MXPA98000809A - Procedure to prepare forms of solid doses of very low dose of farm - Google Patents
Procedure to prepare forms of solid doses of very low dose of farmInfo
- Publication number
- MXPA98000809A MXPA98000809A MXPA/A/1998/000809A MX9800809A MXPA98000809A MX PA98000809 A MXPA98000809 A MX PA98000809A MX 9800809 A MX9800809 A MX 9800809A MX PA98000809 A MXPA98000809 A MX PA98000809A
- Authority
- MX
- Mexico
- Prior art keywords
- further characterized
- composition according
- drug
- vehicle
- pharmaceutical composition
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims description 18
- 239000007787 solid Substances 0.000 title description 9
- 239000003814 drug Substances 0.000 claims abstract description 66
- 229940079593 drugs Drugs 0.000 claims abstract description 61
- 239000000203 mixture Substances 0.000 claims abstract description 50
- 238000002156 mixing Methods 0.000 claims abstract description 16
- 239000008194 pharmaceutical composition Substances 0.000 claims abstract description 14
- 206010012289 Dementia Diseases 0.000 claims abstract description 12
- 239000002245 particle Substances 0.000 claims abstract description 12
- 230000000069 prophylaxis Effects 0.000 claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 12
- 238000009472 formulation Methods 0.000 claims abstract description 10
- 239000003981 vehicle Substances 0.000 claims description 21
- 150000001875 compounds Chemical class 0.000 claims description 13
- 239000011230 binding agent Substances 0.000 claims description 9
- 239000000126 substance Substances 0.000 claims description 9
- HQKMJHAJHXVSDF-UHFFFAOYSA-L magnesium stearate Chemical compound [Mg+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O HQKMJHAJHXVSDF-UHFFFAOYSA-L 0.000 claims description 8
- WSVLPVUVIUVCRA-RJMJUYIDSA-N (2R,3R,4S,5R,6S)-2-(hydroxymethyl)-6-[(2R,3S,4R,5R)-4,5,6-trihydroxy-2-(hydroxymethyl)oxan-3-yl]oxyoxane-3,4,5-triol;hydrate Chemical compound O.O[C@@H]1[C@@H](O)[C@@H](O)[C@@H](CO)O[C@H]1O[C@@H]1[C@@H](CO)OC(O)[C@H](O)[C@H]1O WSVLPVUVIUVCRA-RJMJUYIDSA-N 0.000 claims description 7
- 229960001021 Lactose Monohydrate Drugs 0.000 claims description 7
- 238000004519 manufacturing process Methods 0.000 claims description 7
- 239000007884 disintegrant Substances 0.000 claims description 6
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 6
- 239000003795 chemical substances by application Substances 0.000 claims description 5
- GUBGYTABKSRVRQ-XLOQQCSPSA-N lactose Chemical compound O[C@@H]1[C@@H](O)[C@@H](O)[C@@H](CO)O[C@H]1O[C@@H]1[C@@H](CO)O[C@H](O)[C@H](O)[C@H]1O GUBGYTABKSRVRQ-XLOQQCSPSA-N 0.000 claims description 5
- 239000000314 lubricant Substances 0.000 claims description 5
- 239000003960 organic solvent Substances 0.000 claims description 5
- HWPKGOGLCKPRLZ-UHFFFAOYSA-M Monosodium citrate Chemical compound [Na+].OC(=O)CC(O)(C([O-])=O)CC(O)=O HWPKGOGLCKPRLZ-UHFFFAOYSA-M 0.000 claims description 4
- 235000019359 magnesium stearate Nutrition 0.000 claims description 4
- 235000018342 monosodium citrate Nutrition 0.000 claims description 4
- 239000002524 monosodium citrate Substances 0.000 claims description 4
- 238000002360 preparation method Methods 0.000 claims description 4
- 230000001225 therapeutic Effects 0.000 claims description 4
- FBPFZTCFMRRESA-KAZBKCHUSA-N D-Mannitol Natural products OC[C@@H](O)[C@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-KAZBKCHUSA-N 0.000 claims description 3
- FBPFZTCFMRRESA-KVTDHHQDSA-N Mannitol Chemical compound OC[C@@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-KVTDHHQDSA-N 0.000 claims description 3
- 239000000654 additive Substances 0.000 claims description 3
- 229960004977 anhydrous lactose Drugs 0.000 claims description 3
- 230000001419 dependent Effects 0.000 claims description 3
- 239000003937 drug carrier Substances 0.000 claims description 3
- 239000000594 mannitol Substances 0.000 claims description 3
- 235000010355 mannitol Nutrition 0.000 claims description 3
- 229960001855 mannitol Drugs 0.000 claims description 3
- -1 methoxyimino Chemical group 0.000 claims description 3
- 230000002378 acidificating Effects 0.000 claims description 2
- 239000000084 colloidal system Substances 0.000 claims description 2
- 239000000377 silicon dioxide Substances 0.000 claims description 2
- WEVYAHXRMPXWCK-UHFFFAOYSA-N acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 claims 4
- 239000002253 acid Substances 0.000 claims 2
- 239000000546 pharmaceutic aid Substances 0.000 claims 2
