US20020120150A1 - Process for the preparation of thiazolidinedione derivatives - Google Patents
Process for the preparation of thiazolidinedione derivatives Download PDFInfo
- Publication number
- US20020120150A1 US20020120150A1 US10/082,995 US8299502A US2002120150A1 US 20020120150 A1 US20020120150 A1 US 20020120150A1 US 8299502 A US8299502 A US 8299502A US 2002120150 A1 US2002120150 A1 US 2002120150A1
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- psi
- formula
- process according
- pharmaceutically acceptable
- compound
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 0 [1*]N(C)COC/C=C1\SC(=O)NC1=O.[1*]N(C)COCCC1SC(=O)NC1=O Chemical compound [1*]N(C)COC/C=C1\SC(=O)NC1=O.[1*]N(C)COCCC1SC(=O)NC1=O 0.000 description 5
- URLKBWYHVLBVBO-UHFFFAOYSA-N CC1=CC=C(C)C=C1 Chemical compound CC1=CC=C(C)C=C1 URLKBWYHVLBVBO-UHFFFAOYSA-N 0.000 description 1
- UMLRTZPSKKQOBP-UHFFFAOYSA-N CN([RaH])COCC([Rb])C1(C)SC(=O)NC1=O Chemical compound CN([RaH])COCC([Rb])C1(C)SC(=O)NC1=O UMLRTZPSKKQOBP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D417/00—Heterocyclic compounds containing two or more hetero rings, at least one ring having nitrogen and sulfur atoms as the only ring hetero atoms, not provided for by group C07D415/00
- C07D417/02—Heterocyclic compounds containing two or more hetero rings, at least one ring having nitrogen and sulfur atoms as the only ring hetero atoms, not provided for by group C07D415/00 containing two hetero rings
- C07D417/12—Heterocyclic compounds containing two or more hetero rings, at least one ring having nitrogen and sulfur atoms as the only ring hetero atoms, not provided for by group C07D415/00 containing two hetero rings linked by a chain containing hetero atoms as chain links
Definitions
- This invention relates to a novel process and in particular to a process for preparing certain substituted thiazolidinedione derivatives.
- a a represents a substituted or unsubstituted aromatic heterocyclyl group
- R a represents a hydrogen atom, an alkyl group, an acyl group, an aralkyl group, wherein the aryl moiety may be substituted or unsubstituted, or a substituted or unsubstituted aryl group;
- R b and R c each represent hydrogen or R b and R c together represent a bond
- a b represents a benzene ring having in total up to five substituents
- n′ represents an integer in the range of from 2 to 6.
- EP 0306228 also discloses a process for reducing the compounds of formula (A) wherein R b and R c together represent a bond (the ‘benzylidene thiazolidine-2,4-diones’) to the corresponding compounds of formula (A) wherein R b and R c each represent hydrogen (the ‘benzylthiazolidine-2,4-diones’).
- the particular reduction methods disclosed in EP 0306228 are dissolving metal methods and catalytic hydrogenation methods.
- the present invention provides a process for preparing a compound of formula (I):
- a 1 represents a substituted or unsubstituted aromatic heterocyclyl group
- R 1 represents a hydrogen atom, an alkyl group, an acyl group, an aralkyl group, wherein the aryl moiety may be substituted or unsubstituted, or a substituted or unsubstituted aryl group;
- a 2 represents a benzene ring having in total up to five substituents
- n represents an integer in the range of from 2 to 6
- a 1 , R 1 , A 2 and n are as defined in relation to formula (I), characterised in that the reduction reaction is carried out using a hydrogen pressure above 20 psi, and thereafter, if required, forming a pharmaceutically acceptable salt and/or a pharmaceutically acceptable solvate of the compound of formula (I).
- the reaction is carried out at a pressure in the range of from 50 to 1500 psi, such as 60 to 1500 psi, 75 to 1500 psi, 200 to 1500 psi, 70 to 1000 psi or 200 to 1000 psi, suitably 70 to 1000 psi.
- reaction pressures include 70, 75, 80, 500 and 1000 psi.
- a suitable hydrogenation catalyst is a noble metal catalyst, suitably a palladium catalyst.
- Favoured catalysts are supported noble metal catalysts, such as a palladium-on-carbon catalyst, typically comprising 5% to 10% of palladium.
- a preferred catalyst is a 10% palladium-on-carbon catalyst.
- Catalyst loadings (expressed as w/w% of catalyst to substrate) in the reaction are typically in the range of from 5 to 100%, usually 10 to 50% and preferably 25 to 50%.
