BENZENEDIMETHANOL SUITABLE FOR MICRONISATION

Abstract: 1-Hydroxy-2-naphthalene carboxylate (hydroxynaphthoate) salt of 4-hydroxy-a<1>-[[[6-(4-phenylbutoxy)hexyl]amino]methyl]-1,3-benzenedim ethanol in the form of spherical accretions of microcrystals, the spherical accretions being free-flowing, friable and micronisable and preferably having a mean particle size from 70 to 300 mm and a mean surface area from 4 to 12 m<2>g-<1>. The hydroxynaphthoate salt (in the claimed form) may be prepared by quenching a hot organic/aqueous organic solution containing the salt with a cold organic/aqueous organic solvent.

Description: BENZENEDIMETHANOL SUITABLE FOR MICRONISATION . The present invention relates to a drug material suitable for micronisation. In particular, the invention relates to a novel readily micronisable form of the 1- hydroxy-2-naphthalenecarboxylate (hereinafter hydroxy naphthoate) salt of 4- hydroxy-α -[[[6-(4-phenylbutoxy)hexyl]amino]methyl]-l,3-benzenedimethancl (hereinafter compound A) and to processes for the preparation of this novel form. United Kingdom Patent Specification No. 2140800A (GB2140800A) relates to phenethanolamine derivatives having a selective stimulant action at beta-2 adrenoreceptors. The compounds may be used inter alia in the treatment oϊ respiratory diseases associated with reversible airways obstruction, such as asthma and chronic bronchitis. In particular, GB2140800A describes compound A and its physiologically acceptable salts, especially (at Example 20) its hydroxy naphthoate salt. Compound A and its hydroxy naphthoate salt have been found to be particularly advantageous in the treatment of such respiratory diseases. When treating patients suffering from respiratory conditions, it has been founα most convenient to deliver the appropriate beta-2 stimulant directly to the site o; action, either by inhalation or insufflation. In order to administer a drug via these routes, it is first necessary to provide the active ingredient as a fine powder having an appropriate particle size range. Material meeting the required particle size specification is generally obtained by micronisation of the drug substance, using, for example, a mill, such as a fluid-energy mill. The present inventors have found that when the hydroxy naphthoate salt of compound A is prepared as described in GB2140800A, Example 20, crystals are obtained that are extremely difficult to micronise to the required particle size range. These crystals are seen to adhere to the feed system (in the fluid energy mill) causing accumulation and ultimately blockage. This accumulation and blockage (of crystals) prevents efficient micronisation. SUBSTITUTE SHEET It is an object of the present invention to provide a novel, readily micronisable form of the hydroxy naphthoate salt of compound A that overcomes the disadvantage (in terms of micronisation) associated with the specific crystalline form described above. According to the present invention, there is provided the hydroxy naphthoate salt of compound A in the form of spherical accretions of microcrystals, the spherical accretions being free-flowing, friable and micronisable. The present inventors have surprisingly found that the presently claimed form of the hydroxy naphthoate salt of compound A, a form that combines a novel, spherical shape, and a free-flowing and friable nature, is readily micronisable to a material suitable for use in dosage forms that are administered by inhalation or insufflation. The present invention provides the hydroxy naphthoate salt of compound A in the form of spherical accretions of microcrystals. This form consists of thin crystalline plates arranged radially about a central core or void. The form has an open structure in which the polymorphic form of the compound A hydroxy naphthoate is the same as that obtained from Example 20 of GB2140800A. The form provided by the present inventors also encompasses two or more spherical accretions (of microcrystals) fused together. In the present specification, the term "spherical" refers both to sphere shaped and spherelike (i.e. spheroidal) shaped forms. Spherelike forms would include elliptical (egg shaped) and distorted elliptical (pear shaped) forms. The present novel form of the compound A hydroxy naphthoate must be free- flowing. This means that the form must flow freely into a powder mill, for example a fluid energy powder mill, to allow its efficient particle size reduction by micronisation on an industrial scale. The physical characteristics of a material that determine its flow characteristics include its bulk density, cohesivity, particle size and shape and uniformity with respect to the particle size. Ideally, a material, in