- FYNJWLOOBINARS-UHFFFAOYSA-N 3-chlorooctane Chemical compound CCCCCC(Cl)CC FYNJWLOOBINARS-UHFFFAOYSA-N 0.000 claims 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N HCl Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims 1
- 125000000956 methoxy group Chemical group [H]C([H])([H])O* 0.000 claims 1
- 238000001035 drying Methods 0.000 description 11
- 239000000843 powder Substances 0.000 description 7
- 230000015572 biosynthetic process Effects 0.000 description 6
- 238000005755 formation reaction Methods 0.000 description 6
- 239000002904 solvent Substances 0.000 description 6
- 239000012141 concentrate Substances 0.000 description 4
- 238000010790 dilution Methods 0.000 description 4
- 238000005538 encapsulation Methods 0.000 description 4
- 238000005469 granulation Methods 0.000 description 4
- 230000003179 granulation Effects 0.000 description 4
- 238000005507 spraying Methods 0.000 description 4
- 238000007907 direct compression Methods 0.000 description 3
- 239000007888 film coating Substances 0.000 description 3
- 238000009501 film coating Methods 0.000 description 3
- 229960001375 Lactose Drugs 0.000 description 2
- GUBGYTABKSRVRQ-UUNJERMWSA-N Lactose Natural products O([C@@H]1[C@H](O)[C@H](O)[C@H](O)O[C@@H]1CO)[C@H]1[C@@H](O)[C@@H](O)[C@H](O)[C@H](CO)O1 GUBGYTABKSRVRQ-UUNJERMWSA-N 0.000 description 2
- WHNWPMSKXPGLAX-UHFFFAOYSA-N N-Vinylpyrrolidone Chemical compound C=CN1CCCC1=O WHNWPMSKXPGLAX-UHFFFAOYSA-N 0.000 description 2
- 229940069328 Povidone Drugs 0.000 description 2
- CSCPPACGZOOCGX-UHFFFAOYSA-N acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- 239000008186 active pharmaceutical agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 239000008119 colloidal silica Substances 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 238000000227 grinding Methods 0.000 description 2
- 239000008101 lactose Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000011068 load Methods 0.000 description 2
- OKKJLVBELUTLKV-UHFFFAOYSA-N methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 2
- 229920000036 polyvinylpyrrolidone Polymers 0.000 description 2
- 235000013855 polyvinylpyrrolidone Nutrition 0.000 description 2
- 238000005204 segregation Methods 0.000 description 2
- 229960004373 Acetylcholine Drugs 0.000 description 1
- 210000003169 Central Nervous System Anatomy 0.000 description 1
- NEFBYIFKOOEVPA-UHFFFAOYSA-K Dicalcium phosphate Chemical compound [Ca+2].[Ca+2].[O-]P([O-])([O-])=O NEFBYIFKOOEVPA-UHFFFAOYSA-K 0.000 description 1
- 235000019739 Dicalciumphosphate Nutrition 0.000 description 1
- 241000124008 Mammalia Species 0.000 description 1
- 229920000168 Microcrystalline cellulose Polymers 0.000 description 1
- 102000014415 Muscarinic acetylcholine receptor family Human genes 0.000 description 1
- 108050003473 Muscarinic acetylcholine receptor family Proteins 0.000 description 1
- RUOJZAUFBMNUDX-UHFFFAOYSA-N Propylene carbonate Chemical compound CC1COC(=O)O1 RUOJZAUFBMNUDX-UHFFFAOYSA-N 0.000 description 1
- 229940032147 Starch Drugs 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- OIPILFWXSMYKGL-UHFFFAOYSA-N acetylcholine Chemical compound CC(=O)OCC[N+](C)(C)C OIPILFWXSMYKGL-UHFFFAOYSA-N 0.000 description 1
- 239000002535 acidifier Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000001506 calcium phosphate Substances 0.000 description 1
- 239000007963 capsule composition Substances 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 230000019771 cognition Effects 0.000 description 1
- 229940038472 dicalcium phosphate Drugs 0.000 description 1
- 229910000390 dicalcium phosphate Inorganic materials 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000002552 dosage form Substances 0.000 description 1
- 238000009509 drug development Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000010408 film Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000009477 fluid bed granulation Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 239000012442 inert solvent Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 230000002452 interceptive Effects 0.000 description 1
- 238000005461 lubrication Methods 0.000 description 1
- 229940016286 microcrystalline cellulose Drugs 0.000 description 1
- 235000019813 microcrystalline cellulose Nutrition 0.000 description 1
- 239000008108 microcrystalline cellulose Substances 0.000 description 1
- 239000002664 nootropic agent Substances 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 230000003389 potentiating Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 229940079832 sodium starch glycolate Drugs 0.000 description 1
