WO2012088992A1 - Process for preparing solid medicine preparation and solid medicine preparation therefrom - Google Patents

Process for preparing solid medicine preparation and solid medicine preparation therefrom Download PDF

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Publication number
WO2012088992A1
WO2012088992A1 PCT/CN2011/083285 CN2011083285W WO2012088992A1 WO 2012088992 A1 WO2012088992 A1 WO 2012088992A1 CN 2011083285 W CN2011083285 W CN 2011083285W WO 2012088992 A1 WO2012088992 A1 WO 2012088992A1
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Prior art keywords
water
insoluble
active ingredient
agent
pharmaceutical active
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PCT/CN2011/083285
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French (fr)
Chinese (zh)
Inventor
郑斯骥
谭波
傅麟勇
袁少卿
曹智慧
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上海中西制药有限公司
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Publication of WO2012088992A1 publication Critical patent/WO2012088992A1/en

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    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/14Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
    • A61K9/16Agglomerates; Granulates; Microbeadlets ; Microspheres; Pellets; Solid products obtained by spray drying, spray freeze drying, spray congealing,(multiple) emulsion solvent evaporation or extraction
    • A61K9/1605Excipients; Inactive ingredients
    • A61K9/1617Organic compounds, e.g. phospholipids, fats
    • A61K9/1623Sugars or sugar alcohols, e.g. lactose; Derivatives thereof; Homeopathic globules
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K31/00Medicinal preparations containing organic active ingredients
    • A61K31/33Heterocyclic compounds
    • A61K31/335Heterocyclic compounds having oxygen as the only ring hetero atom, e.g. fungichromin
    • A61K31/365Lactones
    • A61K31/366Lactones having six-membered rings, e.g. delta-lactones
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K31/00Medicinal preparations containing organic active ingredients
    • A61K31/33Heterocyclic compounds
    • A61K31/395Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins
    • A61K31/40Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins having five-membered rings with one nitrogen as the only ring hetero atom, e.g. sulpiride, succinimide, tolmetin, buflomedil
    • A61K31/403Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins having five-membered rings with one nitrogen as the only ring hetero atom, e.g. sulpiride, succinimide, tolmetin, buflomedil condensed with carbocyclic rings, e.g. carbazole
    • A61K31/404Indoles, e.g. pindolol
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K31/00Medicinal preparations containing organic active ingredients
    • A61K31/33Heterocyclic compounds
    • A61K31/395Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins
    • A61K31/495Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins having six-membered rings with two or more nitrogen atoms as the only ring heteroatoms, e.g. piperazine or tetrazines
    • A61K31/505Pyrimidines; Hydrogenated pyrimidines, e.g. trimethoprim
    • A61K31/513Pyrimidines; Hydrogenated pyrimidines, e.g. trimethoprim having oxo groups directly attached to the heterocyclic ring, e.g. cytosine
    • A61K31/515Barbituric acids; Derivatives thereof, e.g. sodium pentobarbital
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K31/00Medicinal preparations containing organic active ingredients
    • A61K31/33Heterocyclic compounds
    • A61K31/395Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins
    • A61K31/495Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins having six-membered rings with two or more nitrogen atoms as the only ring heteroatoms, e.g. piperazine or tetrazines
    • A61K31/505Pyrimidines; Hydrogenated pyrimidines, e.g. trimethoprim
    • A61K31/519Pyrimidines; Hydrogenated pyrimidines, e.g. trimethoprim ortho- or peri-condensed with heterocyclic rings
    • A61K31/525Isoalloxazines, e.g. riboflavins, vitamin B2
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K31/00Medicinal preparations containing organic active ingredients
    • A61K31/33Heterocyclic compounds
    • A61K31/395Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins
    • A61K31/54Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins having six-membered rings with at least one nitrogen and one sulfur as the ring hetero atoms, e.g. sulthiame
    • A61K31/549Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins having six-membered rings with at least one nitrogen and one sulfur as the ring hetero atoms, e.g. sulthiame having two or more nitrogen atoms in the same ring, e.g. hydrochlorothiazide
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K31/00Medicinal preparations containing organic active ingredients
    • A61K31/64Sulfonylureas, e.g. glibenclamide, tolbutamide, chlorpropamide
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/14Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
    • A61K9/16Agglomerates; Granulates; Microbeadlets ; Microspheres; Pellets; Solid products obtained by spray drying, spray freeze drying, spray congealing,(multiple) emulsion solvent evaporation or extraction
    • A61K9/1605Excipients; Inactive ingredients
    • A61K9/1629Organic macromolecular compounds
    • A61K9/1635Organic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polyvinyl pyrrolidone, poly(meth)acrylates
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/14Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
    • A61K9/16Agglomerates; Granulates; Microbeadlets ; Microspheres; Pellets; Solid products obtained by spray drying, spray freeze drying, spray congealing,(multiple) emulsion solvent evaporation or extraction
    • A61K9/1605Excipients; Inactive ingredients
    • A61K9/1629Organic macromolecular compounds
    • A61K9/1652Polysaccharides, e.g. alginate, cellulose derivatives; Cyclodextrin
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/20Pills, tablets, discs, rods
    • A61K9/2004Excipients; Inactive ingredients
    • A61K9/2013Organic compounds, e.g. phospholipids, fats
    • A61K9/2018Sugars, or sugar alcohols, e.g. lactose, mannitol; Derivatives thereof, e.g. polysorbates
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/20Pills, tablets, discs, rods
    • A61K9/2004Excipients; Inactive ingredients
    • A61K9/2022Organic macromolecular compounds
    • A61K9/205Polysaccharides, e.g. alginate, gums; Cyclodextrin
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/20Pills, tablets, discs, rods
    • A61K9/2004Excipients; Inactive ingredients
    • A61K9/2022Organic macromolecular compounds
    • A61K9/205Polysaccharides, e.g. alginate, gums; Cyclodextrin
    • A61K9/2054Cellulose; Cellulose derivatives, e.g. hydroxypropyl methylcellulose

Definitions

  • the invention belongs to the field of pharmaceutical preparations, and particularly relates to a preparation method of a solid pharmaceutical preparation and a obtained solid preparation of the medicament. Background technique
  • the particle size of the pharmaceutically active ingredient is closely related to the preparation process and quality of the solid preparation, and the reduction of the particle size is the key to improving the dissolution and content uniformity of the pharmaceutical preparation.
  • the particle size of a suitable pharmaceutically active ingredient is usually selected depending on the dissolution characteristics of the drug and the permeability of the biofilm. For example, if the solubility is poor, drug dissolution is a drug that absorbs the rate-limiting process, and a smaller particle size can be selected to promote drug absorption.
  • selective control of the particle size of the pharmaceutically active ingredient is often involved.
  • the universal pulverizer is a pulverizer widely used in the field of medicine.
  • the effect of crushing materials is mainly on impact force and shearing force. It is suitable for a variety of medium-hardness dry materials.
  • the average particle size after treatment is generally 100. About micrometers.
  • the treatment method of mechanical pulverization has problems such as a lot of dust, a polluted environment, and a large loss.
  • it is easy to cause adverse reactions in the mechanical pulverization process, and there are serious safety hazards.
  • inhalation of a lower dose of sedative sleeping pills powder can quickly produce hypnotic effects.
  • these drugs are pulverized, it is highly prone to cause an operator's rapid hypnosis and cause a safety accident.
  • inhaling or contacting a certain amount of the drug powder can easily cause a serious drug reaction by the operator.
  • the average particle size reaches about 100 microns, and the dissolution characteristics of the prepared solid preparations are not satisfactory.
  • mechanical pulverization treatment for a high active pharmaceutically active ingredient having a low content (e.g., 5 wt%) in a solid preparation, it also relates to the problem of dispersion uniformity of its mixing with an auxiliary material.
  • a method of gradually diluting the pharmaceutically active ingredient and the auxiliary material in an equal amount is used to uniformly disperse the pharmaceutically active ingredient in the solid preparation.
  • the method is cumbersome in process operation, and also causes many problems such as dust, environmental pollution, large loss, and safety hazards in labor protection.
  • the preparation of solid preparations also needs to consider whether the various properties of the product can meet the needs. For example, is it possible to ensure a better content uniformity?
  • stability is the focus of the quality of the solid preparation, including the chemical stability of the active ingredient, the content of impurities, the stability of the solid preparation, and the stability of dissolution during storage of the solid preparation, whether it is in the medicine Within the standard limits.
  • the technical problem to be solved by the present invention is to overcome the conventional method for preparing a solid preparation by mechanically pulverizing and controlling the particle size of the pharmaceutically active ingredient, which causes environmental pollution, has serious safety hazards, and has large loss, and the obtained solid pharmaceutical preparation
  • the solubility is not ideal, and the water-insoluble or poorly water-soluble acidic drug provides a simpler operation, less pollution, no such safety hazard, and can ensure that the prepared solid preparation has excellent dissolution characteristics.
  • A-BSoD Acid-Base Solventing-out Dispersion
  • the drug which is then returned to the solid state during the granulation process, avoids many of the drawbacks of mechanical comminution.
  • the inventors have unexpectedly found that the water-insoluble and/or poorly water-soluble acidic pharmaceutical solid preparation obtained by the method has excellent dissolution characteristics, stability, and content uniformity.
  • the method for preparing a pharmaceutical solid preparation of the present invention comprises the steps of: insoluble water and/or water
  • the soluble acidic pharmaceutical active ingredient is dissolved in an alkaline solution containing an alkalizing agent to prepare a medicated alkaline liquid; thereafter, the auxiliary material and the medicated alkaline liquid are uniformly mixed to perform wet granulation.
  • the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient is selected from various existing pharmaceutically active ingredients satisfying the above properties, including an amphoteric active ingredient having both an acidic group and a basic group. .
  • the acidic pharmaceutically active ingredients are weak acid active ingredients.
  • the present invention preferably has a high activity and a low content in a solid preparation (generally 20% or less, preferably 10% or less, more preferably 5% or less, and a percentage by mass) of water-insoluble or poorly water-soluble acidity. Pharmaceutical active ingredient.
