Title of Invention

A PROCESS FOR PREPARING A THIOESTER COMPOUND

Abstract 1. A process for preparing a thioester compound of formula A: (A) wherein R1, R2, and R4 are each selected from the group consisting of hydrogen, substituted or unsubstituted lower alkyl and substituted lower alkoxy; and R3 is selected from the group consisting of hydrogen and substituted or unsubstituted lower alkyl, said process comprising reacting a thioether compound of formula B: (B) wherein R1 through R4 are as in formula A with an oxidizing agent to produce selective oxidation of the thioether compound of formula B to form the thioester compound of formula A, wherein the oxidizing agent is tert-butyl hydroperoxide or Oxone®, and if the oxidizing agent is tert-butyl hydroperoxide the molar ratio of tert-butyl hydroperoxide to the compound of formula B is in the range of about 1.15 to about 4.5.
Full Text

ORIGINAL
726/MUMNP/2003

FORM 2
THE PATENTS ACT, 1970
[39 OF 1970]

COMPLETE SPECIFICATION [See Section 10; Rule 13]
"A PROCESS FOR PREPARING A THIOESTER COMPOUND"
TEVA PHARMACEUTICALS INDUSTRIES, LTD., having a place of business at 5 Basel Street, P.O. Box 3190, Petah Tiqva, 49131, Israel,


GRANTED
10/5/2006


The following specification particularly describes the nature of the invention and the manner in which it is to be performed:-




The present invention relates to a process for preparing a thioester compound.
This invention claims the benefit under 35 U.S.C. §1.119(e) of provisional application Serial No. 60/266,162, filed February 2,2001.
FIELD OF THE INVENTION
The present invention relates to novel processes of preparing substituted 2-(2-pyridylmethyl) sulfinyl-1H-benzimidazoles.
BACKGROUND OF THE INVENTION
Several substituted 2-(2-pyridylmethyl]sulfinyl]-1H-benzimidazole are known gastric proton pump inhibitors. These include omeprazole (5-inethoxy-2-[[(4-methoxy-3,5-dimethyl-2-pyidyl)methyl]sulfinyl]-1H-benzimidazole), lansoprazole (2-[[[3-methyl-4-(2,2,2-trifluoro-ethoxy)2-pyidyl)methyl]sulfinyl]-1H-benzimidazole), pantoprazole (5-
(difluoromemoxy)-2-[[(3,4-dithemoxy-2-pyidyl)methyl]sulfinyl]-1H-benzimidazole), and
rabeprazole(2-[[[4-(3-methoxy-propoxy)-3-memyl-2-pyidinyl]methyl]sulfinyl]-1H-benzimidazole. Fox example, omeprazole is a proton pump inhibitor commercially available for the treatment of gastric ulcers. The compound is disclosed in European Patent No. 5318.
A

The reported synthesis of these substituted 2-(2-pyridyhnethyl)sulfinyl-1H-benzimidazoles principally involves generally an oxidation process of a thioether moiety to form a thioester moiety of the compound of formula A:


Various methods employing various different oxidants to perform this oxidation are known. For example, Canadian Patent No. 1,263,119 describes the use of hydrogen peroxide over a vanadium catalyst (such as vanadium pentoxide, sodium vanadate and vanadium acteylacetonate). Canadian Patent No. 1,127,158 similarly describes the use of peracids, 5 peresters, ozone, etc. European Patent Application, Publication No. 533,264 describes the use of magnesium monoperoxyphthalate as the oxidizing agent. PCT Publication No. W091/18895 describes the use of m-chloroperoxy benzoic acid as the oxidizing agent. GB Pat. No.2,069,492 generally describes this acid and other peroxy acids in the oxidation of substituted (phenylthiomethyl)pyridines.
10
Use of tert-butyl hydroperoxide (TBHP) as an oxidant has already been suggested for the performance of various organic oxidations. Sharpless et at, Aldrichimica Acta 12:63 (1979) review the use of THBP as an oxidant and compared with hydrogen peroxide and other peracids. Sharpless et al. describe the use of TBHP in the epoxidation of olefinic
15 alcohols in the presence of VO(acac)2 or Mo(CO)5 catalysts. The oxidation of sulphides,
however, is not described.
In an effort to develop a method for the selective oxidation of sulphides to
sulphoxides, Choudray et al, J. Mol. Catalysts, 75:L7-L12 (1992) describe the use of TBHP
20 in the presence of vanadium pillared clay. The results demonstrated selectivity for the
oxidation to sulphoxide in preference to the sulphone far superior to that of known TBHP/vanadium catalysts. The use of VO(acac)2 or V2O5 resulted in sulphones rather than sulfoxide predominating in the final product.
25 There has been a long felt need for efficient and safe methods for the selective
oxidation of a thioether moiety of formula B to a thioester moiety of formula A. The present invention provides efficient and safe methods of preparing various substituted 2-(2-pyridylmethyl) sulfinyl-1H-benzimidazoles.
30
SUMMARY OF THE INVENTION
The present invention provides a process for preparing a thioester compound of formula A:




10

A
wherein R1, R2, and R4 are each selected from the group consisting of hydrogen, substituted or unsubstituted lower alkyl and substituted or unsubstituted lower alkoxy; and R3 is selected from the group consisting of hydrogen and substituted or unsubstituted lower alkyl, comprising reacting a thioether compound of formula B

15

20

25

B
wherein R1through R4 are as in formula A, with an oxidizing agent to produce selective oxidation of the thioether compound of formula B to form the thioester compound of formula A.



30

The present invention further provides a process for preparing a thioester compound of compound of formula A, comprising reacting a thioether compound of formula B with Oxone® (Oxone monopersulphate).
The present invention further provides a process for preparing a thioester compound of compound of fonnula A, comprising reacting a thioether compound of formula B with tert-


butyl hydroperoxide (TBHP) in the presence of a catalyst selected from the group consisting of vanadyl (TV) acetylacetonate, sodium metavanadate and vanadium pentoxide.
The substituted 2-(2-pyridymethyl]sulfinyl]-1H-benzimidazole prepared according to 5 the process of the present invention yield the desired products in a relatively high yield with only small amounts of the corresponding sulphone as by-product.
An object of the present invention is to provide an improved process of selective oxidation of 5-methoxy-2-[[(4-methoxy-3,5-dimethyl-2-pyridyl)methyl]thio]-1H-10 benzimidazole (MPB) that utilizes a non-hazardous oxidant and results in the selective production of 5-methoxy-2-[[(4-methoxy-3,5-dmiethyl-2-pyridyl)methyl]sulfinyl]-1H-benzimidazole (omeprazole), i.e., the corresponding sulphoxide, with only minor amounts of 5-methoxy-2[[(4-methoxy-3,5-dimethyl-2-pyridyl)methyl]sulphonyl]benzimidazole.
15 Another object of the present invention is to provide an improved process of selective
oxidation of 2-[[[3-methyl-4-(2,2,2-trifluoro-ethoxy)-2-pyridinyl]methyl]thio]-1H-benzimidazole that utilizes a non-hazardous oxidant and results in the selective production of 2-[[[3-methyl-4-(2,2,2-tafluoro-ethoxy)-2-pyridinyl]methyl]sulfinyl]-1H-benzimidazole (lansoprazole), i.e., the corresponding sulphoxide, with only minor amounts of 2-[[[3-methyI-
20 4-(2,2,2-trifluoro-ethoxy)-2-pyridinyl]methyl]sulphonyl]-1H-benzimidazole.
Another object of the present invention is to provide an improved process of selective
oxidation of 5-(difluoromethoxy)-24[(3,4-dimethoxy-2-pyridthyl)methyl]thio]-1H-
benzimidazole that utilizes a non-hazardous oxidant and results in the selective production of
25 5-(difluoromethoxy)-2-[[(3,4-dimethoxy-2-pyridinyl)methyl]sulfinyl]-1H-benzimidazole
(pantoprazole), i.e., the corresponding sulphoxide, with only minor amounts of 5-(difluoromethoxy)-2-[[(3,4-dimethoxy-2-pyridmyl)methyl]sulphonyl]-1H-benzimidazole.
Another object of the present invention is to provide an improved process of selective 30 oxidation of 2-[[[4-(3-methoxy-propoxy)-3-methyl-2-pyidmyl]methyl]thio]-1H-
benzimidazole that utilizes a non-hazardous oxidant and results in the selective production of