- 239000008109 sodium starch glycolate Substances 0.000 description 1
- 229920003109 sodium starch glycolate Polymers 0.000 description 1
- 239000007909 solid dosage form Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 150000003431 steroids Chemical class 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- 238000004448 titration Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000005550 wet granulation Methods 0.000 description 1
Abstract
A method of formulation comprising mixing vehicle particles with a drug solution in water in an amount of 1-3% by weight of solution to total mixture and a method of treatment and / or prophylaxis of dementia, which method comprises administering to the [R- (Z)] - alpha- (methoxyimino) -alpha- (1-azabicyclo [2.2.2] oct-3-yl) acetonitrile monohydrochloride patient at a daily dose lower than 0.01 mg / kg and pharmaceutical compositions used in the present
Description
PROCEDURE FOR PREPARING FORMS OF SOLID DOSES OF VERY LOW DOSES OF THE DRUG
DESCRIPTIVE MEMORY
This invention relates to a method for formulating solid dose forms of drugs and solid dosage forms produced thereby, in particular solid dose forms containing low dose of drug. The invention also relates to a method for the treatment and / or prophylaxis of dementia and unit dosage forms useful herein. The common challenge in the manufacture of solid dose forms of drugs of very low dose, for example, with active doses of about 5-125 micrograms (μg) (eg, 0.004-0.1% by weight of drug to total solid) , is to ensure homogeneity. The technical problem is how to distribute the substance of the drug evenly among the large amount of excipient particles. The simplest way to make tablets is to simply mix all the ingredients like dry powders and make them tablet ("direct compression"). This is rarely successful for low-dose drugs; A common problem is the segregation of the powder mixture during tablet formation. A variation of this method that has been successful for low dose drugs is known as "titration," and is sometimes referred to as "orderly mixing" or "interactive mixing." First, very fine particles of the drug are mixed with a small portion of excipient; then the product is mixed with a slightly larger portion of excipient and so on until the desired mixture is obtained. This method depends on the fine particles of the drug that adhere electrostatically to large particles of the excipient, thus preventing segregation. The method works with some drugs, but success depends on the surface properties of both the drug and the excipient, and the method is very laborious. EP0503521 describes the application of this method to steroid drugs with high binding affinity and low non-mixing potential for certain excipients. A preferred alternative method for formulating low dose drugs is known as "wet granulation". The drug is dissolved in water or another solvent, and mixed with excipients including a binder, for example, povidone, to form a moist mass containing 5-20% by weight of solution to total weight of granulation mixture, which is dry later in a separate step. The binder causes the particles of the excipient to kneade together, and as the dry mass these lumps ("granules"), contain or coat with the drug. This is effective but difficult to handle, since the drying step requires special equipment, and usually involves high temperatures that can degrade labile drugs. Also, the use of the binder requires the additional inclusion of a disintegrant such as sodium starch glycolate or starch to help the tablet, which is cohesive, to disperse in the mouth. Fluid-bed granulation has been used to achieve uniformity of the low-dose tablet content (lμg-lOmg) (Thiel et al, J. Pharm Pharmacol 1986, 335-343). In this process, the micronized drug is mixed as a powder with other excipients, then loaded into a fluid bed granulator, and the powders are agglomerated by spraying in a solution of a binder; drying occurs concomitantly. The process does not require a separate drying step, but requires the use of micronized drug, and also incorporates a separate mixing step prior to granulation. It also requires specialized equipment and precise optimization of the parameters of the procedure. Another method for formulating low dose drugs is known as vehicle granulation (Michoel et al., Pharmaceutical Technology, June 1988, 66-84). This works by spraying a binder solution such as povidone in water into relatively large excipient particles such as hydrated lactose and then by spraying small particles of dry drug substance., thus coating the excipient with drug particles sticking thereto by the binder. The amount of solution used was 3.3-3.5% by weight of solution to the total granulation mixture. The method was applied to a formulation containing 4-5% drug by weight. This method also requires drying, the particle size of the drug needs to be very small, which often requires an additional grinding step and the very fine powder of the drug may not flow very well; and the formula still requires a disintegrant. Dahl et al., Drug Development and Industrial