  • the present invention is preferably, but not limited to, glipizide, folic acid, bumetanide, diclofenac, isocarbopurine, benzfluorothiazide, p-fluorothiazide, methotrexate, vitamin H , hexaerythritol, indapamide, furosemide, thioguanine, allopurinol, gliclazone, simvastatin, leflunomide, hydrochlorothiazide or phenobarbital.
  • the mass percentage of the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient in the wet-processed dry material can be determined during the preparation.
  • other pharmaceutically active ingredients may be added to prepare a compound solid preparation.
  • the alkalizing agent refers to a reagent capable of completely dissolving a water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient in an alkaline solution containing an alkalizing agent.
  • the basifying agent should be a pharmaceutically acceptable agent compatible with water insoluble and/or poorly water soluble acidic pharmaceutical active ingredients.
  • the compatibility means coexistence without adverse effects.
  • the alkalizing agent may be a single alkalizing agent or a complex alkalizing agent composed of two or more components, and may be selected from various bases such as inorganic bases and/or organic bases, strong bases and/or weakeners.
  • the base is preferably selected from one or more of sodium hydroxide, potassium hydroxide, sodium carbonate, potassium carbonate, sodium ethoxide, meglumine, diethanolamine and triethanolamine.
  • the basifying agent described below is particularly preferred in the present invention:
  • the alkalizing agent is sodium hydroxide, potassium hydroxide or sodium ethoxide, most preferably sodium hydroxide.
  • the alkalization is sodium hydroxide or potassium hydroxide, and the most preferred is sodium hydroxide.
  • the alkalizing agent is sodium hydroxide, potassium hydroxide, sodium ethoxide, sodium carbonate or potassium carbonate, and most preferably sodium hydroxide or carbonic acid. sodium.
  • the alkalizing agent is sodium hydroxide, potassium hydroxide, sodium carbonate or potassium carbonate.
  • the alkalizing agent is sodium hydroxide or potassium hydroxide.
  • the alkalizing agent is used in an amount at least the minimum amount which can completely dissolve the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient, preferably 1 to 1.5 times the minimum amount, and most preferably 1 to 1.05. Times.
  • the amount of the alkalizing agent which can dissolve the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient is related to various factors such as the type of alkalizing agent, the type of solvent, the water-insoluble and/or poorly water-soluble acidic drug in the alkalizing agent.
  • the number of negative ions combined with the acid center of the active ingredient and the preparation conditions of the medicated alkaline solution (such as temperature, time, feeding sequence, stirring method) and the like.
  • the acidic center means a group or a portion of the water-insoluble and/or water-insoluble acidic drug active ingredient which can bind to a negative ion in the alkalizing agent molecule. Therefore, the above minimum amount refers to the minimum amount of an alkalizing agent which can be dissolved by a certain alkali-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient under the same solvent and medicated alkaline solution. The minimum amount can be determined by a simple conventional method: in the same solvent and the medicated alkaline solution, the amount of the alkalizing agent is gradually increased to dissolve a certain water-insoluble and/or poorly water-soluble acidic drug. The active ingredient, when completely dissolved, is the minimum amount.
  • the present inventors have found through a large number of experiments that, in particular, the molar ratio of the alkalizing agent to the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient is generally from 0.1 to 2.5, and most of from 0.9 to 1.5, and the present invention is particularly preferred.
  • sodium hydroxide or sodium ethoxide having a molar amount of 0.7 to 1.1 times is particularly preferred.
  • sodium hydroxide having a molar amount of 0.95 to 1.1 times is particularly preferable.
  • sodium hydroxide having a molar amount of 1.8 to 2.1 times or a molar amount of 0.95 to 1.1 is particularly preferable. Times sodium carbonate or potassium carbonate.
  • sodium hydroxide having a molar amount of 1.4 to 1.6 times or sodium carbonate having a molar amount of 0.85 to 1.1 times is particularly preferable.
  • sodium hydroxide having a molar amount of 0.9 to 1.6 times is particularly preferable.
  • the solvent in the alkalizing agent-containing alkaline solution may be water, an organic solvent or a mixture of water and an organic solvent.
  • the solvent selected should be an ion dissociable solvent in the alkalizing agent.
  • the alkalizing agent is an inorganic substance, water or a mixed liquid of water and an organic solvent may be selected; and when the alkalizing agent is an organic substance, it may be a mixed liquid of water, water and an organic solvent, or an organic solvent.
  • the pharmaceutically active ingredient is superior to the solubility in water in some organic solvents, it is preferred to select a mixture of water and the organic solvent to facilitate dissolution of the active ingredient of the drug, and to reduce the amount of alkalizing agent or solvent, which is advantageous for The operation of the subsequent granulation step.
  • the organic solvent is selected according to the principle that its solubility in water-insoluble and/or poorly water-soluble acidic pharmaceutically active ingredients is superior to water in a solvent acceptable for the pharmaceutical field, preferably organically miscible with water.
  • a solvent such as a water-soluble alcohol solvent commonly used in the pharmaceutical field, such as ethanol, propylene glycol, glycerol, acetone, isopropanol or tert-butanol, preferably one or more of ethanol, acetone, propylene glycol and glycerol. Particularly preferred is ethanol.
  • the concentration of the organic solvent can be arbitrarily selected.
  • the amount of the solvent in the alkaline solution is such that at least the drug is soluble, at least the minimum amount of granulating liquid required for wet granulation, generally 5 to 100% by mass of the dry granulated dry material, preferably 10 ⁇ 50%.
  • some excipients such as a binder, a surfactant, a solubilizing agent, and a water-soluble carrier of the solid dispersion may be added.
  • the water-insoluble and/or water-insoluble acidic pharmaceutically active ingredient is dissolved in the alkaline solution containing the alkalizing agent while and/or after, the water-soluble solution of the surfactant, the solubilizing agent and the solid dispersion is further added.
  • One or more of the carrier materials are then subjected to a subsequent step of uniformly mixing the excipients with the excipients for wet granulation.
  • the amount of the water-soluble carrier of the solid dispersion to be added at this time is required. Controlled to ensure that the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredients are completely dissolved in the alkaline agent-containing alkaline The amount in the solution is below; after that, a water-soluble carrier of the solid dispersion may be further added to the solution, and when the amount added is large, the obtained drug-containing acidic liquid may be in the form of a suspension or a viscous liquid.
  • Particularly preferred in the present invention are the addition of povidone, polyethylene glycol (preferably polyethylene glycol 400-8000), sodium dodecyl sulfate, poloxamer, polyoxyethylene castor oil, Tween (preferably Tween 80). And one or more of polyoxyl 40 stearate, lactose, mannitol, sucrose, hydroxypropyl- ⁇ -cyclodextrin, ⁇ -cyclodextrin and maltitol.
  • the surfactant and/or solubilizer is preferably added in an amount of 0.05 to 5 times, more preferably 0.05 to 2 times, the mass of the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient.
  • the water-soluble carrier of the solid dispersion is preferably added in an amount of from 0.5 to 20 times, more preferably from 0.5 to 2 times, the mass of the water-insoluble and/or water-insoluble acidic pharmaceutical active ingredient.
  • a surfactant and/or a solubilizing agent as described above, the solubility of the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient in an alkaline solution can be increased, the amount of the solvent can be reduced, and the operation of the subsequent granulation step can be facilitated.
  • the water-soluble carriers of the surfactant, the solubilizer and the solid dispersion are added as described above, in particular, the water-soluble carrier of the solid dispersion can make the dissolution characteristics of the obtained solid preparation.
  • the preparation temperature of the medicated alkaline solution may be appropriately raised by a conventional heating method such as a hot water bath to facilitate dissolution of the pharmaceutically active ingredient.
  • a conventional heating method such as a hot water bath
  • water is used as the solvent, it is preferably raised to 40 to 80 °C.
  • the preferred increase is 40 to 70 °C.
  • ethanol is used as the solvent, the preferred increase is 30 to 50 °C.
  • the excipient may be selected from any of the excipients known and widely used in the art, such as fillers, binders, disintegrants, adsorbents, lubricants and the like.
  • the amount of the excipients can be selected according to routine or prior knowledge in the art.
  • the filler is preferably one or more of lactose, microcrystalline cellulose, starch, pregelatinized starch, mannitol, sucrose and maltitol.
  • the binder is preferably one or more of hypromellose, povidone, methylcellulose and hydroxypropylcellulose.
  • the disintegrant is preferably one or more of sodium carboxymethyl starch, low-substituted hydroxypropyl cellulose, cross-linked polyvinylpyrrolidone and croscarmellose sodium.
  • the lubricant is preferably magnesium stearate, micronized silica gel (colloidal silica), talc or sodium stearate.
  • the acidifying agent is added to lower the alkalinity of the mixture of the acidifying agent and the medicated alkaline solution with respect to the alkalinity of the medicated alkaline solution.
  • the acidulant should be a pharmaceutically acceptable agent compatible with water insoluble and/or poorly water soluble acidic pharmaceutical active ingredients.
  • the present invention is preferably a combination of an alkalizing agent and an acidifying agent of the following type: the alkalizing agent is an inorganic strong base, an organic strong base or an inorganic medium strong base, and the acidifying agent is an inorganic strong acid (such as hydrochloric acid).
  • the amount of the acidifying agent is such an amount that at least the alkalinity of the mixture of the acidifying agent and the medicated alkaline liquid is lowered relative to the alkalinity of the medicated alkaline liquid.
  • the amount of the alkalizing agent and the acidifying agent satisfies the following relationship:
  • the value obtained by the formula 1 is 0.01 to 1.5, preferably 0.2 to 1.1, more preferably 0.9 to 1.1.
  • the present invention particularly preferably has a combination of the following alkalizing agent and acidifying agent of the formula 1 having a value of 0.9 to 1.1: sodium hydroxide and hydrochloric acid, potassium hydroxide and hydrochloric acid, sodium ethoxide and hydrochloric acid, sodium carbonate and hydrochloric acid, and potassium carbonate and hydrochloric acid. .
  • the addition of an acidifying agent is more advantageous for the stability of the solid preparation.
  • the solid preparation can still have better stability without adding an acidifying agent or an acidifying agent in the formulation, but does not affect the preparation. Under the premise of stability, appropriately increasing the amount of acidifier to reduce alkalinity can help to alleviate the pH of solid preparations.