- the reaction may be carried out using any suitable solvent such as acetic acid, or an alkanol, such as methanol or ethanol, preferably admixed with an aqueous mineral acid such as hydrochloric acid; or tetrahydrofuran, preferably admixed with an aqueous mineral acid such as hydrochloric acid.
- a suitable solvent such as acetic acid, or an alkanol, such as methanol or ethanol, preferably admixed with an aqueous mineral acid such as hydrochloric acid; or tetrahydrofuran, preferably admixed with an aqueous mineral acid such as hydrochloric acid.
- the solvent is acetic acid or aqueous acetic acid, for example a 4:1 acetic acid:water mixture.
- the reaction is carried out at a temperature which provides a suitable rate of formation of the required product, suitably at an elevated temperature, preferably above 70° C., for example in the range of from 80° C. to 115° C.
- the compounds of formula (I) are isolated from the reaction and subsequently purified by use of conventional isolation and purification methods such as chromatography and crystallization/recrystallization.
- a most preferred value of A 1 is a 2-pyridyl group.
- a most preferred value of A 2 is a moiety of formula:
- a most preferred value of R 1 is a methyl group.
- n is 2.
- a most preferred value of formula (I) is 5- ⁇ 4-[2-(N-methyl-N-(2-pyridyl)amino)ethoxy]benzyl ⁇ -2,4-thiazolidinedione, or a tautomeric form thereof or a salt thereof, or a solvate thereof.
- Crystalline 5- ⁇ 4-[2-(N-methyl-N-(2-pyridyl)amino)ethoxy]benzylidene ⁇ -2,4-thiazolidinedione is isolated from the present reaction and as such forms a further aspect of the present invention.
- a suitable crystallization/recrystallization solvent is acetic acid/denatured ethanol, the crystallization is favourably effected from refluxing, solvent which is allowed to coot to provide the required compound.
- a most preferred value of formula (II) is 5- ⁇ 4-[2-(N-methyl-N-(2-pyridyl)amino)ethoxy]benzylidene ⁇ -2,4-thiazolidinedione or a tautomeric form thereof or a salt thereof, or a solvate thereof.
- Suitable salts are pharmaceutically acceptable salts.
- Suitable pharmaceutically acceptable salts include metal salts, such as for example aluminium, alkali metal salts such as sodium or potassium, alkaline earth metal salts such as calcium or magnesium and ammonium or substituted ammonium salts, for example those with lower alkylamines such as triethylamine, hydroxy alkylamines such as 2-hydroxyethylamine, bis-(2-hydroxyethyl)-amine or tri-(2-hydroxyethyl)-amine, cycloalkylamines such as bicyclohexylamine, or with procaine, dibenzylpiperidine, N-benzyl-b-phenethylamine, dehydroabietylamine, N,N′-bisdehydroabietylamine, glucamine, N-methylglucamine or bases of the pyridine type such as pyridine, collidine or quinoline.
- metal salts such as for example aluminium, alkali metal salts such as sodium or potassium, alkaline earth metal salts such
- salts provided by pharmaceutically acceptable acids including mineral acids, including salts provided by mineral acids, such as hydrobromic, hydrochloric and sulphuric acids, and organic acids, such as methanesulphonic, tartaric and maleic acids, especially tartaric and maleic acid.
- mineral acids such as hydrobromic, hydrochloric and sulphuric acids
- organic acids such as methanesulphonic, tartaric and maleic acids, especially tartaric and maleic acid.
- a preferred salt is a maleate salt.
- Suitable solvates are pharmaceutically acceptable solvates, such as hydrates.
- reaction time (hours.) 1 (75 psi, 50% catalyst) 15-20 2 1000 psi, 50% catalyst ⁇ 2 3 1000 psi, 25% catalyst 7 4 500 psi, 50% catalyst 4 5 500 psi, 25% catalyst ca. 12
Abstract
A process for preparing a compound of formula (I) or a tautomeric form thereof or a pharmaceutically acceptable salt thereof, wherein: A1 represents a substituted or unsubstituted aromatic heterocyclyl group; R1 represents a hydrogen atom, an alkyl group, an acyl group, an aralkyl group, wherein the aryl moiety may be substituted or unsubstituted, or a substituted or unsubstituted aryl group; A2 represents a benzene ring having in total up to five substituents; and n represents an integer in the range of from 2 to 6, which process comprises catalytically reducing a compound of formula (II): wherein A1, R1, A2 and n are as defined in relation to formula (I), characterized in that the reduction reaction is carried out using a hydrogen pressure above 20 psi; and thereafter if required forming a pharmaceutically acceptable salt and/or a pharmaceutically acceptable solvate of the compound of formula (I).