Pharmacy 1990, 16 (12), 1881-1891, describes the preparation of solid capsule formulations using a liquid drug sprayer vehicle. The model drug is dissolved in a non-volatile solvent, propylene carbonate, and sprayed in a compressible sugar at a loading of about 0.01% by weight of drug to total solid, to give a final unit dose of 35μg. The solvent, being non-volatile, remains in the mixture. About 5% by weight of the total formulation is added; lower solvent to solid ratios resulted in reduced ability to disintegrate and dissolve. The resulting dust, somehow sticky, showed some difficulties in automatic encapsulation machines, and would probably give significant problems for tablet formation. Yal Owski (US 4,489,026) describes a process involving very slow spraying of a dilute solution of drug in a volatile inert solvent, preferably an organic solvent having a boiling point lower than 80 ° C, in the excipient powder in an open liner tray; a continuous flow of dry air the product during the sprinkling process. This procedure was applied to drugs with a unit dose of 10 μg or less. The spray speed is limited to l-10ml / min, making the procedure suitable only for very small load sizes (the aforementioned example prepared 1000 tablets). The weight ratio of solution to vehicle used was 15%; Also, the use of volatile organic liquids is now considered a significant hazard, requiring solvent recovery procedures and explosion-proof equipment. Katdare (US 4,989,736) describes a simplified version of this procedure, suitable for unit doses of 50-1000μg; the drug, dissolved in an easily evaporated solvent such as ethanol, methanol, acetone or rahydrofuran tet, is simply mixed with excipients in a ratio of 2.26% or 6.75% and then dried, followed by lubrication and tablet formation. This procedure is suitable in principle for commercial scale manufacturing, but still does not have the problems associated with the use of volatile organic solvents. In accordance with the present invention, there is provided a method of drug formulation comprising mixing vehicle particles with a drug solution in water in an amount of 1-3% by weight of solution to total mixture. The resulting mixture can be formulated into a suitable unit dose presentation, for example, by the tablet formation and optionally film coating of the tablets or by encapsulation. It may be convenient to do the initial mixture of drug / vehicle with a higher drug concentration, and then in a separate step mix this with additional vehicle, and this may be particularly useful where a tablet resistance scale is required. The separate mixing step aids drying by the dilution effect, ie the waste water is distributed through a larger amount of vehicle powder, and by the longer mixing time. Dilution is conveniently on the scale of 4/1 to 40/1 vehicle / concentrate by weight, depending on the processing characteristics of the vehicle. A convenient dilution ratio for lactose monohydrate is 10/1. Where the dilution step is not employed, the weight ratio of solution / mixture is more preferably up to 2% by weight. The optimum amount of solution will depend on the absorbing qualities of the vehicle particles, the solubility of the drug and the characteristics of the mixing device, the amount of solution chosen to allow even distribution of drug at the same time avoiding the need for a Hot drying step. The mixing step is preferably carried out in a high shear mixer. The vehicle can be any pharmaceutically acceptable excipientdirectly compressible, soluble, suitable such as anhydrous lactose, lactose monohydrate, mannitol, or a pharmaceutically acceptable, directly compressible, insoluble excipient such as microcrystalline cellulose or dicalcium phosphate, preferably a soluble excipient. Any drug having a sufficient degree of water solubility can be formulated by the process of the invention. The concentration of drug in the solution depends on the unit dose of drug