  • the wet granulation can be carried out according to the conventional steps and conditions of various granulation methods in the field of wet granulation in the art, such as extrusion granulation (such as swinging machine extrusion, spiral extrusion or rotary extrusion). Pressing, etc., stirring granulation, fluidized spray granulation or centrifugal spray granulation.
  • extrusion granulation such as swinging machine extrusion, spiral extrusion or rotary extrusion. Pressing, etc., stirring granulation, fluidized spray granulation or centrifugal spray granulation.
  • the acidic pharmaceutically active ingredient may be selected from a wet granulation process in which the amount of the granulation solution is limited, such as fluidized spray granulation or centrifugal spray
  • the acidifying agent or the acidifying agent-containing solution and the auxiliary material are uniformly mixed, and then uniformly mixed with the medicated alkaline liquid, and subjected to extrusion granulation or stirring granulation; and (2) the medicated alkaline liquid and the acidifying agent or The solution of the acidifying agent is uniformly mixed to obtain a granulating liquid, and then the granulating liquid and the auxiliary material are subjected to extrusion granulation, agitation granulation, fluidized spray granulation or centrifugal spray granulation; and the method (3) will contain The alkaline solution of the drug is uniformly mixed with the auxiliary material, and then uniformly mixed with the solution containing the acidifying agent, and subjected to extrusion granulation or stirring granulation; and (4) the medicated alkaline liquid and the auxiliary material of 1/3 or less And the acidifying agent or the acidifying agent-containing solution is uniformly mixed
  • the excipients in the 1/3 or less of the excipients are preferably water-soluble excipients.
  • the 1/3 or less of the above may be usually 1/4 to 1/10 or less.
  • the acidifier-containing solution refers to a solution obtained by dissolving an acidifying agent with a small amount of solvent according to a routine operation in the art to facilitate the mixing step; the solvent may be water, an organic solvent or water and an organic solvent. Mixture.
  • the organic solvent is the same as described above.
  • the solid granule preparation can be directly obtained, or can be used as a preparation intermediate, and further solid preparations such as tablets or capsules can be obtained through further conventional steps.
  • the present invention also relates to a solid preparation prepared by the above method.
  • the reagents and starting materials used are commercially available.
  • the positive progress of the invention is that the preparation method of the invention avoids the defects of serious pollution, large loss and serious safety hazard caused by mechanical pulverization treatment, and achieves reduction of water insolubility and/or poor water solubility during granulation.
  • the method is easy to operate, has a high safety factor, and is easy to be applied to industrial production.
  • the solid active preparation of the present invention has a small particle size, excellent dissolution characteristics, high bioavailability, small individual difference, and also good stability and content uniformity. detailed description
  • the experimental methods in the following examples which do not specify the specific conditions are usually in accordance with conventional conditions or in accordance with the conditions recommended by the manufacturer.
  • the dosage form specification is based on the content of the active ingredient of the drug, such as 2 mg/tablet, which means that each tablet contains 2 mg of the active ingredient of the drug.
  • the unit of use is gram and the percentage is the mass percentage.
  • the mass percentage of the pharmaceutically active ingredient and the solvent is the mass percentage of the wet granulated dry material.
  • the amount of the solvent includes water in an aqueous solution of an acidifying agent and an alkalizing agent.
  • the coating material is a premix of the gastric coating material - Opadry. Comparative Example 1 and Example 1 Indapamide particle formulation and preparation method (Indapamide molecular weight: 365.83)
  • Example 4 Indapamide granule formula and preparation method
  • Example 5 Indapamide Tablets (2.5 mg/tablet) Formulation and Preparation Method
  • magnesium stearate and talc powder are added to form a soft material, which is extruded and granulated, and the wet granules are dried.
  • the mixture was added to the Opadry in the water while stirring, and magnesium stearate and talc powder were added and then compressed. Powder, continue to stir for 45 minutes after the addition, add Opadry powder in water while stirring, add the coating solution of 19% concentration, continue to stir for 45 minutes after the core, and prepare the film with 19wt% concentration. Coating.
  • the coating liquid is film coated on the core.
  • Example 10 Indapamide Capsule (2.5 mg/granule) Formulation and Preparation Method The particles before the tableting of Example 6 were passed through a 30 mesh sieve, uniformly mixed, and then filled. Comparative Example 3 Glipizide granule formulation and preparation method (glipizide molecular weight 445.54)
  • Example 13 Drug glipizide 2.5 (2.3%, micronized treatment) Glipizide 2.5 (2.2%, no pretreatment) Lactose 100, povidone K30 2, lactose lactose 100, polydimensional Ketone ⁇ 30 2, magnesium stearate 0.5, accessories
  • the sodium sulphate solution is formulated into a medicated alkaline solution, and 25% of the sugar is added and uniformly mixed, and the povidone ⁇ 30 is added.
  • lactose The amount of lactose is stirred evenly, and 10% salt is added with stirring to prepare an aqueous solution for stirring to form a soft material.
  • the aqueous acid solution is added to the 75% amount of lactose and stirred to process the granules.
  • the wet granules are dried and then granulated.
  • Example 15 glipizide tablets (5 mg / tablet) formula and preparation method
  • Example 16 glipizide capsule (2.5 mg / granule) formula and preparation method The granules before the tableting of Example 14 were passed through a 30 mesh sieve, and the mixture was uniformly mixed and then filled.
  • Example 17 Folic acid granule formula and preparation method (folic acid molecular weight 441.4) ) Comparative Example 5 and Example 18 Folic acid granule formulation and preparation method (folic acid molecular weight 441.4)
  • Example 24 Folic acid tablet (5 mg / tablet) formula and preparation method
  • Example 28 Methotrexate tablets (2.5 mg / tablet) formula and preparation method
  • Example 37 Benzyl fluorothiazide tablets (2.5 mg / tablet) formulation and preparation method
  • Example 38 Benzyl fluorothiazide particle formulation and preparation method
  • Example 39 Benzyl fluorothiazide tablets (5 mg / tablet) formulation and preparation method
  • Example 40 Indapamide Tablets (2.5 mg/tablet) Formulation and Preparation Method
  • Test equipment BT-9300S laser particle size distribution instrument; BT-800 automatic cycle injection system.
  • Test conditions The medium in the circulating injection system is water, the volume is about 570ml, and the centrifugal pump has a rotation speed of 1600rpm.
  • Test method Take about 2g of particles, add to the circulating injection system, make the absorbance of the system reach about 15%, turn on the ultrasonic dispersion for 3 minutes, and test the sample for 6 consecutive times to obtain the average particle size.
  • D10, D50 and D90 are the corresponding particle sizes when the cumulative particle size distribution percentage reaches 10%, 50% and 90%, respectively.
  • the intrinsic average particle size of indapamide in the indapamide particles obtained by the method of the present invention is reduced to 8.5 to 21.8% of the particle diameter of the drug substance, reaching 4.78 to 12.25 ⁇ m.
  • the average volume fraction of folic acid in the folic acid granules obtained by the method of the present invention is reduced to 15.9 to 34.6% of the particle size of the raw material treated with the fine powder, and is 0.89 to 1.94 ⁇ m.
  • the volume average particle diameter of methotrexate in the methotrexate particles obtained by the method of the present invention is reduced to 5.2 to 10.9% of the particle diameter of the drug substance, which is 4.43 to 9.37 ⁇ m.
  • Dissolution method Take the sample, according to the dissolution method (Chinese Pharmacopoeia 2010 edition two appendix XC second method), the dissolution solution 900 ml, take 0.2mol / l potassium dihydrogen phosphate solution 250ml, add 0.2mol / KOH
  • the sodium solution was diluted with water to 1000 ml of 118 m, the pH was adjusted to 6.8, the rotation speed was 100 rpm, and the control solution was prepared according to the law.
  • the spectrophotometry (Chinese Pharmacopoeia 2010 edition two appendix IV A)
  • the absorbance was measured at a wavelength of 240 nm, and the amount of dissolution per tablet was calculated.
  • Dissolution method (1) Take the sample, according to the dissolution method (Chinese Pharmacopoeia 2010 edition two appendix XC second method), the eluate is phosphate buffer (pH 7.4) 500ml, the rotation speed is 100 rpm , operate according to law, and prepare a control solution. According to the spectrophotometry (Chinese Pharmacopoeia 2010 edition two appendix IV A), the absorbance was measured at a wavelength of 222 nm, and the amount of dissolution per tablet was calculated.
  • Dissolution method (2) Take the sample, according to the dissolution method (Chinese Pharmacopoeia 2010 edition two appendix XC second method), the eluate is water 500ml, the rotation speed is 100 rpm, operate according to the law, and prepare the control solution . According to the spectrophotometry (Chinese Pharmacopoeia 2010 edition two appendix IV A), the absorbance was measured at a wavelength of 222 nm, and the amount of dissolution per tablet was calculated.
  • Dissolution method (1) Take the sample, according to the dissolution method (Chinese Pharmacopoeia 2010 edition two appendix XC second method), the eluate is phosphate buffer (pH 6.8) buffer 900ml, the rotation speed is every minute 100 rpm, operate according to law, and prepare a control solution. According to the spectrophotometry (Chinese Pharmacopoeia 2010 edition two appendix IV A), the absorbance is measured at a wavelength of 281 nm, and the dissolution of each tablet is calculated.
  • Dissolution method (2) Take the sample, according to the dissolution method (Chinese Pharmacopoeia 2010 edition two appendix XC second method), the eluate is 900ml of water, the rotation speed is 100 rpm, operate according to the law, and prepare the control solution . According to the spectrophotometry (Chinese Pharmacopoeia 2010 edition two appendix IV A), the absorbance was measured at a wavelength of 281 nm, and the amount of dissolution per tablet was calculated. Dissolution (%)
  • test samples were placed in high-density polyethylene plastic bottles, sealed, placed in an accelerated inspection box, and subjected to an accelerated test for 3 months at a temperature of 40 ° C ⁇ 2 ° C and a relative humidity of 75% ⁇ 5%. Stability determination of related items.
  • Method for determining the substance Protect from light. Take the appropriate amount of fine powder, add appropriate amount of mobile phase, shake in a hot water bath for 5 minutes, dissolve indapamide, dilute with mobile phase to make a solution containing about 0.5 mg of indapamide per 1 ml, filter After that, the filtrate was taken as the test sample. According to high performance liquid chromatography (Chinese Pharmacopoeia 2010 edition two appendix V D), octadecyl silicon germanium bonded silica was used as a filler and determined separately. Calculated according to the area normalization method.