5-methoxy-2-[[(4-methoxy-3,5-dimethyl-2-pyrifyl)methyl]sulfinyl]-1H-benzimidazole
(rabeprazole), i.e., the corresponding sulphoxide, with only minor amounts of 5-methoxy-
2[[(4-memoxy-3,5-dimethyl-2-pyridyl)methyl]sulphonyl]-lH-berizimidazole.
5 Another object of the present invention is to provide an improved process of preparing
omeprazole while the amount of 5-methoxy-2-[[(4-methoxy-3,5-dimethyl-2-pyridyl)methyl] sulphonyl]-1H-benzirnidazole (SOMP) as by-product when the reaction proceeds to completion, is typically within the range of about 1 to about 4.5% by weight of the crude product mixture.
10
Another object of the present invention is to provide an improved process of preparing lansoprazole while the amount of 2-[[[3-methyl-4-(2,2,2-trifluoro-ethoxy)-2-pyridinyl] methyl]sulphonyl]-1H-benzimidazole as by-product when the reaction proceeds to completion, is typically within the range of about 1 to about 4.5% by weight of the crude
15 product mixture.
Another object of the present invention is to provide an improved process of preparing pantoprazole while the amount of 5-(difluoromethoxy)-2-[[(3,4-dimethoxy-2-pyridrnyl) methyl]sulphonyl]-1H-benzimidazole as by-product when the reaction proceeds to 20 completion, is typically within the range of about 1 to about 4.5% by weight of the crude product mixture.
Another object of the present invention is to provide an improved process of preparing rabeprazole while the amount of 5-methoxy-2-[[(4-methoxy-3,5-dimethyl-2-pyridinyl) 25 memyl]sulphonyl]-1H-benzimidazo]e as by-product when the reaction proceeds to
completion, is typically within the range of about 1 to about 4.5% by weight of the crude product mixture.

30

DETAILED DESCRIPTION OF THE INVENTION

Definitions: As used herein, the following abbreviations are used:"VO
(acac)2" is vanadium bis acetylacetonate ;"TBHP" is tert-butyl
hydroperoxide;"NaV03"is sodium meta-vanadate; "V205"is vanadium
pentoxide;"MPB" is 5-methoxy-2- [ [ (4-methoxy-3, 5-dimethyl-
2pyridyl) methyl] thio] benzimidazole; "OMP" is omeprazole; "SOMP"
is 5-methoxy-2- [ [ (4- methoxy-3,5-dimethyl-2-pyridyl)
methyl]sulphonyl]-lH-benzimidazole ; "Oxone" refers to a trademark
name of an oxidizing agent under DuPont for an acidic, white,
granular, free flowing solid containing the active ingredient
potassium peroxymonosulfate; "TBAB" is tertbutyl ammonium
bromide which is a quaternary ammonium salt that is one of the
most common phase transfer catalysts; "substantially free" refers to
sulphone by-product less than about 1 to about 4.5% by weight of
the crude product mixture.
The present invention provides a process for preparing a thioester
compound of formula A:

B

wherein Rl, R2, and R4 are each selected from the group consisting of hydrogen, substituted or unsubstituted lower alkyl and substituted or unsubstituted lower alkoxy; and R3 is selected from the group consisting of hydrogen and substituted or unsubstituted lower alkyl, comprising reacting a thioether compound of formula B