Description
- This invention relates to a novel process and in particular to a process for preparing certain substituted thiazolidinedione derivatives.
-
- or a tautomeric form thereof or a pharmaceutically acceptable salt thereof, or a pharmaceutically acceptable solvate thereof, wherein:
- Aa represents a substituted or unsubstituted aromatic heterocyclyl group;
- Ra represents a hydrogen atom, an alkyl group, an acyl group, an aralkyl group, wherein the aryl moiety may be substituted or unsubstituted, or a substituted or unsubstituted aryl group;
- Rb and Rc each represent hydrogen or Rb and Rc together represent a bond;
- Ab represents a benzene ring having in total up to five substituents; and
- n′ represents an integer in the range of from 2 to 6.
- EP 0306228 also discloses a process for reducing the compounds of formula (A) wherein Rb and Rc together represent a bond (the ‘benzylidene thiazolidine-2,4-diones’) to the corresponding compounds of formula (A) wherein Rb and Rc each represent hydrogen (the ‘benzylthiazolidine-2,4-diones’). The particular reduction methods disclosed in EP 0306228 are dissolving metal methods and catalytic hydrogenation methods.
- It has now been discovered that when the catalytic hydrogenation of the benzylidene thiazolidine-2,4-diones is carried out using an elevated pressure of hydrogen that the reaction can be effected with a surprising reduction in the catalytic loading and reaction time and, most surprisingly, produces a significant reduction in by-product formation.
-
- or a tautomeric form thereof or a pharmaceutically acceptable salt thereof, or a pharmaceutically acceptable solvate thereof, wherein:
- A1 represents a substituted or unsubstituted aromatic heterocyclyl group;
- R1 represents a hydrogen atom, an alkyl group, an acyl group, an aralkyl group, wherein the aryl moiety may be substituted or unsubstituted, or a substituted or unsubstituted aryl group;
- A2 represents a benzene ring having in total up to five substituents; and
- n represents an integer in the range of from 2 to 6,
-
- wherein A1, R1, A2 and n are as defined in relation to formula (I), characterised in that the reduction reaction is carried out using a hydrogen pressure above 20 psi, and thereafter, if required, forming a pharmaceutically acceptable salt and/or a pharmaceutically acceptable solvate of the compound of formula (I).
- Suitably the reaction is carried out at a pressure in the range of from 50 to 1500 psi, such as 60 to 1500 psi, 75 to 1500 psi, 200 to 1500 psi, 70 to 1000 psi or 200 to 1000 psi, suitably 70 to 1000 psi.
- Examples of reaction pressures include 70, 75, 80, 500 and 1000 psi.
- A suitable hydrogenation catalyst is a noble metal catalyst, suitably a palladium catalyst.
- Favoured catalysts are supported noble metal catalysts, such as a palladium-on-carbon catalyst, typically comprising 5% to 10% of palladium.
- A preferred catalyst is a 10% palladium-on-carbon catalyst.
- Catalyst loadings (expressed as w/w% of catalyst to substrate) in the reaction are typically in the range of from 5 to 100%, usually 10 to 50% and preferably 25 to 50%.
- The reaction may be carried out using any suitable solvent such as acetic acid, or an alkanol, such as methanol or ethanol, preferably admixed with an aqueous mineral acid such as hydrochloric acid; or tetrahydrofuran, preferably admixed with an aqueous mineral acid such as hydrochloric acid. Preferably the solvent is acetic acid or aqueous acetic acid, for example a 4:1 acetic acid:water mixture.
- The reaction is carried out at a temperature which provides a suitable rate of formation of the required product, suitably at an elevated temperature, preferably above 70° C., for example in the range of from 80° C. to 115° C.
- The compounds of formula (I) are isolated from the reaction and subsequently purified by use of conventional isolation and purification methods such as chromatography and crystallization/recrystallization.
- The suitable, apt, favoured and preferred values of the variables A1, A2, R1 and n in formulae (I) and (II) are as defined in relation to formula (I) of EP 0306228.
- A most preferred value of A1 is a 2-pyridyl group.
-
- A most preferred value of R1 is a methyl group.
- A most preferred value of n is 2.
- A most preferred value of formula (I) is 5-{4-[2-(N-methyl-N-(2-pyridyl)amino)ethoxy]benzyl}-2,4-thiazolidinedione, or a tautomeric form thereof or a salt thereof, or a solvate thereof.