  • the dissolution test method was the same as in the effect example 2.
  • Determination of content uniformity Take 1 tablet of this product, place it in the milk, add appropriate amount of ethanol, grind, and transfer it to 100ml volumetric flask with ethanol, shake it, dissolve indapamide, dilute with ethanol to scale Shake well, filter, and accurately measure 10ml of the filtrate. Place in a 50ml volumetric flask, dilute to the mark with ethanol, shake well, take the reference solution under the solution and the content determination, and observe the UV-visible spectrophotometry. Chinese Pharmacopoeia 2010 edition two appendix IV A), the absorbance is measured at a wavelength of 242 nm, calculated.
  • Determination of content uniformity Take 1 piece of this product, grind it, add phosphate buffer (pH 7.4), grind it in an appropriate amount, and transfer it to a 200ml volumetric flask with phosphate buffer (pH 7.4). Shake well. , filtered, take the filtrate as the test solution; take the appropriate amount of glipizide reference substance, the same method to make a solution containing about 25 per 1ml, as a reference solution. The above two solutions were taken, and the absorbance was measured at a wavelength of 275 nm, and calculated.
  • Determination of content uniformity Take 1 piece of this product, place it in a 25ml volumetric flask, add about 15ml of 0.5% ammonia solution, heat in a hot water bath for 20 minutes, shake it to dissolve the folic acid, let cool, dilute with water to the scale Shake, filter, and take the filtrate as the test solution, according to high performance liquid chromatography (Chinese Pharmacopoeia 2010 edition two appendix VD), using 18 ⁇ ⁇ silicon germanium bonded silica as a filler, record the chromatogram
  • Another folic acid reference substance determined by the same method, according to the external standard method to calculate the content of the peak area, should be consistent with (Chinese Pharmacopoeia 2010 edition two appendix XE).
  • Determination of content uniformity Take 1 tablet of this product, place it in a mortar, grind it, add 0.4% sodium hydroxide solution, grind it, and transfer it to a 25ml volumetric flask with 0.4% sodium hydroxide solution, shake it thoroughly.

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Abstract

Disclosed is a process for preparing a solid medicine preparation and a solid medicine preparation therefrom. The preparation process uses an acid-alkali solventing-out dispersion technique comprising the steps of: dissolving a water insoluble and/or indissolvable acid active medicine ingredient in an alkaline solution containing an alkalizing agent to produce a medicine-containing alkaline solution; then uniformly mixing an auxiliary material and the medicine-containing alkaline solution to perform a wet granulation. The process avoids the disadvantages caused by a mechanical crushing treatment, such as serious pollution, large losses and potential safety hazards, by which the effect of reducing the particle size of the water insoluble and/or indissolvable acid active medicine ingredients can be achieved during preparation, and the solid produced has an excellent solventing-out characteristic, stability and content uniformity.

Description

一种药物固体制剂的制备方法及所得药物固体制剂 技术领域  Preparation method of pharmaceutical solid preparation and obtained medicine solid preparation technical field
本发明属于药物制剂领域, 具体涉及一种药物固体制剂的制备方法及 所得药物固体制剂。 背景技术  The invention belongs to the field of pharmaceutical preparations, and particularly relates to a preparation method of a solid pharmaceutical preparation and a obtained solid preparation of the medicament. Background technique
在药物制剂领域,药物活性成分的粒径对固体制剂的制备过程和质量密 切相关, 粒径的减小是提高药物制剂溶出度和含量均匀度的关键。在具体的 药物制剂的制备工艺中, 通常依据药物的溶解特性和生物膜通透性, 来选择 合适的药物活性成分的粒径。 例如, 若属于溶解性较差, 药物溶出是吸收限 速过程的药物, 可选择较小的粒径, 以促进药物的吸收。 在药物固体制剂的 制备工艺中, 时常涉及到对药物活性成分的粒径的选择控制。  In the field of pharmaceutical preparations, the particle size of the pharmaceutically active ingredient is closely related to the preparation process and quality of the solid preparation, and the reduction of the particle size is the key to improving the dissolution and content uniformity of the pharmaceutical preparation. In the preparation process of a specific pharmaceutical preparation, the particle size of a suitable pharmaceutically active ingredient is usually selected depending on the dissolution characteristics of the drug and the permeability of the biofilm. For example, if the solubility is poor, drug dissolution is a drug that absorbs the rate-limiting process, and a smaller particle size can be selected to promote drug absorption. In the preparation process of a pharmaceutical solid preparation, selective control of the particle size of the pharmaceutically active ingredient is often involved.
目前, 大多通过选择不同的机械粉碎方法及粉碎工艺条件, 以实现对药 物活性成分粒径的选择控制。万能粉碎机是一种在药物领域应用较广泛的粉 碎机, 对物料粉碎的作用以撞击力、 剪切力为主, 适用于多种中等硬度的干 燥物料, 处理后的平均粒径一般达到 100微米左右。  At present, most of the selection and control of the particle size of the active ingredient of the drug are achieved by selecting different mechanical pulverization methods and pulverization process conditions. The universal pulverizer is a pulverizer widely used in the field of medicine. The effect of crushing materials is mainly on impact force and shearing force. It is suitable for a variety of medium-hardness dry materials. The average particle size after treatment is generally 100. About micrometers.
但是, 机械粉碎的处理方法存在粉尘多、 污染环境和损耗大等问题。 对 于一些高活性药物, 还容易在机械粉碎过程中, 使操作人员产生不良反应, 存在严重的安全隐患。 例如, 吸入较低剂量的镇静安眠药物粉末即可快速产 生催眠效果, 在对这类药物进行粉碎处理时, 极易发生致操作人员快速催眠 的不良反应, 引发安全事故。 再例如, 在对一些高活性的激素或抗肿瘤等药 物进行粉碎处理时, 吸入或接触一定量的药物粉末, 极易使操作人员产生严 重的药物反应。  However, the treatment method of mechanical pulverization has problems such as a lot of dust, a polluted environment, and a large loss. For some highly active drugs, it is easy to cause adverse reactions in the mechanical pulverization process, and there are serious safety hazards. For example, inhalation of a lower dose of sedative sleeping pills powder can quickly produce hypnotic effects. When these drugs are pulverized, it is highly prone to cause an operator's rapid hypnosis and cause a safety accident. For example, when pulverizing some highly active hormones or anti-tumor drugs, inhaling or contacting a certain amount of the drug powder can easily cause a serious drug reaction by the operator.
对于一些难溶性药物, 平均粒径达到 100微米左右, 制得的固体制剂的 溶出特性尚达不到要求。 在机械粉碎处理的工艺中, 对于在固体制剂中含量较低 (如 5wt% ) 的高活性药物活性成分, 还涉及其与辅料混合的分散均匀性问题。 通常, 采 用将药物活性成分与辅料等量稀释逐步扩大的方法, 以使药物活性成分在固 体制剂中分散均匀。但该方法工艺操作繁琐, 同样会产生粉尘多、污染环境、 损耗大和劳动防护存在安全隐患等诸多问题。 For some poorly soluble drugs, the average particle size reaches about 100 microns, and the dissolution characteristics of the prepared solid preparations are not satisfactory. In the process of mechanical pulverization treatment, for a high active pharmaceutically active ingredient having a low content (e.g., 5 wt%) in a solid preparation, it also relates to the problem of dispersion uniformity of its mixing with an auxiliary material. Usually, a method of gradually diluting the pharmaceutically active ingredient and the auxiliary material in an equal amount is used to uniformly disperse the pharmaceutically active ingredient in the solid preparation. However, the method is cumbersome in process operation, and also causes many problems such as dust, environmental pollution, large loss, and safety hazards in labor protection.
此外,固体制剂的制备还需考虑产品的各种性能是否能满足需要。例如, 是否能保证较佳的含量均匀度。再例如,稳定性是固体制剂质量的考察重点, 其包括在固体制剂贮存期内, 药物活性成分的化学稳定性、 杂质的含量、 固 体制剂性状稳定性、 以及溶出稳定性等, 是否处在药品标准限度内。  In addition, the preparation of solid preparations also needs to consider whether the various properties of the product can meet the needs. For example, is it possible to ensure a better content uniformity? For example, stability is the focus of the quality of the solid preparation, including the chemical stability of the active ingredient, the content of impurities, the stability of the solid preparation, and the stability of dissolution during storage of the solid preparation, whether it is in the medicine Within the standard limits.
因此, 针对上述现有技术的缺陷, 亟待寻求一种既可避免机械粉碎处理 方法的上述缺陷, 又可保证固体制剂各种性能优良的制备方法。 发明内容  Therefore, in view of the above-mentioned drawbacks of the prior art, it is urgent to seek a preparation method which can avoid the above-mentioned drawbacks of the mechanical pulverization treatment method and which can ensure various properties of the solid preparation. Summary of the invention
本发明所要解决的技术问题是为了克服现有的固体制剂制备方法通过 机械粉碎的方式选择控制药物活性成分的粒径, 会造成环境污染, 存在严重 的安全隐患, 损耗大, 且所得固体药物制剂的溶出性等不够理想的缺陷, 而 针对水不溶性或水难溶性酸性药物, 提供一种操作更简便, 污染更小, 没有 前述安全隐患, 且能保证所制得的固体制剂具有优异的溶出特性、 稳定性和 含量均匀度的药物固体制剂的制备方法及所得药物固体制剂。  The technical problem to be solved by the present invention is to overcome the conventional method for preparing a solid preparation by mechanically pulverizing and controlling the particle size of the pharmaceutically active ingredient, which causes environmental pollution, has serious safety hazards, and has large loss, and the obtained solid pharmaceutical preparation The solubility is not ideal, and the water-insoluble or poorly water-soluble acidic drug provides a simpler operation, less pollution, no such safety hazard, and can ensure that the prepared solid preparation has excellent dissolution characteristics. , a method for preparing a solid pharmaceutical preparation having stability and content uniformity, and a solid pharmaceutical preparation obtained.