wherein R1 through R4 are as in formula A, with an oxidizing agent to produce selective oxidation of the thioether compound of formula B to form the thioester compound of fonnula A.
5 Preferably, the present invention provides the preparation of substituted 2-(2-
pyridylmethyl)sulfinyl-1H-benzirnidazoles of formula A, wherein R1 is methyl; R2 is methoxy; R3 is methyl and R4 is methoxy. The compound is omeprazole.
Preferably, the present invention provides the preparation of substituted 2-(2-10 pyridylmethyl)sulfinyl-1H-benzirnidazoles of formula A, wherein R1 is methyl; R2 is 2-trifluoroethoxy; R3 is hydrogen and R4 is hydrogen. The compound is lansoprazole.
Preferably, the present invention provides the preparation of substituted 2-(2-pyridylmethyl)sulfinyl-1H-benzirnidazoles of formula A, wherein R1 is methoxy; R2 is 15 methoxy; R3 is hydrogen and R4 is difiuoromethoxy. The compound is pantoprazole.
Preferably, the present invention provides the preparation of substituted 2-(2-pyridylmethyl)sulfinyl-1H-benzirnidazoles of formula A, wherein R1 is methyl; R2 is MeOCH2CH2CH2O, R3 is hydrogen and R4 is hydrogen. The compound is rabeprazole. 20
According to one embodiment, the oxidation is performed with tert-butyl hydroperoxide (TBHP) in the presence of a catalyst selected from the group consisting of vanadyl bis-acetylacetonate, sodium meta-vanadate and vanadium pentoxide. Preferably, the catalyst is vanadyl bis-acetylacetonate. 25
According to another embodiment, the molar ratio of tart-butyl hydroperoxide (TBHP) to a compound of formula B, is in the range of about 1.15 to about 4.5. Preferably, the compound of formula A includes 5-methoxy-2-[[(4-methoxy-3,5-dimethyl-2-pyridyl)methyl]thio]-1H-benzirnidazole, 2[[[3-methyl-4-(2,2,2-trifluoro-ethoxy)-2-30 pyridinyl]methyl]thio]-1H-benzimidazole, 5-(difluoromethoxy)-2-[[3,4-dimethoxy-2-


pyridinyi)methyl](hio]-1H-benzimidazole, and 2-[[[4-3-methoxy-propoxy)-3-methyl-2-pyridinyl]methyl]thio]-1H-benzimidazole.
According to another embodiment, the molar ratio of vanadyl bis-acetylacetonate to 5 the compound of formula B is from about 0.01 to about 0.6.
According to another embodiment, the oxidation by tert-butyl hydroperoxide (TBHP) in the presence of a catalyst is performed in an organic solvent selected from the group consisting of toluene, lower alkanols and ethyl acetate. 10
Another preferred embodiment of the present invention is that the oxidation is performed in an organic solvent such as toluene, a lower alkanol preferably isopropanol or ethyl acetate. Most preferable solvent is toluene or isopropanol.
15 Preferably, the oxidation of substituted 2-(2-pyridylmethyl)sulfinyl- 1H-
benzimidazoles of formula A is performed at temperature ranging from about -10 °C to about 30°C.
Preferably, the oxidation of substituted 2-(2-pyridylmethyl)sulfinyl-1H-20 benzhnidazoles of formula A is performed over a period of about 2 to about 10 hours.
According to another embodiment, the oxidation is performed in the presence of Oxone (Oxone monopersulphate).
25 According to another embodiment, the molar ratio between Oxone® (Oxone
monopersulphate) and the compound of formula B is from about 1.25 to about 1.6:1, most preferably about 1.4 to about 1.6:1.
According to another embodiment, the oxidation by Oxone® (Oxone 30 monopersulphate) is performed in the presence of an aqueous organic solvent. Preferably, the organic solvent is acetone, methanol or in two-phase system (CH2C12 / H2O, (ethyl acetate /

H2O) in the presence of phase-transferred catalyst (e.g. TBAB). More preferably, the oxidation is performed in about 5% aqueous methanol.
Preferably, the oxidation of substituted 2-(2-pyridylmethyl)sulfinyl-1H-5 benzimidazoles of formula A is performed in a two-phase system selected from (CH2C12 / H2O) and (ethyl acetate / H2O),
Preferably, the oxidation of substituted 2-(2-pyridylmemyl)sulfinyl-1H-benzimidazoles of formula A is performed in the presence of tert-butyl ammonium bromide 10 (TBAB).
According to another embodiment, the oxidation by Oxone® (Oxone monopersulphate) is performed at a temperature ranging from about —10°C to about 30°C over a time period of about 2 to about 10 hours. 15
The oxidation conditions of the present invention result in the production of the compound of formula A, wherein the amount of sulphone derivative is less than about 0.5% (wt/wt) of the final product preferably less than 0.2% (wt/wt).
20 Preferably, the pure products prepared in according to the disclosed method include
pantoprazole, lansoprazole, omeprazole and rabeprazole.
The invention will now be exemplified by the following non-limiting Examples.
25 EXAMPLES
Example 1
30
1.5 mg (0.6% molar) VO (acac)2) was dissolved in 12 ml ethanol at room temperature.
The solution was stirred and 3 grams of 5-methoxy-2-[[(4-methoxy-3,5-dimethyl-2-
pyridyl)memyl]thio]bezimidazole (MPB) were added. 1.5 ml aqueous tert-butyl