required, the upper limit being dependent on the solubility of the drug. During mixing, the carrier particles are coated evenly with a very thin film of drug solution. Some of the water dries naturally during mixing, since there is usually a small air flow through the mixer; the remaining amount is so low that drying is not specifically required. If the tablets are coated with film, an additional degree of drying can be obtained during the coating process. The process of the invention has a number of advantages: it does not require grinding of the drug substance - a drying step is not needed. This simplifies processing and reduces production costs; Heat-labile drugs do not suffer at the temperature required for drying; for drugs that are highly potent, the omission of the drying step makes it easier to contain dust, improving safety for the factory worker - the use of volatile organic solvents is avoided - no need to add a binder - no need to add a disintegrant when the excipient is a highly soluble one. Optional additives in the final mixture include a disintegrant; a variety of acidic or alkaline excipients to improve the chemical stability of the drug in the formulation such as sodium dihydrogen citrate, preferably included in the initial mixture; a lubricant such as magnesium stearate; and a slip agent such as colloid silica. The present invention further provides a pharmaceutical composition comprising a drug formulated in accordance with the method of the invention and the use of said composition as an active therapeutic substance. The invention further provides a pharmaceutical composition comprising a drug, which can be obtained by the process of the invention and the use of said composition as an active therapeutic substance. The process of the invention is particularly useful for formulating [- (Z)] - a- (methoxyimino) -a- (l-azabicyclo [2.2.2] oct-3-yl) acetonitrile monohydrochloride (compound X) with active doses of about 5-125 micrograms (μg). Compound X and methods for its preparation are described in EP-A-0392803, W095 / 31456 and W093 / 17018. The compound improves the function of acetylcholine by means of an action on muscarinic receptors within the central nervous system, and therefore is of potential use in the treatment and / or prophylaxis of dementia in mammals. In particular, the invention provides a pharmaceutical composition comprising a pharmaceutically acceptable carrier and compound X at a level of up to 0.1% by weight of drug to vehicle, 0% of volatile organic solvent and 0% of binder. EP-A-0392803 suggests the appropriate daily dose for compound X and other compounds described therein as 0.01-5mg / kg. Surprisingly, it has been discovered through administration to human patients that efficacy as a cognition enhancer can be obtained at lower daily doses of O.Olmg / kg, more in particular 0.003mg / kg and less, for example, 0.0001- 0.003mg / kg, such as 0.00035-0.003mg / kg, 0.0007-0.003mg / kg, 0.0001-0.0007mg / kg or 0.00035-0.002mg / kg. Accordingly, the present invention provides a method of treatment and / or prophylaxis of dementia, and more particularly a method of improving cognition in a patient, which method comprises administering compound X to the patient at a lower daily dose of O. Olmg / kg, more preferable 0.003mg / kg or less. The invention also relates to the use of compound X in the manufacture of a medicament for the treatment and / or prophylaxis of dementia at a lower daily dose of O.Olmg / kg, more preferably of 0.003mg / kg or less. The invention further relates to a pharmaceutical composition for the treatment and / or prophylaxis of dementia which comprises compound X at a unit dose suitable for administration at a lower daily dose of O.Olmg / kg, more preferably 0.003mg / kg or less, and a pharmaceutically acceptable vehicle. The appropriate unit doses to achieve these daily doses are 5, 12.5, 25, 50 or 75μg, administered twice a day and, in the case of 50μg, once a day. The invention extends to the method, use or composition defined above wherein compound X is provided in said unit doses. The invention further provides a pharmaceutical composition comprising the compound X of the invention and / or formulated in accordance with the process of the invention, in the form of a unit dose selected from the scale of 5-125μg per unit dose, such as 5, 12.5, 25, 50 or 75μg per unit dose and the use of said composition as an active therapeutic substance, in particular in the treatment and / or prophylaxis of dementia.