为解决上述技术问题, 本发明人另辟蹊径, 独特地采用酸 -碱溶析分散 技术 (Acid-Base Solventing-out Dispersion, A-BSoD ), 即用碱性溶液溶解 水不溶性和 /或水难溶性酸性药物,之后在制粒过程中,使药物回复固体状态, 从而避免了机械粉碎处理的诸多缺陷。 并且, 本发明人还意外发现, 该方法 所制得的水不溶性和 /或水难溶性酸性药物固体制剂具有优异的溶出特性、稳 定性和含量均匀度。  In order to solve the above technical problems, the present inventors have taken a different approach, uniquely using Acid-Base Solventing-out Dispersion (A-BSoD), which dissolves water-insoluble and/or poorly water-soluble acidic with an alkaline solution. The drug, which is then returned to the solid state during the granulation process, avoids many of the drawbacks of mechanical comminution. Further, the inventors have unexpectedly found that the water-insoluble and/or poorly water-soluble acidic pharmaceutical solid preparation obtained by the method has excellent dissolution characteristics, stability, and content uniformity.
本发明的药物固体制剂的制备方法包括如下步骤:将水不溶性和 /或水难 溶性酸性药物活性成分溶于含碱化剂的碱性溶液中,制得含药碱性液;之后, 将辅料和所述的含药碱性液均匀混合, 进行湿法制粒。 The method for preparing a pharmaceutical solid preparation of the present invention comprises the steps of: insoluble water and/or water The soluble acidic pharmaceutical active ingredient is dissolved in an alkaline solution containing an alkalizing agent to prepare a medicated alkaline liquid; thereafter, the auxiliary material and the medicated alkaline liquid are uniformly mixed to perform wet granulation.
本发明中,所述的水不溶性和 /或水难溶性酸性药物活性成分选自现有的 各种符合上述性质的药物活性成分,包括同时具有酸性基团和碱性基团的两 性药物活性成分。 本领域中, 所述的酸性药物活性成分大都为弱酸类药物活 性成分。 本发明优选活性较高、 在固体制剂中含量较低 (一般为 20%以下, 较佳的为 10%以下, 更佳的为 5%以下, 百分比为质量百分比) 的水不溶性 或水难溶性酸性药物活性成分。 更具体的, 本发明优选但不限于格列吡嗪、 叶酸、 布美他尼、 双氯非那胺、 异卡波肼、 苄氟噻嗪、对氟噻嗪、 甲氨蝶呤、 维生素 H、 己垸雌酚、 吲达帕胺、 呋塞米、 硫鸟剽呤、 别嘌醇、 格列喹酮、 辛伐他汀、 来氟米特、 氢氯噻嗪或苯巴比妥。  In the present invention, the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient is selected from various existing pharmaceutically active ingredients satisfying the above properties, including an amphoteric active ingredient having both an acidic group and a basic group. . In the art, most of the acidic pharmaceutically active ingredients are weak acid active ingredients. The present invention preferably has a high activity and a low content in a solid preparation (generally 20% or less, preferably 10% or less, more preferably 5% or less, and a percentage by mass) of water-insoluble or poorly water-soluble acidity. Pharmaceutical active ingredient. More specifically, the present invention is preferably, but not limited to, glipizide, folic acid, bumetanide, diclofenac, isocarbopurine, benzfluorothiazide, p-fluorothiazide, methotrexate, vitamin H , hexaerythritol, indapamide, furosemide, thioguanine, allopurinol, gliclazone, simvastatin, leflunomide, hydrochlorothiazide or phenobarbital.
根据水不溶性和 /或水难溶性酸性药物活性成分在固体制剂中的常规含 量, 即可确定制备过程中,水不溶性和 /或水难溶性酸性药物活性成分占湿法 制粒干物料的质量百分比。根据需要, 除水不溶性和 /或水难溶性酸性药物活 性成分之外, 还可加入其他药物活性成分制成复方固体制剂。  Based on the conventional content of the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient in the solid preparation, the mass percentage of the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient in the wet-processed dry material can be determined during the preparation. In addition to the water-insoluble and/or poorly water-soluble acidic drug active ingredients, other pharmaceutically active ingredients may be added to prepare a compound solid preparation.
本发明中,所述的碱化剂是指能使水不溶性和 /或水难溶性酸性药物活性 成分完全溶解于含碱化剂的碱性溶液中的试剂。 根据本领域常识, 所述的碱 化剂应为药学上可接受的,且与水不溶性和 /或水难溶性酸性药物活性成分相 配伍的试剂。 本发明中, 所述的配伍是指可共存, 无不良影响。 所述的碱化 剂可为单一的碱化剂, 也可为两种以上成分组成的复合碱化剂, 可选自各种 碱, 如无机碱和 /或有机碱, 强碱和 /或弱碱, 较佳的选自氢氧化钠、 氢氧化 钾、 碳酸钠、 碳酸钾、 乙醇钠、 甲葡胺、 二乙醇胺和三乙醇胺中的一种或多 种。 本发明特别优选下述碱化剂:  In the present invention, the alkalizing agent refers to a reagent capable of completely dissolving a water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient in an alkaline solution containing an alkalizing agent. According to common knowledge in the art, the basifying agent should be a pharmaceutically acceptable agent compatible with water insoluble and/or poorly water soluble acidic pharmaceutical active ingredients. In the present invention, the compatibility means coexistence without adverse effects. The alkalizing agent may be a single alkalizing agent or a complex alkalizing agent composed of two or more components, and may be selected from various bases such as inorganic bases and/or organic bases, strong bases and/or weakeners. The base is preferably selected from one or more of sodium hydroxide, potassium hydroxide, sodium carbonate, potassium carbonate, sodium ethoxide, meglumine, diethanolamine and triethanolamine. The basifying agent described below is particularly preferred in the present invention:
当水不溶性和 /或水难溶性酸性药物活性成分为吲达帕胺时,所述的碱化 剂为氢氧化钠、 氢氧化钾或乙醇钠, 最佳的为氢氧化钠。  When the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient is indapamide, the alkalizing agent is sodium hydroxide, potassium hydroxide or sodium ethoxide, most preferably sodium hydroxide.
当水不溶性和 /或水难溶性酸性药物活性成分为格列吡嗪时,所述的碱化 剂为氢氧化钠或氢氧化钾, 最佳的为氢氧化钠。 When the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient is glipizide, the alkalization The agent is sodium hydroxide or potassium hydroxide, and the most preferred is sodium hydroxide.
当水不溶性和 /或水难溶性酸性药物活性成分为叶酸时,所述的碱化剂为 氢氧化钠、 氢氧化钾、 乙醇钠、 碳酸钠或碳酸钾, 最佳的为氢氧化钠或碳酸 钠。  When the water-insoluble and/or water-insoluble acidic pharmaceutical active ingredient is folic acid, the alkalizing agent is sodium hydroxide, potassium hydroxide, sodium ethoxide, sodium carbonate or potassium carbonate, and most preferably sodium hydroxide or carbonic acid. sodium.
当水不溶性和 /或水难溶性酸性药物活性成分为甲氨蝶呤时,所述的碱化 剂为氢氧化钠、 氢氧化钾、 碳酸钠或碳酸钾。  When the water-insoluble and/or water-insoluble acidic pharmaceutical active ingredient is methotrexate, the alkalizing agent is sodium hydroxide, potassium hydroxide, sodium carbonate or potassium carbonate.
当水不溶性和 /或水难溶性酸性药物活性成分为苄氟噻嗪时,所述的碱化 剂为氢氧化钠或氢氧化钾。  When the water-insoluble and/or water-insoluble acidic pharmaceutical active ingredient is benzfluorothiazide, the alkalizing agent is sodium hydroxide or potassium hydroxide.
所述的碱化剂的用量至少为能使水不溶性和 /或水难溶性酸性药物活性 成分完全溶解的最小量,较佳的为此最小量的 1~1.5倍,最佳的为 1~1.05倍。 可溶解水不溶性和 /或水难溶性酸性药物活性成分的碱化剂的量与诸多因素 有关, 如碱化剂种类、溶剂种类、碱化剂中可与水不溶性和 /或水难溶性酸性 药物活性成分的酸性中心相结合的负离子数、 以及含药碱性液配制条件(如 温度、 时间、 加料顺序、 搅拌方式) 等有关。 其中, 所述的酸性中心是指水 不溶性和 /或水难溶性酸性药物活性成分中可与碱化剂分子中负离子结合的 基团或部位。 因此, 上述最小量是指在同一溶剂和含药碱性液配制条件下, 对某种水不溶性和 /或水难溶性酸性药物活性成分而言,某种碱化剂可将其溶 解的最小量, 通过简单的常规方法即可确定该最小量: 在同一溶剂和含药碱 性液配制条件下,采用逐渐增大某种碱化剂的用量溶解某种水不溶性和 /或水 难溶性酸性药物活性成分, 刚好完全溶解时, 即为最小量。 本发明人经大量 实验摸索得出,具体而言,碱化剂与水不溶性和 /或水难溶性酸性药物活性成 分的摩尔比值一般为 0.1~2.5, 大多为 0.9~1.5, 本发明特别优选下述用量的 碱化剂:  The alkalizing agent is used in an amount at least the minimum amount which can completely dissolve the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient, preferably 1 to 1.5 times the minimum amount, and most preferably 1 to 1.05. Times. The amount of the alkalizing agent which can dissolve the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient is related to various factors such as the type of alkalizing agent, the type of solvent, the water-insoluble and/or poorly water-soluble acidic drug in the alkalizing agent. The number of negative ions combined with the acid center of the active ingredient and the preparation conditions of the medicated alkaline solution (such as temperature, time, feeding sequence, stirring method) and the like. Here, the acidic center means a group or a portion of the water-insoluble and/or water-insoluble acidic drug active ingredient which can bind to a negative ion in the alkalizing agent molecule. Therefore, the above minimum amount refers to the minimum amount of an alkalizing agent which can be dissolved by a certain alkali-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient under the same solvent and medicated alkaline solution. The minimum amount can be determined by a simple conventional method: in the same solvent and the medicated alkaline solution, the amount of the alkalizing agent is gradually increased to dissolve a certain water-insoluble and/or poorly water-soluble acidic drug. The active ingredient, when completely dissolved, is the minimum amount. The present inventors have found through a large number of experiments that, in particular, the molar ratio of the alkalizing agent to the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient is generally from 0.1 to 2.5, and most of from 0.9 to 1.5, and the present invention is particularly preferred. The amount of alkalizing agent:
对于吲达帕胺, 特别优选其摩尔量 0.7~1.1倍的氢氧化钠或乙醇钠。 对于格列吡嗪, 特别优选其摩尔量 0.95~1.1倍的氢氧化钠。  For indapamide, sodium hydroxide or sodium ethoxide having a molar amount of 0.7 to 1.1 times is particularly preferred. For glipizide, sodium hydroxide having a molar amount of 0.95 to 1.1 times is particularly preferable.