order to be free flowing, will have a high bulk density, a low cohesivity, and a uniform particle size distribution. To meet this ideal, the individual particles within the material should also be spherical in shape. The SϋB sτ i τότ s H ^ present novel form meets these criteria. Employing methods of measurement based upon those described by R.L.Carr in Chemical Engineering, 1965, 163-168 the present novel form exhibits a high aerated bulk density, preferably from 0.2 to 0.5gml , especially from 0.3 to 0.4gml , a low cohesivity, preferably from 0 to 20%, especially from 0 to 5%, a spherical (or near spherical) particle shape and a uniform particle size distribution, as measured by a uniformity coefficient of from 1 to 20, preferably of from 1 to 5, typically about 3. The present novel form of the compound A hydroxy naphthoate must be friable. This means that the form must be easily broken down to particles of a size suitable for use in a pharmaceutical dosage form to be delivered by inhalation or insufflation. The present novel form of the compound A hydroxy naphthoate must be micronisable. This means that the form must be easily broken down under micronising conditions, for example in a fluid-energy mill, to particles of a size suitable for use in a pharmaceutical dosage form to be delivered by inhalation or insufflation. The present novel form of the compound A hydroxy naphthoate preferably has a mean particle size of from 70 to 300μm, most preferably from 100 to 200 ^rn, when measured by a laser diffraction method, T. Allen in Particle Size Measurement, 1981, 3rd Edition. The particle size distribution (measured by sieve analysis) is within the range 10 to 2000 μm, preferably from 100 to lOOOμm. For a discussion of sieve analysis, see the above Allen reference. The present novel form of the compound A hydroxy naphthoate preferably has a mean surface area of from 4 to 12m 9 g 1 , most preferably from 6 to 10m 9 g 1 , when measured by the nitrogen adsorption method of Brunnauer, E mett and Teller (BET), S. Lowell and J.E. Shields, Powder Surface Area and Porosity, 1984, 2nd Edition. Conventional wisdom in the powder milling art suggests that, for optimum flow properties, a material should consist of large particles having a low surface area. The present inventors have surprisingly found that, in the case of the preferred form of the compound A hydroxy naphthoate, a novel form that consists of l r^e SUBSTITUTE SHEET particles having a high surface area flows far more freely than a known form (GB2140800A, Example 20) that consists of large particles having a low surface area. This finding contradicts the conventional wisdom. A skilled man seeking to overcome the flow difficulties associated with the compound A hydroxy naphthoate would not have expected to produce a material having the novel form's preferred particle size/surface area properties. Other favourable physical properties exhibited by the present novel form of the compound A hydroxy naphthoate are a low compressibility and a relatively low angle of repose. These terms are defined and their means of measurement are described by R.L.Carr in Chemical Engineering, 1965, 163-168. Preferably the present novel form has an angle of repose of from 25-50°, especially from 40-50°, and a compressibility of from 5 to 25%, especially 8 to 20%. The provision of the present novel form of the compound A hydroxy naphthoate allows its efficient micronisation on an industrial scale. According to a further aspect of the present invention therefore, there is provided a process for the micronisation of the hydroxy naphthoate salt of compound A comprising feeding the hydroxy naphthoate salt of compound A in the form of spherical accretions of microcrystals, the spherical accretions being free-flowing, friable and micronisable into a microniser, micronising the hydroxy naphthoate salt to give a micronised material and collecting the micronised material. Preferably the present novel form of the compound A hydroxy naphthoate iε micronised until the collected material has a particle size range that is suitable for pharmaceutical dosage forms to be delivered by inhalation or insufflation. A suitable particle size range for this use is from 1 to 10 um, preferably from 1 to 5j_.m. The present novel form of the compound A hydroxy naphthoate may be prepared by any suitable method. In a still further aspect of the present invention, however, there is provided a process for the preparation of the hydroxy naphthoate salt of compound A in the form of spherical accretions of microcrystals, the spherical accretions being free-flowing, friable and micronisable said process comprising quenching an organic or aqueous