalents to the thioether (I).
- 6. The method as claimed in claim 2, wherein the oxidative reaction is conducted in methanol, ethanol, propanol and mixture solvents such as methanol/toluene, ethanol/toluene, propanol/toluene, water/methanol, water/ethanol, water/propanol and toluene/dimethylformamide or acetic acid.
- 7. The method as claimed in claim 2, which is conducted in the presence of the acid anhydride.
- 8. The method as claimed in claim 7, wherein the acid anhydride is at least one selected from the group consisting of acetic anhydride, propionic anhydride, butyric anhydride, succinic anhydride, maleic anhydride, benzoic anhydride and phthalic anhydride.
- 9. The method as claimed in claim 7, wherein the acid anhydride is used in an amount of 0.9 to 1.5 equivalents to the thioether (I).
- 10. The method as claimed in claim 7, wherein the acid anhydride is used in an amount of 1.0 to 2.0 equivalents to the perborate, and of 0.9 to 1.5 equivalents to the thioether (I).
- 11. The method as claimed in claim 2, which is conducted in the presence of the metal catalyst.
- 12. The method as claimed in claim 11, wherein the metal catalyst is at least one selected from the group consisting of vanadium pentaoxide, vanadyl acetylacetonate, molybdenum oxide actylacetonate, ammonium heptamolybdate tetrahydrate, ammonium molybdate, sodium vanadate, titanium tetraisopropoxide, titanium trichloride, tellurium dioxide, selenium dioxide, methyl trioxorhenium and tungsten oxide.
- 13. The method as claimed in claim 11, wherein the metal catalyst is used in an amount of 0.05 to 0.15 equivalent to the perborate.
- 14. The method as claimed in claim 1, which comprises the step of oxidizing with b) N-halosuccinimide, 1,3-dihalo-5,5-dimethylhydantoin or dichloroisocyanurate in the presence of a base.
- 15. The method as claimed in claim 14, wherein the N-halosuccinimide is N-chlorosuccinimide or N-bromosuccinimide.
- 16. The method as claimed in claim 14, wherein the N-halosuccinimide is used in an amount of 0.9 to 1.5 equivalents to the thioether (I).
- 17. The method as claimed in claim 14, wherein the 1,3-dihalo-5,5-dimethylhydantoin is 1,3-dichloro-5,5-dimethylhydantoin or 1,3-dibromo-5,5-dimethylhydantoin.
- 18. The method as claimed in claim 14, wherein the 1,3-dihalo-5,5-dimethylhydantoin is used in an amount of 0.4 to 0.8 equivalent to the thioether (I).
- 19. The method as claimed in claim 14, wherein the dichloroisocyanurate is sodium dichloroisocyanurate or potassium dichloroisocyanurate.
- 20. The method as claimed in claim 19, wherein the dichloroisocyanurate is used in an amount of 0.4 to 0.8 equivalent to the thioether (I).
- 21. The method as claimed in claim 14, wherein the base is an inorganic base.
- 22. The method as claimed in claim 21, wherein the base is at least one selected from the group consisting of sodium hydroxide, potassium hydroxide, lithium hydroxide, sodium carbonate, potassium carbonate, sodium hydrogen carbonate, potassium hydrogen carbonate, sodium phosphate, potassium phosphate, sodium hydrogen phosphate, sodium formate, potassium formate, sodium acetate and potassium acetate.
- 23. The method as claimed in claim 21, wherein the base is used in an amount of 0.9 to 3.0 equivalents to the N-halosuccinimide, and of 0.4 to 1.5 equivalents to the 1,3-dihalo-5,5-dimethylhydantoin or dichloroisocyanurate salt.
- 24. The method as claimed in claim 14, wherein the oxidation is conducted in the solvent at least one selected from the group consisting of N,N-dimethylformamide, acetonitrile, toluene, tetrahydrofuran, lower fatty acid esters and water.
- 25. The method as claimed in claim 14, wherein the oxidation is conducted in a solvent at least one selected from the group consisting of N,N-dimethylformamide, acetonitrile, toluene, tetrahydrofuran and lower fatty acid esters, in the presence of water.
- 26. The method as claimed in claim 1, wherein the amount of perborate is in the range of 0.8 to 1.7 equivalents to thioether (I).
- 27. The method as claimed in claim 1, wherein the amount of N-halosuccinimide is 0.8 to 1.7 equivalents to thioether (I).
- 28. The method as claimed in claim 1, wherein the amount of 1,3-dihalo-5,5-dimethylhydantoin is in the range of 0.3 to 1.0 equivalent to thioether (I).
- 29. The method as claimed in claim 1, wherein the amount of dichloroisocyanurate is in the range of 0.3 to 1.0 equivalent to thioether (I).
- 30. The method as claimed in claim 1, wherein the amount of acid anhydride is in the range of 0.8 to 1.7 equivalents to thioether (I).
- 31. The method as claimed in claim 1, wherein the amount of metal catalyst is 0.05 to 0.15 equivalent to perborate.
- 32. The method as claimed in claim 1, wherein the amount of base is 0.8 to 4.0 equivalents to N-halosuccinimide.
- 33. The method as claimed in claim 1, wherein the amount of base is 0.4 to 2.0 equivalents to 1,3-dihalo-5,5-dimethylhydrantoin or dichloroisocyanurate.
- 34. The method as claimed in claim 24, wherein the amount of water is in the range of 0.1 to 50 ml per 1 g of thioether (I).
- 35. The method as claimed in claim 24, wherein the amount of solvent ranges from 1 to 100 ml per 1 g of thioether (I).
Priority Claims (3)
Number |
Date |
Country |
Kind |
9-186095 |
Jul 1997 |
JP |
|
9-197119 |
Jul 1997 |
JP |
|
10-117706 |
Apr 1998 |
JP |
|
Parent Case Info
This application is the national phase under 35 U.S.C. §371 of PCT International Application No. PCT/JP98/03113 which has an International filing date of Jul. 10, 1998, which designated the United States of America.
PCT Information
Filing Document |
Filing Date |
Country |
Kind |
102e Date |
371c Date |
PCT/JP98/03113 |
|
WO |
00 |
1/3/2000 |
1/3/2000 |
Publishing Document |
Publishing Date |
Country |
Kind |
WO99/02521 |
1/21/1999 |
WO |
A |
US Referenced Citations (2)
Number |
Name |
Date |
Kind |
4045563 |
Berntsson et al. |
Aug 1977 |
|
5374730 |
Slemon et al. |
Dec 1994 |
|
Foreign Referenced Citations (7)
Number |
Date |
Country |
05-93463 |
Nov 1997 |
EP |
52-62275 |
May 1977 |
JP |
56-142286 |
Nov 1981 |
JP |
61-205211 |
Sep 1986 |
JP |
1-484265 |
May 1992 |
JP |
3-52887 |
Jul 1993 |
JP |
5-507714 |
Nov 1993 |
JP |
Non-Patent Literature Citations (2)
Entry |
M. Fieser, Fieser and Fieser's Reagents for Organic Synthesis, U.S. New York, vol. 12 12, 1986, p. 452 (XP-002109649). |
Paquette L A, Encyclopedia of Reagents for Organic Synthesis, vol. 7, 1995, pp. 4611-4613 (XP002109650). |