对于叶酸,特别优选其摩尔量 1.8~2.1倍的氢氧化钠或其摩尔量 0.95~1.1 倍的碳酸钠或碳酸钾。 For folic acid, sodium hydroxide having a molar amount of 1.8 to 2.1 times or a molar amount of 0.95 to 1.1 is particularly preferable. Times sodium carbonate or potassium carbonate.
对于甲氨蝶呤, 特别优选其摩尔量 1.4~1.6 倍的氢氧化钠或摩尔量 0.85~1.1倍的碳酸钠。  For methotrexate, sodium hydroxide having a molar amount of 1.4 to 1.6 times or sodium carbonate having a molar amount of 0.85 to 1.1 times is particularly preferable.
对于苄氟噻嗪, 特别优选其摩尔量 0.9~1.6倍的氢氧化钠。  For the benzfluorothiazine, sodium hydroxide having a molar amount of 0.9 to 1.6 times is particularly preferable.
本发明中, 所述的含碱化剂的碱性溶液中的溶剂可为水、 有机溶剂或者 水和有机溶剂的混合液。 根据本领域常识, 选择的溶剂应为碱化剂中离子可 解离的溶剂。例如,碱化剂为无机物时,可选择水或水和有机溶剂的混合液; 碱化剂为有机物时, 可为水、 水和有机溶剂的混合液、 或者有机溶剂。 若药 物活性成分在某些有机溶剂中有优于在水中的溶解性, 较佳的选择水与该有 机溶剂的混合液, 以利于药物活性成分的溶解, 减少碱化剂或溶剂的用量, 利于后续制粒步骤的操作。所述的有机溶剂根据其对水不溶性和 /或水难溶性 酸性药物活性成分的溶解性优于水的原则在药剂领域可接受的溶剂中进行 选择,较佳的为能与水混溶的有机溶剂,如药剂领域常用的水溶性醇类溶剂, 如乙醇、 丙二醇、 丙三醇、 丙酮、 异丙醇或叔丁醇等, 优选乙醇、 丙酮、 丙 二醇和丙三醇中的一种或多种, 特别优选乙醇。 水与有机溶剂的混合液中, 有机溶剂的浓度可任意选择。所述的碱性溶液中溶剂的用量以至少使得药物 可溶解, 至少为湿法制粒所需制粒液最小量, 一般为湿法制粒干物料的质量 百分比 5~100%, 较佳的为 10~50%。  In the present invention, the solvent in the alkalizing agent-containing alkaline solution may be water, an organic solvent or a mixture of water and an organic solvent. According to common knowledge in the art, the solvent selected should be an ion dissociable solvent in the alkalizing agent. For example, when the alkalizing agent is an inorganic substance, water or a mixed liquid of water and an organic solvent may be selected; and when the alkalizing agent is an organic substance, it may be a mixed liquid of water, water and an organic solvent, or an organic solvent. If the pharmaceutically active ingredient is superior to the solubility in water in some organic solvents, it is preferred to select a mixture of water and the organic solvent to facilitate dissolution of the active ingredient of the drug, and to reduce the amount of alkalizing agent or solvent, which is advantageous for The operation of the subsequent granulation step. The organic solvent is selected according to the principle that its solubility in water-insoluble and/or poorly water-soluble acidic pharmaceutically active ingredients is superior to water in a solvent acceptable for the pharmaceutical field, preferably organically miscible with water. a solvent, such as a water-soluble alcohol solvent commonly used in the pharmaceutical field, such as ethanol, propylene glycol, glycerol, acetone, isopropanol or tert-butanol, preferably one or more of ethanol, acetone, propylene glycol and glycerol. Particularly preferred is ethanol. In the mixture of water and an organic solvent, the concentration of the organic solvent can be arbitrarily selected. The amount of the solvent in the alkaline solution is such that at least the drug is soluble, at least the minimum amount of granulating liquid required for wet granulation, generally 5 to 100% by mass of the dry granulated dry material, preferably 10 ~50%.
在制备含药碱性液时, 可加入一些辅料, 如粘合剂、 表面活性剂、 增溶 剂和固体分散体的水溶性载体等。较佳的,在将水不溶性和 /或水难溶性酸性 药物活性成分溶于含碱化剂的碱性溶液中的同时和 /或之后,还加入表面活性 剂、 增溶剂和固体分散体的水溶性载体中的一种或多种, 然后将所得含药碱 性液进行后续步骤, 即与辅料均匀混合, 进行湿法制粒。 其中, 将固体分散 体的水溶性载体与水不溶性和 /或水难溶性酸性药物活性成分同时加入含碱 化剂的碱性溶液中时,此时加入的固体分散体的水溶性载体的量需控制在能 保证水不溶性和 /或水难溶性酸性药物活性成分完全溶解于含碱化剂的碱性 溶液中的量以下; 之后还可以再向该溶液中加入固体分散体的水溶性载体, 当加入量较大时, 所得含药酸性液可能为悬浊液或粘稠液形式。 本发明特别 优选加入聚维酮、 聚乙二醇 (优选聚乙二醇 400-8000)、 十二垸基硫酸钠、 泊洛沙姆、 聚氧乙烯蓖麻油、 吐温(优选吐温 80)、 硬脂酸聚烃氧 40酯、 乳 糖、甘露醇、蔗糖、羟丙基 -β-环糊精、 β-环糊精和麦芽糖醇中的一种或多种。 所述的表面活性剂和 /或增溶剂的加入量较佳的为水不溶性和 /或水难溶性酸 性药物活性成分质量的 0.05~5倍, 更佳的为 0.05~2倍。 所述的固体分散体 的水溶性载体的加入量较佳的为水不溶性和 /或水难溶性酸性药物活性成分 质量的 0.5~20倍, 更佳的为 0.5~2倍。 按上述操作加入表面活性剂和 /或增 溶剂,可增加水不溶性和 /或水难溶性酸性药物活性成分在碱性溶液中的溶解 度, 减少溶剂用量, 利于后续制粒步骤的操作。 更值得一提的是, 按上述操 作加入表面活性剂、 增溶剂和固体分散体的水溶性载体中的一种或多种, 尤 其是固体分散体的水溶性载体可使所得固体制剂的溶出特性更佳。 In the preparation of the medicated alkaline solution, some excipients such as a binder, a surfactant, a solubilizing agent, and a water-soluble carrier of the solid dispersion may be added. Preferably, the water-insoluble and/or water-insoluble acidic pharmaceutically active ingredient is dissolved in the alkaline solution containing the alkalizing agent while and/or after, the water-soluble solution of the surfactant, the solubilizing agent and the solid dispersion is further added. One or more of the carrier materials are then subjected to a subsequent step of uniformly mixing the excipients with the excipients for wet granulation. Wherein, when the water-soluble carrier of the solid dispersion and the water-insoluble and/or poorly water-soluble acidic pharmaceutically active ingredient are simultaneously added to the alkaline solution containing the alkalizing agent, the amount of the water-soluble carrier of the solid dispersion to be added at this time is required. Controlled to ensure that the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredients are completely dissolved in the alkaline agent-containing alkaline The amount in the solution is below; after that, a water-soluble carrier of the solid dispersion may be further added to the solution, and when the amount added is large, the obtained drug-containing acidic liquid may be in the form of a suspension or a viscous liquid. Particularly preferred in the present invention are the addition of povidone, polyethylene glycol (preferably polyethylene glycol 400-8000), sodium dodecyl sulfate, poloxamer, polyoxyethylene castor oil, Tween (preferably Tween 80). And one or more of polyoxyl 40 stearate, lactose, mannitol, sucrose, hydroxypropyl-β-cyclodextrin, β-cyclodextrin and maltitol. The surfactant and/or solubilizer is preferably added in an amount of 0.05 to 5 times, more preferably 0.05 to 2 times, the mass of the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient. The water-soluble carrier of the solid dispersion is preferably added in an amount of from 0.5 to 20 times, more preferably from 0.5 to 2 times, the mass of the water-insoluble and/or water-insoluble acidic pharmaceutical active ingredient. By adding a surfactant and/or a solubilizing agent as described above, the solubility of the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient in an alkaline solution can be increased, the amount of the solvent can be reduced, and the operation of the subsequent granulation step can be facilitated. It is further worth mentioning that one or more of the water-soluble carriers of the surfactant, the solubilizer and the solid dispersion are added as described above, in particular, the water-soluble carrier of the solid dispersion can make the dissolution characteristics of the obtained solid preparation. Better.
较佳的, 在制备含药碱性液时, 可以通过热水浴等常规加热方法, 适当 升高含药碱性液的配制温度, 以利于药物活性成分的溶解。 以水为溶剂时, 较佳的升高至 40~80°C。 以水和有机溶剂的混合溶液为溶剂时, 较佳的升高 为 40~70°C。 以乙醇为溶剂时, 较佳的升高为 30~50°C。  Preferably, in the preparation of the medicated alkaline solution, the preparation temperature of the medicated alkaline solution may be appropriately raised by a conventional heating method such as a hot water bath to facilitate dissolution of the pharmaceutically active ingredient. When water is used as the solvent, it is preferably raised to 40 to 80 °C. When a mixed solution of water and an organic solvent is used as a solvent, the preferred increase is 40 to 70 °C. When ethanol is used as the solvent, the preferred increase is 30 to 50 °C.