EXAMPLE FORMULATION OF COMPOUND X
To make lOOg of mixture for tablet formation or encapsulation, at lOOug of drug per 150mg of excipient: - dissolve 67g of drug in 1 liter of water (i.e., 1% water (1067% solution) on a weight)
- slowly add this to 100kg of a "direct compression" grade of lactose monohydrate in a high shear mixer-granulator - mix with 0.25kg of lubricant (Magnesium Stearate) and 0.15kg of Sliding Agent (Colloidal Silica)
- tablet - film coating (optional) To make 100kg of mixture for the tablet formation or encapsulation, to lOOug of drug per 150mg of excipient, by means of a concentrate: - dissolve 67g of drug in 0.1 liter of water - add slowly this to 9.8kg of a grade of
"Direct compression" of lactose monohydrate and 0.2kg of acidifying agent (Sodium Dihydrogen Citrate) in a high-shear ezclador-granulator, followed by another 0.1 liter of water to rinse the used containers, at the same time mixing vigorously with a crumbling speed of about 1500 rpm and then raising the speed to about 3000 rpm, during 10-20 minutes of total mixing time (i.e., a total of 2% water (2.67% solution) is added over a base in weight with respect to the amount of concentrate) - sift the resulting concentrate in a drum mixer - mix with 88kg of additional lactose and 1.8kg of Sodium Dihydrogen Citrate, then mix in 0.15kg of Sliding Agent (Colloidal Silica ) and 0.25kg of lubricant (Magnesium Stearate) - tablet - film coating (optional) To make unit doses of 75, 50, 25, 12.5 and 5μg in 150mg of excipient, the amount of rmaco used in the above methods is 50, 33.6, 16.8, 8.4 and 3.3g respectively.
Claims (29)
1. - A process for preparing a drug formulation comprising mixing vehicle particles with a drug solution in water in an amount of 1-3% solution to total mixture.
2. A method according to claim 1, further characterized in that the vehicle is a pharmaceutically acceptable excipient, directly compressible, soluble or an insoluble.
3. A method according to claim 2, further characterized in that the vehicle is a soluble excipient selected from anhydrous lactose, lactose monohydrate and mannitol.
4. A process according to claim 3, further characterized in that the mixture comprises an acid or alkaline excipient to improve the chemical stability of the drug in the formulation.
5. A method according to any preceding claim, further characterized in that it comprises mixing the mixture with additional vehicle and / or one or more additives selected from a disintegrant; an acid or alkaline excipient to improve the chemical stability of the drug in the formulation, a lubricant and a slip agent.
6. - A method according to claim 5, further characterized in that the mixture is mixed with additional vehicle in a weight ratio of 1/4 to 1/40.
7. A method according to any preceding claim, further characterized in that the mixture is formulated in a unit dose presentation.
8. A method according to any preceding claim, further characterized in that the drug is [R- (Z)] -oc- (methoxyimino) -a- (l-azabicicio [2.2.2] oct-3-yl monohydrochloride. Acetonitrile.
9. A pharmaceutical composition comprising a drug, which can be obtained by the method according to any preceding claim.
10. A pharmaceutical composition comprising a pharmaceutically acceptable carrier and [R- (Z)] - a- (methoxyimino) -a- (l-azabicyclo [2.2.2] oct-3-yl) acetonitrile monohydrochloride at a up to 0.1% by weight of drug to vehicle, 0% of volatile organic solvent and 0% of binder.
11. A composition according to claim 10, further characterized in that the vehicle is a pharmaceutically acceptable excipient, directly compressible, soluble or insoluble.
12. A composition according to claim 11, further characterized in that the vehicle is a soluble excipient selected from anhydrous lactose, lactose monohydrate and mannitol.
13. A composition according to any of claims 10 to 12, further characterized in that it also comprises one or more additives selected from a disintegrant; an acidic excipient to improve the chemical stability of the drug in the formulation, a lubricant and a slip agent.
14. A composition according to claim 13, further characterized in that it comprises lactose monohydrate, sodium dihydrogen citrate, colloid silica and magnesium stearate.