- Crystalline 5-{4-[2-(N-methyl-N-(2-pyridyl)amino)ethoxy]benzylidene}-2,4-thiazolidinedione is isolated from the present reaction and as such forms a further aspect of the present invention. A suitable crystallization/recrystallization solvent is acetic acid/denatured ethanol, the crystallization is favourably effected from refluxing, solvent which is allowed to coot to provide the required compound.
- A most preferred value of formula (II) is 5-{4-[2-(N-methyl-N-(2-pyridyl)amino)ethoxy]benzylidene}-2,4-thiazolidinedione or a tautomeric form thereof or a salt thereof, or a solvate thereof.
- Suitable salts are pharmaceutically acceptable salts.
- Suitable pharmaceutically acceptable salts include metal salts, such as for example aluminium, alkali metal salts such as sodium or potassium, alkaline earth metal salts such as calcium or magnesium and ammonium or substituted ammonium salts, for example those with lower alkylamines such as triethylamine, hydroxy alkylamines such as 2-hydroxyethylamine, bis-(2-hydroxyethyl)-amine or tri-(2-hydroxyethyl)-amine, cycloalkylamines such as bicyclohexylamine, or with procaine, dibenzylpiperidine, N-benzyl-b-phenethylamine, dehydroabietylamine, N,N′-bisdehydroabietylamine, glucamine, N-methylglucamine or bases of the pyridine type such as pyridine, collidine or quinoline.
- In addition should be mentioned those pharmaceutically acceptable salts provided by pharmaceutically acceptable acids including mineral acids, including salts provided by mineral acids, such as hydrobromic, hydrochloric and sulphuric acids, and organic acids, such as methanesulphonic, tartaric and maleic acids, especially tartaric and maleic acid. A preferred salt is a maleate salt.
- Suitable solvates are pharmaceutically acceptable solvates, such as hydrates.
- The compounds of formula (II) are prepared according to known methods, for example by use of the appropriate method disclosed in EP 0306228. The contents of EP 0306228 are incorporated herein by reference.
- The following example illustrates the invention but does not limit it in any way.
- To a solution of (Z)-5-{[4-[2-(N-methyl-N-(2-pyridyl)amino)ethoxy]benzylidene}2,4-thiazolidinedione (123 kg) in glacial acetic acid (1232 L) is added 10% palladium on charcoal (Johnson-Matthey type 87L, 123 kg, catalyst contains ˜50% w/w water and hence the catalyst loading was 50% w/w). The resulting mixture is hydrogenated at 70-80 p.s.i. hydrogen pressure at about 95° C. After the starting material is consumed (15-20 hours), the reaction mixture is cooled to about 65° C. and the catalyst is removed by filtration. The resulting solution is concentrated under reduced pressure to low volume and the residue is dissolved in denatured ethanol (1000 L) at 60° C. The solution is heated to reflux and then cooled to ambient temperature to effect recrystallisation. The product, 5-{[4-[2-(N-methyl-N-(2-pyridyl)amino)ethoxy]benzyl}-2,4-thiazolidinedione, is isolated by filtration, and dried in vacuo at 45° C. Typical yields are 70-80%.
- Effect of Change of Reaction Pressure
- The above reaction can be preformed over a range of pressures resulting in a significant reduction in reaction time and catalyst loading, as shown below.
Reaction number Conditions Reaction Time (hours.) 1 (75 psi, 50% catalyst) 15-20 2 1000 psi, 50% catalyst <2 3 1000 psi, 25% catalyst 7 4 500 psi, 50% catalyst 4 5 500 psi, 25% catalyst ca. 12
Claims (10)
1. A process for preparing a compound of formula (I):
or a tautomeric form thereof or a pharmaceutically acceptable salt thereof, or a pharmaceutically acceptable solvate thereof, wherein:
A1 represents a substituted or unsubstituted aromatic heterocyclyl group;
R1 represents a hydrogen atom, an alkyl group, an acyl group, an aralkyl group, wherein the aryl moiety may be substituted or unsubstituted, or a substituted or unsubstituted aryl group;
A2 represents a benzene ring having in total up to five substituents; and
n represents an integer in the range of from 2 to 6,
which process comprises catalytically reducing a compound of formula (II):
wherein A1, R1, A2 and n are as defined in relation to formula (1), characterised in that the reduction reaction is carried out using a hydrogen pressure above 20 psi; and thereafter if required forming a pharmaceutically acceptable salt and/or a pharmaceutically acceptable solvate of the compound of formula (I).