hydroperoxide (TBHP) (70%) was added over a 5-minute period at 16-17 C and the solution was then stirred for 3 hours. After completion of the reaction, the product mixture was cooled to about 15°C and treated with aqueous sodium metabisulphate. The resultant solid was filtered off, washed with cooled ethyl acetate to afford the end product as an almost white 5 solid (2.5 grams, yield 79%).
Example 2

10
15 mg (0.6% molar) VO(acac)2) in 5 ml toluene were added to a suspension of 3
grams of 5-methoxy-2-[[(4-methoxy-3,5-dimethyl-2-pyridyl)methyl]thio]benzimidazole
(MPB) in 30 ml toluene at a temperature of about 5°C. 3.5 ml of tert-bvtyl hydroperoxide
(TBHP) in toluene (3M, 115%) were added dropwise, while the temperature was maintained
15 between 5 and 7°C. Upon completing the addition of the TBHP, the temperature rose to
22°C. The reaction was allowed to proceed to completion (about 3 hours), after which the
cooled product mixture was treated with aqueous sodium metabisulphite. The solid product
was filtered off, washed with cooled ethyl acetate and dried in an oven (yield 80.7%)
20
Example3
25
1.5 mg (0.6% molar) VO (acac)2 is dissolved in 12 ml ethanol at room temperature.
The solution is stirred and 3 grams of 2-[[[3-methyl-4-(2,2,2-trifluoro-ethoxy)-2-
pyridinyl]methyl]thio]-1H-benzimidazole are added. 1.5 ml aqueous tert-butyl
hydroperoxide (TBHP) (70%) is added over a 5-minute period at 16-17°C and the solution is
30 then stirred for 3 hours. After completion of the reaction, the product mixture is cooled to
about 15°C and treated with aqueous sodium metabisulphate. The resultant solid is filtered
off, washed with cooled ethyl acetate to afford the end product as an almost white solid (2.5
grams, yield 79%).


Example 4
5
1.5 mg (0.6% molar) VO (acac)2) is dissolved in 12 ml ethanol at room temperature. The solution is stirred and 3 grams of 5-(difluoromethoxy)-2-[[(3,4-dimethoxy-2-pyridinyl)methyl]memyl]truo]-1H-ben2rinidazole are added. 1.5 ml aqueous tert-butyl
10 hydroperoxide (TBHP) (70%) is added over a 5-minute period at 16-17°C and the solution is then stirred for 3 hours. After completion of the reaction, the product mixture is cooled to about 15°C and treated with aqueous sodium metabisulphate. The resultant solid is filtered off, washed with cooled ethyl acetate to afford the end product as an almost white solid (2.5 grams, yield 79%).
15
Example 5
20
1.5 mg (0.6% molar) VO (acac)2) is dissolved in 12 ml ethanol at room temperature. The solution is stirred and 3 grams of 2-[[[4-(3-methoxy-propxy)-3-methyl-2-pyidmyl]memyl]thio]-1H--berizimidazole are added. 1.5 ml aqueous tert-butyl hydroperoxide 25 (TBHP) (70%) is added over a 5-minute period at 16-17°C and the solution is then stirred for 3 hours. After completion of the reaction, the product mixture is cooled to about 15°C and treated with aqueous sodium metabisulphate. The resultant solid is filtered off, washed with cooled ethyl acetate to afford the end product as an almost white solid (2.5 grams, yield 79%).