15. A composition according to any of claims 10 to 14, further characterized in that it is formulated in a unit dose presentation.
16. The use of [R- (Z)] - a- (methoxyimino) - - (l-azabicyclo [2.2.2] oct-3-yl) acetonitrile monohydrochloride in the manufacture of a medicament for the treatment and / or dementia prophylaxis, by administering the medicament to provide a lower daily dose of O.Olmg / kg.
17. A pharmaceutical composition for the treatment and / or prophylaxis of dementia comprising monohydrochloride of [R- (Z)] - a- (methoxy i) -oc- (l-azabicyclo [2.2.2] oct-3-) il) acetonitrile at a suitable unit dose for administration at a lower daily dose of O.Olmg / kg, and a pharmaceutically acceptable carrier.
18. A method, use or composition according to claim 16 or 17, further characterized in that the daily dose is 0.003mg / kg or less.
19. A method, use or composition according to claim 18, further characterized in that the daily dose is 0.0001-0.003mg / kg.
20. A method, use or composition according to claim 19, further characterized in that the daily dose is 0.00035-0.003mg / kg.
21. A method, use or composition according to claim 19, further characterized in that the daily dose is 0.0007-0.003mg / kg.
22. A method, use or composition according to claim 19, further characterized in that the daily dose is 0.0001-0.0007mg / kg.
23. A method, use or composition according to claim 19, further characterized in that the daily dose is 0.00035-0.002mg / kg.
24. A method, use or composition according to claim 16 or 17, further characterized in that the compound is presented in a unit dose of 5, 12.5, 25, 50 or 75μg, administered twice a day, or in the case of 50μg, once a day.
25. A pharmaceutical composition according to claim 9 dependent on claim 8 or according to any of claims 10 to 15, further characterized in that it is in the unit dose form selected from the scale of 5-125μg per dose unitary
26. A pharmaceutical composition according to claim 25, further characterized in that it comprises 5, 12.5, 25, 50 or 75 μg per unit dose.
27. The use of a pharmaceutical composition according to claim 9, according to any of claims 10 to 15 or according to claim 25 or 26, further characterized as an active therapeutic substance in the preparation of a drug for the treatment and / or prophylaxis of dementia.
28. The use of a pharmaceutical composition according to claim 9 dependent on claim 8, further characterized in the preparation of a medicament for use in the treatment and / or prophylaxis of dementia.
29. Use of a pharmaceutical composition according to claim 28, further characterized in the manufacture of a medicament for the treatment and / or prophylaxis of dementia.
Applications Claiming Priority (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GBGB9515624.6A GB9515624D0 (en) | 1995-07-29 | 1995-07-29 | Novel process |
GBGB9606684.0A GB9606684D0 (en) | 1996-03-29 | 1996-03-29 | Novel process |
GB9515624.6 | 1996-03-29 | ||
GB9606684.0 | 1996-03-29 | ||
PCT/EP1996/003326 WO1997004750A2 (en) | 1995-07-29 | 1996-07-29 | Process for preparing solid dosage forms of very low-dose drugs |
Publications (2)
Publication Number | Publication Date |
---|---|
MXPA98000809A true MXPA98000809A (en) | 1998-04-01 |
MX9800809A MX9800809A (en) | 1998-04-30 |
Family
ID=26307485
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
MX9800809A MX9800809A (en) | 1995-07-29 | 1996-07-29 | Process for preparing solid dosage forms of very low-dose drugs. |
Country Status (25)
Country | Link |
---|---|
EP (1) | EP0841902A2 (en) |
JP (1) | JPH11510493A (en) |
KR (1) | KR19990035972A (en) |