organic solution of the hydroxy naphthoate salt of compound A with an organic or aqueous organic solvent having a lower temperature than the said solution, to give spherical accretions of microcrystals of the hydroxy naphthoate salt of compound A (the product) and collecting the product For brevity, the organic or aqueous organic solution will hereinafter be described as "hot" and the organic or aqueous organic solvent having a lower temperature will hereinafter be described as "cold", these are to be understood as relative and not absolute terms. The production of large spherical shaped, crystalline material from the above crystallisation is extremely unusual and unexpected. The crystallisation, once initiated, is relatively fast. Such "fast" crystallisations usually lead to the production of a fine material having a small particle size. In the above process, an "aqueous organic" solution or solvent contains up tc about 10%(v/v) water. Preferably, a hot organic solution and a cold organic solvent are employed in the above process. Preferably, the organic solvent employed in the hot organic or hot aqueous organic solution has a boiling point (at 760mmHg) from 40° to 150°C, especially from 60° to 120°C. The compound A hydroxy naphthoate should be sparingly soluble or insoluble in the solvent when cold and soluble in the solvent when hot. Solvents suitable for use in the hot organic or hot aqueous organic solution include lower alkyl (C j .4) alcohols such as methanol, ethanol and isopropanol, lower alkyl (C j _4) ethers, such as methyl t-butylether, and lower alkyl (C- j ,^) esters, such as ethyl acetate. In a particularly preferred embodiment of the present process, the organic solvent employed in the hot organic or hot aqueous organic solution is a lower alkyl alcohol, especially methanol, ethanol or isopropanol, most especially methanol. In all of the above cases, the hot organic or the hot aqueous organic solution may contain a single solvent or a mixture of solvents. The organic solvent employed in the cold organic or cold aqueous organic solvent should be miscible with the organic solvent employed in the hot organic or hot aqueous organic solution. Preferably it has a freezing point from -150° to -20°C, especially from -130° to -50°C. The compound A hydroxy naphthoate UTE SHEET should be sparingly soluble or insoluble in the solvent when cold. Solvents suitable for use in the cold organic or cold aqueous organic solvent include lower alkyl (C j _4) alcohols, such as methanol, ethanol and isopropanol, lower alkyl (C j _^) ethers, such as methyl t-butyl ether, and lower alkyl (C-^_ A ) esters, such as ethyl acetate. In a particularly preferred embodiment of the present process, the organic solvent employed in the cold organic or cold aqueous organic solvent is a lower alkyl alcohol, especially methanol, ethanol or isopropanol, most especially isopropanol. In all of the above cases, the cold organic or the cold aqueous organic solvent may contain a single solvent or a mixture of solvents. The temperature of the "hot" solution and the "cold" solvent are chosen to effect a fast crystallisation of the compound A hydroxy naphthoate, such that spherical accretions of microcrystals are formed. The temperatures employed will depend, in large measure, on the choice of solvent or solvents. Conveniently, the temperature of the hot organic or the hot aqueous organic solution is from 30 to 80°C, especially from 40° to 70°C. Also conveniently, the temperature of the cold organic or the cold aqueous organic solvent is form -35° to 15°C, especially from -25° to lO°C. The hot organic or hot aqueous organic solution may be quenched either by addition to or by the addition of the cold organic or cold aqueous organic solvent. Preferably the hot organic or the hot aqueous organic solution is added to the cold organic or the cold aqueous organic solvent. During this quenching process, it is preferable to maintain the temperature of the mixture ("hot" solution and "cold" solvent) at a temperature below about 20°C, especially from -10° to 20°C, most especially from 0° to 20°C. The mixture is maintained at a temperature within this range until all (or most of) the compound A hydroxy naphthoate has crystallised as spherical accretions of microcrystals. This crystallisation process can take, for example, from 10 to 120min, in particular from 20 to 90min. The hydroxy naphthoate salt of compound A may be dissolved as such in the hot organic or the hot aqueous organic solution. Alternatively, the salt may be formed in situ by separately dissolving compound A and l-hydroxy-2-ι.