2. A process according to claim 1 , wherein the reaction is carried out using a hydrogen pressure in the range of from 50 to 1500 psi, 60 to 1500 psi, 75 to 1500 psi, 70 to 1000 psi or 200 to 1500 psi.
3. A process according to claim 1 or claim 2 , wherein the reaction hydrogen pressure is in the range of from 70 to 1000 psi.
4. A process according to any one of claims 1 to 3 , wherein the reaction hydrogen pressure is 70, 75, 80, 500 or 1000 psi.
5. A process according to any one of claims 1 to 4 , wherein the hydrogenation catalyst is a 10% palladium-on-carbon catalyst.
6. A process according to any one of claims 1 to 5 , wherein the catalyst loading is 5 to 100%, (% w/w of catalyst to substrate).
7. A process according to any one of claims 1 to 6 , wherein the reaction solvent is acetic acid, aqueous acetic acid, an alkanol, an alkanol admixed with an aqueous mineral acid, tetrahydrofuran or tetrahydrofuran admixed with an aqueous mineral.
8. A process according to claim 7 , wherein the reaction solvent is acetic acid.
9. A process according to any one of claims 1 to 8 , wherein the reaction temperature is in the range of from 80° C. to 115° C.
10. A process according to any one of claims 1 to 9 , wherein the compound of formula (II) is 5-{4-[2-(N-methyl-N-(2-pyridyl)amino)ethoxy]benzylidene}-2,4-thiazolidinedione, or a tautomeric form thereof or a salt thereof, or a solvate thereof, and the compound of formula (I) is 5-{4-[2-(N-methyl-N-(2-pyridyl)amino)ethoxy]benzyl}-2,4-thiazolidinedione, or a tautomeric form thereof or a salt thereof, or a solvate thereof.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/288,072 US7091359B2 (en) | 1997-11-04 | 1998-10-27 | Process for the preparation of thiazolidinedione derivatives |
US10/082,995 US20020120150A1 (en) | 1997-11-04 | 2002-02-26 | Process for the preparation of thiazolidinedione derivatives |
US11/326,003 US20060106221A1 (en) | 1997-11-04 | 2006-01-05 | Process for the preparation of thiazolidinedione derivatives |
US11/550,506 US7351832B2 (en) | 1997-11-04 | 2006-10-18 | Process for the preparation of thiazolidinedione derivatives |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB9723295.3 | 1997-11-04 | ||
GBGB9723295.3A GB9723295D0 (en) | 1997-11-04 | 1997-11-04 | Novel process |
US53088800A | 2000-07-10 | 2000-07-10 | |
US10/082,995 US20020120150A1 (en) | 1997-11-04 | 2002-02-26 | Process for the preparation of thiazolidinedione derivatives |
Related Parent Applications (3)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US09530888 Continuation | 1998-10-27 | ||
PCT/EP1998/006997 Continuation WO1999023095A1 (en) | 1997-11-04 | 1998-10-27 | Process for the preparation of thiazolidinedione derivatives |
US53088800A Continuation | 1997-11-04 | 2000-07-10 |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US28807202A Continuation | 1997-11-04 | 2002-11-04 |
Publications (1)
Publication Number | Publication Date |
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US20020120150A1 true US20020120150A1 (en) | 2002-08-29 |
Family
ID=26312544
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10/288,072 Expired - Fee Related US7091359B2 (en) | 1997-11-04 | 1998-10-27 | Process for the preparation of thiazolidinedione derivatives |
US10/082,995 Abandoned US20020120150A1 (en) | 1997-11-04 | 2002-02-26 | Process for the preparation of thiazolidinedione derivatives |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
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US10/288,072 Expired - Fee Related US7091359B2 (en) | 1997-11-04 | 1998-10-27 | Process for the preparation of thiazolidinedione derivatives |
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US (2) | US7091359B2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20050080114A1 (en) * | 1999-04-23 | 2005-04-14 | Smithkline Beecham Plc | Polymorph of 5-[4-[2-(N-methyl-N-(2-pyridyl)amino)ethoxy]benzyl]thiazolidine-2, 4-dione, maleic acid salt |