本发明中, 所述的辅料可选自本领域任何已知的并广泛使用的辅料, 如 填充剂、 粘合剂、 崩解剂、 吸附剂和润滑剂等等。 所述的辅料的含量可按照 本领域常规或现有知识进行选择。 其中, 所述的填充剂较佳的为乳糖、 微晶 纤维素、 淀粉、 预胶化淀粉、 甘露醇、 蔗糖和麦芽糖醇中的一种或多种。 所 述的粘合剂较佳的为羟丙甲纤维素、 聚维酮、 甲基纤维素和羟丙纤维素中的 一种或多种。 所说的崩解剂较佳的为羧甲淀粉钠、 低取代羟丙纤维素、 交联 聚乙烯吡咯垸酮和交联羧甲基纤维素钠中的一种或多种。所述的润滑剂较佳 的为硬脂酸镁、 微粉硅胶 (胶态二氧化硅)、 滑石粉或硬脂酸富马酸钠。  In the present invention, the excipient may be selected from any of the excipients known and widely used in the art, such as fillers, binders, disintegrants, adsorbents, lubricants and the like. The amount of the excipients can be selected according to routine or prior knowledge in the art. Wherein the filler is preferably one or more of lactose, microcrystalline cellulose, starch, pregelatinized starch, mannitol, sucrose and maltitol. The binder is preferably one or more of hypromellose, povidone, methylcellulose and hydroxypropylcellulose. The disintegrant is preferably one or more of sodium carboxymethyl starch, low-substituted hydroxypropyl cellulose, cross-linked polyvinylpyrrolidone and croscarmellose sodium. The lubricant is preferably magnesium stearate, micronized silica gel (colloidal silica), talc or sodium stearate.
在将辅料和所述的含药碱性液均匀混合, 进行湿法制粒的步骤时, 还可 加入酸化剂, 使酸化剂与含药碱性液的混合液的碱性相对于含药碱性液的碱 性降低。 When the auxiliary material and the medicated alkaline liquid are uniformly mixed and subjected to the wet granulation step, The acidifying agent is added to lower the alkalinity of the mixture of the acidifying agent and the medicated alkaline solution with respect to the alkalinity of the medicated alkaline solution.
根据本领域常识, 所述酸化剂都应为药学上可接受的, 且与水不溶性和 /或水难溶性酸性药物活性成分相配伍的试剂。较佳的,本发明优选下述类型 的碱化剂和酸化剂的组合: 所述的碱化剂为无机强碱、 有机强碱或无机中强 碱, 所述的酸化剂为无机强酸 (如盐酸)。  According to common knowledge in the art, the acidulant should be a pharmaceutically acceptable agent compatible with water insoluble and/or poorly water soluble acidic pharmaceutical active ingredients. Preferably, the present invention is preferably a combination of an alkalizing agent and an acidifying agent of the following type: the alkalizing agent is an inorganic strong base, an organic strong base or an inorganic medium strong base, and the acidifying agent is an inorganic strong acid (such as hydrochloric acid).
所述的酸化剂的量为至少能使酸化剂与含药碱性液的混合液的碱性相 对于含药碱性液的碱性降低的量。 较佳的, 碱化剂与酸化剂的用量满足下述 关系: 式 1所得值为 0.01~1.5, 较佳的为 0.2~1.1, 更佳的为 0.9~1.1。  The amount of the acidifying agent is such an amount that at least the alkalinity of the mixture of the acidifying agent and the medicated alkaline liquid is lowered relative to the alkalinity of the medicated alkaline liquid. Preferably, the amount of the alkalizing agent and the acidifying agent satisfies the following relationship: The value obtained by the formula 1 is 0.01 to 1.5, preferably 0.2 to 1.1, more preferably 0.9 to 1.1.
(酸化剂摩尔数 xA ) I (碱化剂摩尔数 xB ) 式 1 其中, A为酸化剂分子中的氢离子数, B为碱化剂分子阴离子总价态数。  (Number of moles of acidifying agent xA) I (molar number of alkalizing agent xB) Formula 1 wherein A is the number of hydrogen ions in the acidifying agent molecule, and B is the total number of valence states of the alkalizing agent molecule anion.
本发明特别优选式 1值为 0.9~1.1的下述碱化剂和酸化剂的组合: 氢氧 化钠和盐酸、 氢氧化钾和盐酸、 乙醇钠和盐酸、 碳酸钠和盐酸、 以及碳酸钾 和盐酸。  The present invention particularly preferably has a combination of the following alkalizing agent and acidifying agent of the formula 1 having a value of 0.9 to 1.1: sodium hydroxide and hydrochloric acid, potassium hydroxide and hydrochloric acid, sodium ethoxide and hydrochloric acid, sodium carbonate and hydrochloric acid, and potassium carbonate and hydrochloric acid. .
对于某些水不溶性和 /或水难溶性酸性药物活性成分,加入酸化剂,能更 有利于固体制剂的稳定性。而对于某些水不溶性和 /或水难溶性酸性药物活性 成分, 在配方中不加酸化剂或酸化剂用量很少的情况下, 固体制剂仍然可具 有较佳的稳定性, 但在不影响制剂稳定性的前提下, 适当增加酸化剂用量降 低碱性, 能有利于缓和固体制剂的酸碱度。  For certain water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredients, the addition of an acidifying agent is more advantageous for the stability of the solid preparation. For certain water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredients, the solid preparation can still have better stability without adding an acidifying agent or an acidifying agent in the formulation, but does not affect the preparation. Under the premise of stability, appropriately increasing the amount of acidifier to reduce alkalinity can help to alleviate the pH of solid preparations.
本发明中, 所述的湿法制粒可按本领域属于湿法制粒范畴的各种制粒方 法的常规步骤和条件进行, 如挤压制粒 (如摇摆机挤压、 螺旋挤压或旋转挤 压等)、 搅拌制粒、 流化喷雾制粒或离心喷雾制粒等。 对于在固体制剂中剂量 较大(一般大于 10% ) , 或在含碱化剂的碱性溶液中溶解度较小, 需较大量的 碱性溶液才可溶解完全的水不溶性和 /或水难溶性酸性药物活性成分, 可选择 对制粒溶液量限制小的湿法制粒工艺, 如流化喷雾制粒或离心喷雾制粒。  In the present invention, the wet granulation can be carried out according to the conventional steps and conditions of various granulation methods in the field of wet granulation in the art, such as extrusion granulation (such as swinging machine extrusion, spiral extrusion or rotary extrusion). Pressing, etc., stirring granulation, fluidized spray granulation or centrifugal spray granulation. For larger doses in solid preparations (generally greater than 10%) or less soluble in alkaline solutions containing alkalizing agents, larger amounts of alkaline solution are required to dissolve complete water insolubility and/or poor water solubility. The acidic pharmaceutically active ingredient may be selected from a wet granulation process in which the amount of the granulation solution is limited, such as fluidized spray granulation or centrifugal spray granulation.
当使用酸化剂时,较佳的按下述方式中的任一种进行具体操作:方式(1 ) 将酸化剂或含酸化剂的溶液和辅料均匀混合, 再与含药碱性液均匀混合, 进 行挤压制粒或搅拌制粒; 方式 (2 ) 将含药碱性液与, 酸化剂或含酸化剂的 溶液均匀的混合, 得制粒液, 之后再将该制粒液与辅料进行挤压制粒、 搅拌 制粒、 流化喷雾制粒或离心喷雾制粒等; 方式 (3 ) 将含药碱性液与辅料均 匀的混合,之后再与含酸化剂的溶液均匀的混合,进行挤压制粒或搅拌制粒; 方式 (4)将含药碱性液与, 1/3以下的辅料, 以及酸化剂或含酸化剂的溶液 均匀的混合 (具体操作可为: 先将 1/3以下的辅料和酸化剂或含酸化剂的溶 液均匀混合, 再将所得混合物与含药碱性液混合, 或者, 先将 1/3以下的辅 料和含药碱性液混合, 再与酸化剂或含酸化剂的溶液均匀混合), 之后再与 剩余辅料混合进行挤压制粒或搅拌制粒。 所述的 1/3以下的辅料中的辅料较 佳的为水溶性辅料。 所述的 1/3以下通常可为 1/4~1/10以下。 所述的含酸化 剂的溶液是指, 按本领域常规操作, 用少量溶剂溶解酸化剂所得的溶液, 以 方便进行混匀步骤;所述的溶剂可为水、有机溶剂或水和有机溶剂的混合液。 所述的有机溶剂同前述。 When an acidulant is used, it is preferred to carry out the specific operation in any of the following ways: mode (1) The acidifying agent or the acidifying agent-containing solution and the auxiliary material are uniformly mixed, and then uniformly mixed with the medicated alkaline liquid, and subjected to extrusion granulation or stirring granulation; and (2) the medicated alkaline liquid and the acidifying agent or The solution of the acidifying agent is uniformly mixed to obtain a granulating liquid, and then the granulating liquid and the auxiliary material are subjected to extrusion granulation, agitation granulation, fluidized spray granulation or centrifugal spray granulation; and the method (3) will contain The alkaline solution of the drug is uniformly mixed with the auxiliary material, and then uniformly mixed with the solution containing the acidifying agent, and subjected to extrusion granulation or stirring granulation; and (4) the medicated alkaline liquid and the auxiliary material of 1/3 or less And the acidifying agent or the acidifying agent-containing solution is uniformly mixed (the specific operation may be: firstly mixing 1/3 or less of the auxiliary material with the acidifying agent or the acidifying agent-containing solution, and then mixing the obtained mixture with the medicated alkaline liquid; Or, firstly mix 1/3 or less of the auxiliary material and the medicated alkaline liquid, and then uniformly mix with the acidifying agent or the acidifying agent-containing solution, and then mix with the remaining auxiliary materials for extrusion granulation or stirring granulation. The excipients in the 1/3 or less of the excipients are preferably water-soluble excipients. The 1/3 or less of the above may be usually 1/4 to 1/10 or less. The acidifier-containing solution refers to a solution obtained by dissolving an acidifying agent with a small amount of solvent according to a routine operation in the art to facilitate the mixing step; the solvent may be water, an organic solvent or water and an organic solvent. Mixture. The organic solvent is the same as described above.
湿法制粒完成后, 可直接得到固体颗粒制剂, 也可作为制剂中间体, 经 进一步的常规步骤, 制得片剂或胶囊剂等其他形式的固体制剂。  After the wet granulation is completed, the solid granule preparation can be directly obtained, or can be used as a preparation intermediate, and further solid preparations such as tablets or capsules can be obtained through further conventional steps.