-.phthcic acid in the "hot" solution. The starting material (compound A or the hydroxy naphthoate salt of compound A) for use in the above process may be prepared by the methods described in GB2140800A. Once formed by the present process the spherical accretions of microcrystals may be collected by any suitable process, for example by filtration. The contents of the references mentioned above, that is GB 2140800A; R L Carr, Chemical Engineering, 1965, 163-168; T Allen, Particle Size Measurement, 1981, 3rd Edition. SXowell and J E Shields, Powder Surface Area and Porosity, 1984, 2nd Edition, are hereby incorporated by way of reference. The present novel form of the hydroxy naphthoate salt of compound A, processes for its preparation and processes for its micronisation will now be described by way of example only. In the Figures, Figure 1 is a scanning electron micrograph of the known crystalline form of the hydroxy naphthoate salt of compound A obtained by following the comparative Example set out below, and Figure 2 is a scanning electron micrograph of the claimed form of the hydroxy naphthoate salt of compound A obtained by following Example 8 set out below. This figure also has an inset showing, in close up, the surface of a spherical accretion obtained by the process described in Example 8. (A) Preparation of the Hydroxynaphthoate Salt of Compound A Comparative Example 4-Hydroxy-α -[[[6-(4-phenylbutoxy)hexyl]amino]methyl]-l,3-benzenedimethanol (compound A) was dissolved in hot (>60°) isopropanol. A solution of 1 -hydro y-2- naphthoic acid (1 equiv.) in hot (70°C) isopropanol was added. The mixture wa.; seeded, allowed to cool to 40°C (ca. 2hr) and then further cooled to 5°C (ca. 2hr). The solid product was isolated by filtration, washed with cold isopropanol and dried in vacuo. The product obtained gave the scanning electron micrograph set out in Figure 1. SUBSTITUTE SHEET Example 1 Cold (ca. -15°C) isopropanol was added rapidly to a solution of the hydroxy naphthoate salt of compound A in hot (ca. 65°C) isopropanol. The resulting suspension was allowed to stand at ca. 5^C for lhr and the product was then collected by filtration, washed with cold isopropanol and dried in vacuo at 50°C. Example 2 Cold (ca. -15°C) isopropanol was added rapidly to a solution of the hydroxy naphthoate salt of compound A in hot (ca. 40°C) methanol. The resulting suspension was allowed to stand at ca. 5°C for lhr and the product was then collected by filtration, washed with cold isopropanol and dried in vacuo at 50°C. Example 3 Compound A (4.63kg) and l-hydroxy-2-naphthoic acid (2.10kg) were dissolved in hot (ca. 60°C) methanol. The solution was added to cold (ca. 5^C isopropanol. During the addition the temperature of the "mixed" solution was allowed to increase until it reached 15°C, whereupon the mixture was maintained at 15°C (±2°C) for 30min., after which the product was isolated by filtration, washed with cold isopropanol and dried in vacuo at 40°C. Example 4 A mixture of compound A (12.4kg) and l-hydroxy-2-naphthoic acid (5.6kg) in hot (57° + 3°C) methanol was added to cold (below 15°C) isopropanol (optionally containing up to 6% (v/v) water). During the addition the temperature of the mixture did not rise above 15-20°C. The resulting suspension was stirred at about 20°C for about 1 hr. The solid was then collected by filtration, washed with cold isopropanol and dried in vacuo at about 40 C. Example 5 B A solution of the hydroxy naphthoate salt of compound A in hot (ca. 70°C) isopropanol (9.5vol) was added over an 8 min. period to cold (5-10°C) t-butyl methyl ether (25vol.) with stirring under nitrogen. After 30min. (at ca. 5^C) the solid material was isolated by filtration, washed with cold isopropanol and dried. The product obtained had a melting point of 121.5- 137.5°C. Example 6 The hydroxy naphthoate salt of compound A was dissolved in hot (75°C) isopropanol (9.5vol.) under nitrogen and the solution was allowed to cool slowly with stirring to 57°C. Cold (-30°C) isopropanol (14vol.) was added to give a mixture the temperature of which was ca. 17°C. After about 4hr. the solid product was filtered, washed with cold isopropanol and dried in vacuo. Example 7 A hot (ca. 60°C) solution of compound A and l-hydroxy-2-naphthoic acid (1 equiv.) in methanol (5.8vol.) was added during ca. 1 min. to cold (-10°C) isopropanol (11.6vol.) with stirring and the mixture was stirred at 0-5°C for 1.5hr. The solid product was collected by filtration, washed with cold isopropanol and dried h vacuo. Example 8 A hot (60°C) solution of compound A and l-hydroxy-2-naphthoic acid (1 equiv). in methanol (5.6vol). was added during ca. 0.5h to cold isopropanol. Throughout the mixing process, the temperature of the mixture was maintained in the range 12 - 17°C. The mixture