US20090093806A1 (en) * | 2007-10-08 | 2009-04-09 | Assaf Govari | Catheter with pressure sensing |
EP3381363A1 (en) | 2004-03-05 | 2018-10-03 | Biosense Webster, Inc. | Positioning sensing system for orthopaedic applications |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB9723295D0 (en) * | 1997-11-04 | 1998-01-07 | Smithkline Beecham Plc | Novel process |
US7435741B2 (en) * | 2006-05-09 | 2008-10-14 | Teva Pharmaceutical Industries, Ltd. | 2-N{5-[[4-[2-(methyl-2-pyridinylamino) ethoxy] phenyl]methyl]-2,4-thiazolidinedione} butanedioic acid, methods of preparation and compositions with rosiglitazone maleate |
Family Cites Families (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5522636A (en) | 1978-08-04 | 1980-02-18 | Takeda Chem Ind Ltd | Thiazoliding derivative |
CN1003445B (en) * | 1984-10-03 | 1989-03-01 | 武田药品工业株式会社 | The preparation method of thiazolidine diketone derivative |
US4812570A (en) | 1986-07-24 | 1989-03-14 | Takeda Chemical Industries, Ltd. | Method for producing thiazolidinedione derivatives |
EP0842925A1 (en) | 1987-09-04 | 1998-05-20 | Beecham Group Plc | Substituted thiazolidinedione derivatives |
US5260445A (en) | 1987-09-04 | 1993-11-09 | Beecham Group P.L.C. | 2,4-thiazolidinediones |
US5232925A (en) | 1987-09-04 | 1993-08-03 | Beecham Group P.L.C. | Compounds |
US6288095B1 (en) | 1987-09-04 | 2001-09-11 | Beecham Group P.L.C. | Compounds |
US5521201A (en) | 1987-09-04 | 1996-05-28 | Beecham Group P.L.C. | Method for treatment of atherosclerosis |
US5194443A (en) | 1987-09-04 | 1993-03-16 | Beecham Group P.L.C. | Compounds |
US20020049240A1 (en) | 1994-12-19 | 2002-04-25 | Beecham Group P.1.C. | Novel compounds |
GB9023585D0 (en) | 1990-10-30 | 1990-12-12 | Beecham Group Plc | Novel compounds |
GB9023583D0 (en) | 1990-10-30 | 1990-12-12 | Beecham Group Plc | Novel compounds |
GB9124513D0 (en) | 1991-11-19 | 1992-01-08 | Smithkline Beecham Plc | Novel process |
US6462337B1 (en) | 2000-04-20 | 2002-10-08 | Agilent Technologies, Inc. | Mass spectrometer electrospray ionization |
WO1993013095A1 (en) | 1991-12-20 | 1993-07-08 | The Upjohn Company | A reduction method for substituted 5-methylene-thiazolidinediones |
US5741803A (en) | 1992-09-05 | 1998-04-21 | Smithkline Beecham Plc | Substituted thiazolidinedionle derivatives |
GB9218830D0 (en) | 1992-09-05 | 1992-10-21 | Smithkline Beecham Plc | Novel compounds |
UY24886A1 (en) | 1997-02-18 | 2001-08-27 | Smithkline Beecham Plc | TIAZOLIDINDIONA |
US6632947B2 (en) * | 1997-02-18 | 2003-10-14 | Smithkline Beecham Plc | Process for the preparation of substituted thiazolidinedione |
GB9723295D0 (en) | 1997-11-04 | 1998-01-07 | Smithkline Beecham Plc | Novel process |
-
1998
- 1998-10-27 US US10/288,072 patent/US7091359B2/en not_active Expired - Fee Related
-
2002
- 2002-02-26 US US10/082,995 patent/US20020120150A1/en not_active Abandoned
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20050080114A1 (en) * | 1999-04-23 | 2005-04-14 | Smithkline Beecham Plc | Polymorph of 5-[4-[2-(N-methyl-N-(2-pyridyl)amino)ethoxy]benzyl]thiazolidine-2, 4-dione, maleic acid salt |
EP3381363A1 (en) | 2004-03-05 | 2018-10-03 | Biosense Webster, Inc. | Positioning sensing system for orthopaedic applications |
US20090093806A1 (en) * | 2007-10-08 | 2009-04-09 | Assaf Govari | Catheter with pressure sensing |
Also Published As
Publication number | Publication date |
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US20030092742A1 (en) | 2003-05-15 |
US7091359B2 (en) | 2006-08-15 |
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Owner name: SMITHLINE BEECHAM P.L.C., UNITED KINGDOM Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:GILES, ROBERT GORDON;LEWIS, NORMAN JOHN;QUICK, JOHN KIRBY;REEL/FRAME:016000/0638;SIGNING DATES FROM 20000420 TO 20000427 |