CN (1) | CN1196677A (en) |
AP (1) | AP858A (en) |
AR (1) | AR004178A1 (en) |
AU (1) | AU716961B2 (en) |
BG (1) | BG102266A (en) |
BR (1) | BR9609804A (en) |
CA (1) | CA2228048A1 (en) |
CZ (1) | CZ24798A3 (en) |
DZ (1) | DZ2077A1 (en) |
EA (2) | EA199901055A1 (en) |
HU (1) | HUP9900521A3 (en) |
IL (1) | IL122897A0 (en) |
MA (1) | MA23953A1 (en) |
MX (1) | MX9800809A (en) |
NO (1) | NO980384L (en) |
NZ (1) | NZ315632A (en) |
OA (1) | OA10659A (en) |
PL (1) | PL325242A1 (en) |
SK (1) | SK11098A3 (en) |
TR (1) | TR199800156T1 (en) |
UY (1) | UY24297A1 (en) |
WO (1) | WO1997004750A2 (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB9619074D0 (en) * | 1996-09-12 | 1996-10-23 | Smithkline Beecham Plc | Composition |
CA2323177A1 (en) * | 1998-03-11 | 1999-09-16 | Susan Marie Milosovich | Composition |
FR2796840B1 (en) * | 1999-07-26 | 2003-06-20 | Ethypharm Lab Prod Ethiques | LOW-DOSE TABLETS AND METHOD OF PREPARATION |
PT1591121E (en) | 2000-12-14 | 2009-07-20 | Ortho Mcneil Janssen Pharm | Process for preparing steroid hormone products comprising a stabilizing agent in non-crystalline form |
JP2007532511A (en) * | 2004-04-09 | 2007-11-15 | スミスクライン ビーチャム コーポレーション | Low dose medicine |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4489026A (en) * | 1982-09-07 | 1984-12-18 | The Upjohn Company | Process for preparing solid unit dosage forms of ultra-low dose drugs |
JPS5970614A (en) * | 1982-10-14 | 1984-04-21 | Asahi Chem Ind Co Ltd | Wet solid pharmaceutical preparation of very small amount of main drug |
US4898736A (en) * | 1988-03-09 | 1990-02-06 | Merck & Co., Inc. | Method for tablet preparation |
DK0392803T3 (en) * | 1989-04-13 | 2004-10-18 | Beecham Group Plc | Hitherto unknown compounds |
ZA939565B (en) * | 1993-12-21 | 1994-08-11 | Applied Analytical Ind Inc | Method for preparing low dose pharmaceutical products. |
-
1996
- 1996-07-25 AR ARP960103748A patent/AR004178A1/en not_active Application Discontinuation
- 1996-07-26 MA MA24329A patent/MA23953A1/en unknown
- 1996-07-26 UY UY24297A patent/UY24297A1/en not_active IP Right Cessation
- 1996-07-27 DZ DZ960121A patent/DZ2077A1/en active
- 1996-07-29 JP JP9507243A patent/JPH11510493A/en active Pending
- 1996-07-29 IL IL12289796A patent/IL122897A0/en unknown
- 1996-07-29 CZ CZ98247A patent/CZ24798A3/en unknown
- 1996-07-29 BR BR9609804A patent/BR9609804A/en not_active Application Discontinuation
- 1996-07-29 WO PCT/EP1996/003326 patent/WO1997004750A2/en not_active Application Discontinuation
- 1996-07-29 SK SK110-98A patent/SK11098A3/en unknown
- 1996-07-29 EA EA199901055A patent/EA199901055A1/en unknown
- 1996-07-29 EA EA199800179A patent/EA000740B1/en not_active IP Right Cessation
- 1996-07-29 HU HU9900521A patent/HUP9900521A3/en unknown
- 1996-07-29 PL PL96325242A patent/PL325242A1/en unknown
- 1996-07-29 CN CN96197054A patent/CN1196677A/en active Pending
- 1996-07-29 MX MX9800809A patent/MX9800809A/en unknown
- 1996-07-29 TR TR1998/00156T patent/TR199800156T1/en unknown
- 1996-07-29 KR KR1019980700633A patent/KR19990035972A/en not_active Application Discontinuation
- 1996-07-29 AU AU67384/96A patent/AU716961B2/en not_active Ceased
- 1996-07-29 EP EP96927621A patent/EP0841902A2/en not_active Withdrawn
- 1996-07-29 NZ NZ315632A patent/NZ315632A/en unknown
- 1996-07-29 AP APAP/P/1998/001170A patent/AP858A/en active
- 1996-07-29 CA CA002228048A patent/CA2228048A1/en not_active Abandoned
-
1998
- 1998-01-28 NO NO980384A patent/NO980384L/en unknown
- 1998-01-28 OA OA9800013A patent/OA10659A/en unknown
- 1998-02-20 BG BG102266A patent/BG102266A/en unknown
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