Example 6 Changes of Experimental Conditions and Yi


The above described processes of Example 1 and Example 2 were repeated while using the conditions given in Table I below, to give the following results:
Table I


Example 7 Comparison with the Method disclosed by Canadian Patent 1,263,119 4 mg (0.06% molar) VO (acac)2 were added to suspension of 9 grams of 5-methoxy-2-[[(4-memoxy-3,5-dimemyl-2-pyridyl)methyl]thio]-1H-benzimidazole (MPB) in 66 ml ethanol S at room temperature. 35 ml of 35% aqueous hydrogen peroxide (150% mol) was added at room temperature with no visible exotherm, the mixture was then stirred. After 12 hours the reaction mixture still contained 65% of untreated MPB and only 32% omeprazole. Prolongation of the reaction time did not lead to further production of omeprazole.
10
Example 8
Selective Oxidation By Oxone® of 5-methoxy-2-[[(4-methoxy-3,5-dimethyl-2-pyridyl) methyl] thio)-lH-benzimidazole to form 5-methoxy-2-[[(4-mefcoxy-3,5-dimethyl-2-pyridyl) methyl] sulfinyl]1H-benzirnidazole (Omeprazole) 15
A mixture of 3 grams 5-memoxy-2-[[(4-memoxy-3,5-dimethyl-2-pyridyl)methyl]
thio]benzimidazole (MPB), 3 grams NaHCO3 and 20 ml aqueous methanol was cooled to
-2°C and 3.5 ml (5.69 mmol) Oxone® was added. The mixture was stirred for 4 hours at 0°C
and a further 1gram (mmol) Oxone® was added and stirring continued for 1.5 hours. A
20 solution of 0.8 gram sodium metabisulfite in 20ml water was added dropwise over 5-10
minutes. After further stirring the resultant precipitate was filtered, washed successively with
water and 50% aqueous methanol and dried.
Yield 2.7 grams, 84% (purity 98.1%), SOMP 0.15%. 25
Example 9 Changes of Experimental Conditions and Yields
30 The above described reaction of Example 8 was repeated while using the conditions
given in Table II below, to give the following results:


Table II
Example 10
Selective Oxidation By Oxone® of 2-[[[3-methvl-4-(2.2,2-trifluoro-ethoxy)-2-
pyridinvl]methvl]thio]-lH-benzimidazole to form of 2-[[[3-methyl-4-(2,2,2-trifluoro-ethoxy)-
2-pvridmvl]methvl]sulfinvl]- lH-benzimidazole (Lansoprazole)
A mixture of 3 grams 2-[[[3-methyl-4-(2,2,2-trifluoro-ethoxy)-2-pyridinyl] methyl] thio]-H-benzimidazole, 3 grams NaHCO3 and 20 ml aqueous methanol is cooled to -2°C and 3.5 ml (5.69 mmol) Oxone® is added. The mixture is stirred for 4 hours at 0°C and a further 1gram (mmol) Oxone® is added and stirring continues for 1.5 hours. A solution of 0.8 gram sodium metabisulfite in 20ml water is added dropwise over 5-10 minutes. After further stirring the resultant precipitate is filtered, washed successively with water and 50% aqueous methanol and dried. Purity is 98.1%.

Example 11
Selective Oxidation By Oxone® of 5-(difluoromemoxy)-2-[[(3,4-dimethyoxy-2-pyridiniyl)methyl] thiol-lH-benzimidazole to form 5-(difluoromethoxyy2-[[(3,4-dimethyoxy-2-pyridiniyl]methvl] sulfinyl]-1H-benzmidazole (Pantoprazole ) 5
A mixture of 3 grams 5-(difluoromethoxy)-2-[[(3,4-dimethyoxy-2-pyridinjyl)methyl]
thio]-lH-benzimidazole, 3 grams NaHCO3 and 20 ml aqueous methanol is cooled to -2°C and
3.5 ml (5.69 mmol) Oxone® is added. The mixture is stirred for 4 hours at 0°C and a further
lgram (mmol) Oxone® is added and stirring continues for 1.5 hours. A solution of 0.8 gram
10 sodium metabisulfite in 20ml water is added dropwise over 5-10 minutes. After further
stirring the resultant precipitate is filtered, washed successively with water and 50% aqueous
methanol and dried. Purity is 98.1%.
15 Example 12
Selective Oxidation By Oxone® of 2-[[[4-(3-methoxv-propoxy)-3-methyl-2-pyridinyl]methyl1 thiol-1H-benzimidazole to form 2-[[[4-(3-methoxv-propoxy)-3-methyl-2-pvridinyl]sulfinyl]-
1H-benzimidazole (Rabeprazole)
20 A mixture of 3 grams 2-[[[4-(3-methoxy-propoxy)-3-methyl-2-pyridinyl]methyl]
thio]-1H-benzimidazole, 3 grams NaHCO3 and 20 ml aqueous methanol is cooled to -2°C and 3.5 ml (5.69 mmol) Oxone® is added. The mixture is stirred for 4 hours at 0°C and a further lgram (mmol) Oxone® is added and stirring continued for 1.5 hours. A solution of 0.8 gram sodium metabisulfite in 20ml water is added dropwise over 5-10 minutes. After further
25 stirring the resultant precipitate is filtered, washed successively with water and 50% aqueous
methanol and dried. Purity is 98.1%.
A number of embodiments of the invention have been described. The present invention is not to be limited in scope by the specific embodiments described herein. It will 30 be understood that various modifications may be made without departing from the spirit and scope of the invention. Various publications are cited herein, the disclosures of which are incorporated by reference in their entireties.