was stirred for lhr. at 15°C and the solid product was then collected by filtration. The filter cake was washed with cold isopropanol and dried in vacuo at 40°C. The product obtained gave the scanning electron micrograph set out in Figure 2. The microcrystalline nature of this novel form can be seen from the inset of Figure 2 which shows in close up, the surface of one of the spherical accretions obtained. SUBSTITUTE SHEET (B) Physical Properties of Two Forms of the Hydroxynaphthoate Salt of Compound A The table set out below compares the physical properties of the known form of the hydroxy naphthoate salt (as prepared in the above comparative example) with the same properties of the present novel form of the hydroxy naphthoate salt (as prepared by the process described in Example 8). TABLE Mean Surface Area (πr'gm- 1 1 ) 1.9 9.6 (BET analysis) (c) Micronisation of Two Forms of the Hydroxynaphthoate Salt of Compound A Micronisation takes place in a fluid energy microniser of known type. Suitable examples are described and illustrated in Remington's Pharmaceutical Sciences, 1985, 17th Edition, at p. 1588, the contents of which disclosure are hereby incorporated by way of reference. During micronisation, raw drug passes through a hopper and is carried through a venturi by a jet of air into a cyclone where the shearing action of air jets and collisions of drug particles break up the crystals. Micronised drug falls from the cyclone into a container; "fines" leave in the exhaust and are trapped in large "vacuum cleaner" bags. EET (i) Micronisation of Comparative Example Material During the micronisation of this material, a waxy deposit of drug built up on the wall of the venturi bringing the process to a halt after only a few minutes. (ii) Micronisation of Example 6 Material During the micronisation of this material, it flowed smoothly from the hopper, through the venturi and into the cyclone. No waxy material adhered to the venturi in a running time of ca. 20 min. SUBSTITUTE SHEET

Claims: CLAIMS 1. l-Hydroxy-2-naphthaIenecarboxylate (hydroxynaphthoate) salt of 4-hydroxy- « -[[[6-(4-phenylbutoxy)hexyl]amino]methyl]-l,3-benzenedimethanol in the form of spherical accretions of microcrystals, the spherical accretions being free-flowing, friable and micronisable. 2. Hydroxynaphthoate salt according to claim 1 characterised in that the spherical accretions of microcrystals have a mean particle size (as hereinbefore defined) from 70 to 300 μm, especially from 100 to 200 μm. 3. Hydroxynaphthoate salt according to either claim 1 or claim 2 characterised in that the spherical accretions of microcrystals have a mean surface area (as hereinbefore defined) from 4 to 12m 2 g , especially from 6 to 10m 2 g . 4. Hydroxynaphthoate salt according to any one of claims 1 to 3 characterised in that the spherical accretions of microcrystals have a particle size distribution (as hereinbefore defined) from 100 to 1000 μm. 5. Hydroxynaphthoate salt according to any one of claims 1 to 4 characterised in that the spherical accretions of microcrystals have an aerated bulk density (as hereinbefore defined) from 0.2 to 0.5gmι " , especially from 0.3 to 0.4gml " . 6. Hydroxynaphthoate salt according to any one of claims 1 to 5 characterised in that the spherical accretions of microcrystals have a cohesivity (as hereinbefore defined) from 0 to 20%, especially from 0 to 5%. SUBSTITUTE SHEET 7. Hydroxynaphthoate salt according to any one of claims 1 to 6 characterised in that the spherical accretions of microcrystals have a uniformity coefficient (as hereinbefore defined) from 1 to 5, especially about 3. 8. Hydroxynaphthoate salt according to any one of claims 1 to 7 characterised in that the spherical accretions of microcrystals have an angle of repose (as hereinbefore defined) from 25 to 50°, especially 40 to 50°. 9. Hydroxynaphthoate salt according to any one of claims 1 to 8 characterised in that the spherical accretions of microcrystals have a compressibility (as hereinbefore defined) from 5 to 25%, especially 8 to 20%. 10. Hydroxynaphthoate salt according to any one of claims 1 to 9 characterised in that the spherical accretions of microcrystals each comprise thin crystalline plates arranged radially about a central core or void. 11. A process for the micronisation of the l-hydroxy-2-naphthalenecarboxylate (hydroxynaphthoate) salt of 4- h y drox y - a - [ [ [6- (4- phenylbutoxy)hexyl]amino]methyl]-l,3-benzenedimethanol comprising feeding the hydroxynaphthoate salt of 4 - h y d r o x y - a - [ [ [ 6 - ( 4 - phenylbutoxy)hexyl]amino]methyl]-l,3-benzenedimethanol in the form of spherical accretions of microcrystals, the spherical accretions being free-flowing, friable and micronisable, into a microniser, micronising the hydroxynaphthoate salt to give a micronised material and collecting the micronised material. 12. A process for the preparation of the l-hydroxy-2-naphthalenecarboxylate (hydroxynaphthoate) salt of 4 - h y d ro x y - α - [ [ [ 6- (4 - phenylbutoxy)hexyl]aminoJmethyl]-l,3-benzenedimethanol in the form of spherical accretions of microcrystals, the spherical accretions being free-flowing, friable and micronisable, said process comprising quenching an organic or aqueous organic solution of the hydroxynaphthoate salt with an organic or aqueous organic solvent having a lower temperature than the said solution, whereby spherical accretions of microcrystals of the hydroxynaphthoate salt are produced. 13. A process according to claim 12 for the preparation of the l-hydroxy-2- naphthalenecarboxylate (hydroxynaphthoate) salt of 4-hydroxy-α. -[[[6-(4- phenylbutoxy)hexyl]amino]methyl]-l,3-benzenedimethanol in the form of spherical accretions of microcrystals, the spherical accretions being free-flowing, friable and micronisable said process comprising quenching a hot organic or hot aqueous organic solution of the hydroxynaphthoate salt with a cold organic or cold aqueous organic solvent to give spherical accretions of microcrystals of the hydroxynaphthoate salt and collecting said spherical accretions of microcrystals. 14. A process according to claim 13 characterised in that a hot organic solution of hydroxynaphthoate salt is quenched with a cold organic solvent to give spherical accretions of microcrystals of the hydroxynaphthoate salt 15. A process according to either claim 13 or claim 14 characterised in that the organic solvent employed in the hot organic or hot aqueous organic solution has a boiling point (at 760mm Hg) from 40° to 150°C, especially from 60° to 120°C. 16. A process according to claim 15 characterised in that the organic solvent comprises a lower alkyl ester. 17. A process according to claim 16 characterised in that the organic solvent comprises a lower alkyl alcohol, especially methanol, ethanol or isopropanol, most especially methanol. 18. A process according to any one of claims 13 to 17 characterised in that the organic solvent employed in the cold organic or cold aqueous organic solvent has a freezing point from -150° to -20°C, especially from -130° to -50°C. 19. A process according to claim 18 characterised in that the organic solvent comprises a lower (C^) alkyl alcohol, a lower (C j _ ) alkyl ether or a lower (C-^) alkyl ester. 20. A process according to claim 19 characterised in that the organic solvent comprises a lower alkyl alcohol, especially methanol, ethanol or isopropanol, most especially isopropanol. 21. A process according to any one of claims 13 to 20 characterised in that the temperature of the hot organic or the hot aqueous organic solution is from 30° to 80°C, especially from 40° to 70°C. 22. A process according to any one of claims 13 to 21 characterised in that the temperature of the cold organic or the cold aqueous solvent is from -35° to +15°C, especially from -25° to +10°C. 23. A process according to any one of claims 13 to 22 characterised in that, during the quenching of the hot organic or hot aqueous organic solution of the hydroxynaphthoate salt with the cold organic or cold aqueous organic solvent, the temperature of the mixture is maintained at a temperature below about +20°C, especially from -10° to +20°C, most especially from 0° to +20°C. 24. A process according to any one of claims 13 to 23 characterised in that the hot organic or hot aqueous organic solution of the hydroxynaphthoate salt is prepared by mixing l -h ydroxy-2-naph thoic acid an d 4- h ydrox y- o. - [ [ [6- (4- phenylbutoxy)hexyl]amino]methyl-l,3-benzenedimethanol in a hot organic or hot aqueous organic solvent. 25. Use of the compound as claimed in any one of claims 1 to 10 in the preparation of micronised hydroxynaphthoate salt. SUBSTITUTE SHEET 26. Use as claimed in claim 25 for the preparation of micronised hydroxynaphthoate salt having a particle size range suitable for pharmaceutical dosage forms to be delivered by inhalation or insufflation. 27. Use as claimed in either claim 25 or claim 26 characterised in that micronisation is effected using a fluid energy mill. E SHEET

Inventors: BEACH STEVEN FREDERICK, LATHAM DAVID WILLIAM STUART, ROBERTS TONY GORDON, SIDGWICK COLIN BRIAN, BEACH, STEVEN, FREDERICK, LATHAM, DAVID, WILLIAM, STUART, ROBERTS, TONY, GORDON, SIDGWICK, COLIN, BRIAN
Applicants: GLAXO GROUP LTD, GLAXO CROUP LIMITED
Application year: 1991
Main classification: A61K9
IPC codes: A61K9, A61K31, A61P11, A61P31, B02C19, C07C65, C07C69, C07C213, C07C217, C07C271, C07C323