WE CLAIM:
1. A process for preparing a thioester compound of formula A:

(A) wherein R1, R2, and R4 are each selected from the group consisting of hydrogen, substituted or unsubstituted lower alkyl and substituted lower alkoxy; and R3 is selected from the group consisting of hydrogen and substituted or unsubstituted lower alkyl,
said process comprising reacting a thioether compound of formula B:

(B) wherein R1 through R4 are as in formula A with an oxidizing agent to produce selective oxidation of the thioether compound of formula B to form the thioester compound of formula A, wherein the oxidizing agent is tert-butyl hydroperoxide or Oxone®, and if the oxidizing agent is tert-butyl hydroperoxide the molar ratio of tert-butyl hydroperoxide to the compound of formula B is in the range of about 1.15 to about 4.5.


A process as claimed in claim 1, wherein the oxidation is performed at a temperature from about 10°C to about 30°C.
A process as claimed in claim 1, wherein the oxidation is performed for about 2 hours to about 10 hours.
A process as claimed in claim 1, wherein R1 is methyl, R2 is methoxy; R3 is methyl; and R4 is methoxy.
A process as claimed in claim 1, wherein R1 is methyl; R2 is 2-trifluoroethoxy; R3 is hydrogen; and R4 is hydrogen.
A process as claimed in claim 1, wherein R1 s methoxy; R2 is methoxy; R3 is hydrogen; and R4 is difluoromethoxy.
A process as claimed in claim 1, wherein R1 is methyl; R2 is MeOCH2CH2CH2O; R3 is hydrogen; and R4 is hydrogen.
A process as claimed in claim 1, wherein the catalyst is selected from the group consisting of vanadyl bisacetylacetonate, sodium meta-vanadate and vanadium pentoxide.
A process as claimed in claim 1, wherein the oxidizing agent is tert-butyl hydroperoxide, and the molar ratio of tert-butyl hydroperoxide to the compound of formula B is in the range of about 1.15 to about 4.5.
A process as claimed in claim 1, wherein the catalyst is vanadyl bis-acetylacetonate.
A process as claimed in claim 1, wherein the vanadyl bis


acetylacetonate and the compound of formula B is in the molar ratio of about 0.01 to about 0.6.
12. A process as claimed in any of the claims 9-11, wherein the oxidation is performed in an organic solvent.
13. A process as claimed in claim 12, wherein the organic solvent is selected from the group consisting of toluene, lower alkanols and ethyl acetate.
14. A process as claimed in claim 12, wherein the oxidation is performed in an organic solvent in the presence of water.
15. A process as claimed in claim 1, wherein the oxidizing agent is OXONE®.
16. A process as claimed in claim 15, wherein the molar ratio between OXONE® and the compound of formula B is about 1.25-1.6 to about 1.
17. A process as claimed in claim 15, wherein the molar ratio between OXONE® and the compound of formula B is about 1.4-1.6 to about 1.
18. A process as claimed in claim 15, wherein the oxidation is performed in an aqueous organic solvent.
19. A process as claimed in claim 15, wherein the oxidation is performed in the presence of at least one solvent wherein the solvent is selected from the group consisting of acetone, methanol and a mixture thereof.


20. A process as claimed in claim 15, wherein the oxidation is performed in about 5% aqueous methanol.
21. A process as claimed in claim 15, wherein the oxidation is performed in a two-phase system selected from (CH2CI2/H2O) and (ethyl acetate/H2O).
22. A process as claimed in claim 15, wherein the oxidation is performed in the presence of a phase-transfer catalyst.
23. A process as claimed in claim 22, wherein the phase-transfer catalyst is tert-butyl ammonium bromide.
24. Omeprazole substantially free of a sulphone by-product prepared by the process as claimed in any one of claims 1, 4, 9 and 15.
25. Lansoprazole substantially free of a sulphone by-product prepared by the process as claimed in any of the claims 1, 5, 9 and 15.
26. Pantoprazole substantially free of a sulphone by-product prepared by the process as claimed in any one of claims 1, 6, 9 and 15.
27. Rabeprazole substantially free of a sulphone by-product prepared by the process as claimed in any one of claims 1, 7, 9 and 15.
Dated this 24th day of July, 2003.


[RANJNA MEHTA DUTT]
OF REMFRY & SAGAR
ATTORNEY FOR THE APPLICANT[S]

Documents:

726-mumnp-2003-cancelled page(10-05-2006).pdf

726-mumnp-2003-claim(granted)-(10-05-2006).pdf

726-mumnp-2003-claims(24-7-2003).pdf

726-mumnp-2003-claims(granted)-(10-05-2006).doc

726-mumnp-2003-correspondence(03-08-2006).pdf

726-mumnp-2003-correspondence(ipo)-(17-10-2007).pdf

726-mumnp-2003-correspondence(ipo)-(24-12-2007).pdf

726-mumnp-2003-description(complete)-(24-7-2003).pdf

726-mumnp-2003-form 1(10-05-2006).pdf

726-mumnp-2003-form 1(24-07-2003).pdf

726-mumnp-2003-form 18(10-06-2005).pdf

726-mumnp-2003-form 2(24-7-2003).pdf

726-mumnp-2003-form 2(granted)-(10-05-2006).doc

726-mumnp-2003-form 2(granted)-(10-05-2006).pdf

726-mumnp-2003-form 2(title page)-(24-7-2003).pdf

726-mumnp-2003-form 3(06-11-2003).pdf

726-mumnp-2003-form 3(10-05-2006).pdf

726-mumnp-2003-form 3(24-07-2003).pdf

726-mumnp-2003-form 4(10-02-2006).pdf

726-mumnp-2003-form 5(24-07-2003).pdf

726-mumnp-2003-form-pct-ipea-409(24-07-2003).pdf

726-mumnp-2003-form-pct-isa-210(24-07-2003).pdf

726-mumnp-2003-petition under rule 137(10-05-2006).pdf

726-mumnp-2003-power of authority(10-05-2006).pdf

726-mumnp-2003-power of authority(24-07-2003).pdf

726-mumnp-2003-specification(amanded)-(10-5-2006).pdf

726-mumnp-2003-wo international publication report(24-7-2003).pdf


Patent Number 211106
Indian Patent Application Number 726/MUMNP/2003
PG Journal Number 45/2007
Publication Date 09-Nov-2007
Grant Date 17-Oct-2007
Date of Filing 24-Jul-2003
Name of Patentee TEVA PHARMACEUTICALS INDUSTRIES, LTD.
Applicant Address 5 BASEL STREET, P.O. BOX 3190, PETAH TIQVA, 49131, ISRAEL
Inventors:
# Inventor's Name Inventor's Address
1 ILYA AVRUTOV 50 BEERY STREET, P.O. BOX 279, BAT HEFER, ISRAEL 42842
2 MARIOARA MENDELOVICI RECHOV HADAR 6/12, RECHEVOT, ISRAEL 76466,
PCT International Classification Number C07D 401/12
PCT International Application Number PCT/US02/03225
PCT International Filing date 2002-02-04
PCT Conventions:
# PCT Application Number Date of Convention Priority Country
1 60/266,162 2001-02-02 U.S.A.