进一步的, 本发明还涉及由上述方法制得的固体制剂。  Further, the present invention also relates to a solid preparation prepared by the above method.
本发明中, 上述各优选条件, 可在符合本领域常识的基础上任意组合, 即可得本发明各较佳实例。  In the present invention, each of the above preferred conditions can be arbitrarily combined on the basis of common knowledge in the art, and preferred embodiments of the present invention can be obtained.
本发明中, 所用试剂和原料可通过市售可得。  In the present invention, the reagents and starting materials used are commercially available.
本发明的积极进步效果在于:本发明的制备方法避免了机械粉碎处理所 带来的污染严重、 损耗大和安全隐患严重的缺陷, 在制粒过程中即达到减小 水不溶性和 /或水难溶性酸性药物活性成分粒径的效果。 该方法操作简便易 行, 安全系数高, 易应用于工业化生产。 本发明的固体制剂中药物活性成分 粒径小, 具有优异的溶出特性, 生物利用度高, 个体差异小, 且还具有较佳 的稳定性和含量均匀度。 具体实施方式 The positive progress of the invention is that the preparation method of the invention avoids the defects of serious pollution, large loss and serious safety hazard caused by mechanical pulverization treatment, and achieves reduction of water insolubility and/or poor water solubility during granulation. The effect of the particle size of the acidic pharmaceutical active ingredient. The method is easy to operate, has a high safety factor, and is easy to be applied to industrial production. The solid active preparation of the present invention has a small particle size, excellent dissolution characteristics, high bioavailability, small individual difference, and also good stability and content uniformity. detailed description
下面用实施例来进一步说明本发明, 但本发明并不受其限制。  The invention is further illustrated by the following examples, but the invention is not limited thereto.
下列实施例中未注明具体条件的实验方法, 通常按照常规条件, 或按照 制造厂商所建议的条件。 剂型规格以药物活性成分含量计, 如 2mg/片, 是 指每片中含药物活性成分 2mg。  The experimental methods in the following examples which do not specify the specific conditions are usually in accordance with conventional conditions or in accordance with the conditions recommended by the manufacturer. The dosage form specification is based on the content of the active ingredient of the drug, such as 2 mg/tablet, which means that each tablet contains 2 mg of the active ingredient of the drug.
用量单位为克, 百分比为质量百分比。  The unit of use is gram and the percentage is the mass percentage.
药物活性成分和溶剂的质量百分比为占湿法制粒干物料的质量百分比。 其中, 溶剂的用量包括酸化剂和碱化剂的水溶液中的水。  The mass percentage of the pharmaceutically active ingredient and the solvent is the mass percentage of the wet granulated dry material. Wherein the amount of the solvent includes water in an aqueous solution of an acidifying agent and an alkalizing agent.
包衣材料为胃溶包衣材料预混料-欧巴代。 对比实施例 1与实施例 1吲达帕胺颗粒配方及制备方法 (吲达帕胺分子量: 365.83)  The coating material is a premix of the gastric coating material - Opadry. Comparative Example 1 and Example 1 Indapamide particle formulation and preparation method (Indapamide molecular weight: 365.83)
Figure imgf000010_0001
实施例 2~3 吲达帕胺颗粒配方及制备方法
Figure imgf000011_0001
Figure imgf000010_0001
Example 2~3 Indapamide granule formula and preparation method
Figure imgf000011_0001
实施例 4吲达帕胺颗粒配方及制备方法
Figure imgf000011_0002
实施例 5吲达帕胺片 (2.5mg/片)配方及制备方法
Figure imgf000012_0001
Example 4 Indapamide granule formula and preparation method
Figure imgf000011_0002
Example 5 Indapamide Tablets (2.5 mg/tablet) Formulation and Preparation Method
Figure imgf000012_0001
对比实施例 2和实施例 6 吲达帕胺片 (2.5mg/片)配方及制备方法
Figure imgf000012_0002
将吲达帕胺过 80目筛, 与乳 将吲达帕胺、 聚维酮 K30、 乙醇、 糖、微晶纤维素混合均匀,加含聚 10%氢氧化钠水溶液配制成含药碱性 维酮 K30的乙醇水溶液进行搅拌 液,边搅拌边加入 10%盐酸水溶液,再 制成软材,挤压制粒,湿粒经干燥 加入到乳糖和微晶纤维素混合粉中混 制备
Comparative Example 2 and Example 6 Indapamide Tablets (2.5 mg/tablet) Formulation and Preparation Method
Figure imgf000012_0002
The indapamide is passed through an 80 mesh sieve, and the indapamide, povidone K30, ethanol, sugar, and microcrystalline cellulose are uniformly mixed with the milk, and the polybasic aqueous solution containing 10% sodium hydroxide is added to prepare a drug-containing alkaline dimension. The ketone K30 aqueous solution of ethanol is stirred, added with 10% hydrochloric acid aqueous solution while stirring, and then made into a soft material, extruded and granulated, and the wet granule is dried and added to the mixed powder of lactose and microcrystalline cellulose to prepare a mixture.
后整粒,加入硬脂酸镁、滑石粉后 合制成软材, 挤压制粒,湿粒经干燥后 工艺  After the whole granules, magnesium stearate and talc powder are added to form a soft material, which is extruded and granulated, and the wet granules are dried.
压片。在水中边搅拌边加入欧巴代 整粒, 加入硬脂酸镁、 滑石粉后压片。 粉末, 加完后继续搅拌 45分钟, 在水中边搅拌边加入欧巴代粉末,加完 配成 19^%浓度的包衣液,对片芯 后继续搅拌 45分钟, 配成 19wt%浓度 进行薄膜包衣。 的包衣液, 对片芯进行薄膜包衣。  Tableting. The mixture was added to the Opadry in the water while stirring, and magnesium stearate and talc powder were added and then compressed. Powder, continue to stir for 45 minutes after the addition, add Opadry powder in water while stirring, add the coating solution of 19% concentration, continue to stir for 45 minutes after the core, and prepare the film with 19wt% concentration. Coating. The coating liquid is film coated on the core.
实施例 7吲达帕胺片 (2.5mg/片)配方及制备方法 Example 7 Indapamide Tablets (2.5 mg/tablet) Formulation and Preparation Method
Figure imgf000013_0001
实施例 8吲达帕胺片 (2.5mg/片)配方及制备方法
Figure imgf000013_0001
Example 8 Indapamide Tablets (2.5 mg/tablet) Formulation and Preparation Method
Figure imgf000014_0001
Figure imgf000014_0001
实施例 10吲达帕胺胶囊(2.5mg/粒)配方及制备方法 取实施例 6压片前的颗粒过 30目筛, 混合均匀后装胶囊。 对比实施例 3格列吡嗪颗粒配方及制备方法 (格列吡嗪分子量 445.54)
Figure imgf000015_0001
Example 10 Indapamide Capsule (2.5 mg/granule) Formulation and Preparation Method The particles before the tableting of Example 6 were passed through a 30 mesh sieve, uniformly mixed, and then filled. Comparative Example 3 Glipizide granule formulation and preparation method (glipizide molecular weight 445.54)
Figure imgf000015_0001
实施例 11~12 格列吡嗪颗粒配方及制备方法Example 11~12 glipizide granule formula and preparation method thereof
Figure imgf000015_0002
对比实施 1 4和实施例 13 格列吡嗪片 (2.5mg/片)配方及制备方法
Figure imgf000015_0002
Comparative Example 14 and Example 13 Glipizide Tablets (2.5 mg/tablet) Formulation and Preparation Method
对比实施例 4 实施例 13 药物 格列吡嗪 2.5 (2.3%, 微粉处理) 格列吡嗪 2.5 (2.2%, 无预处理) 乳糖 100、 聚维酮 K30 2、 硬脂酸 乳糖 100、 聚维酮 Κ30 2、 硬脂酸镁 0.5、 辅料  Comparative Example 4 Example 13 Drug glipizide 2.5 (2.3%, micronized treatment) Glipizide 2.5 (2.2%, no pretreatment) Lactose 100, povidone K30 2, lactose lactose 100, polydimensional Ketone Κ30 2, magnesium stearate 0.5, accessories
镁 0.5、 滑石粉 1、 羧甲淀粉钠 5 滑石粉 1、 羧甲淀粉钠 5 溶剂 水 8.5 (7.7%) 水 3.75 (6.8%)  Magnesium 0.5, talc 1, sodium carboxymethyl starch 5 talc 1, sodium carboxymethyl starch 5 Solvent water 8.5 (7.7%) water 3.75 (6.8%)
10%氢氧化钠水溶液 2.25 碱化剂 \  10% sodium hydroxide solution 2.25 alkalizing agent
(与格列吡嗪的摩尔比值: 1.00) 酸化剂 \ 10%盐酸水溶液 2.05 (式 1值: 1.00) 将格列吡嗪、聚维酮 Κ30和 10%氢氧 将格列吡嗪过 80目筛, 与乳  (Molecular ratio with glipizide: 1.00) Acidifier \ 10% aqueous hydrochloric acid 2.05 (Formula 1 value: 1.00) Glipizide, Povidone 30 and 10% Hydrogen Oxygen Glipizide over 80 mesh Sieve, with milk
化钠水溶液配制成含药碱性液,加入 25% 糖混合均匀, 加含聚维酮 Κ30的  The sodium sulphate solution is formulated into a medicated alkaline solution, and 25% of the sugar is added and uniformly mixed, and the povidone Κ30 is added.
量的乳糖搅拌均匀,边搅拌边加入 10%盐 制备 水溶液进行搅拌制成软材, 挤压  The amount of lactose is stirred evenly, and 10% salt is added with stirring to prepare an aqueous solution for stirring to form a soft material.
酸水溶液,再加入到 75%量的乳糖中搅拌 工艺 制粒, 湿粒经干燥后整粒, 加入  The aqueous acid solution is added to the 75% amount of lactose and stirred to process the granules. The wet granules are dried and then granulated.
制成软材, 挤压制粒, 湿粒经干燥后整 硬脂酸镁、 滑石粉和羧甲淀粉钠  Made of soft material, extruded granulated, wet granules dried, magnesium stearate, talc and sodium carboxymethyl starch
粒。, 加入硬脂酸镁、 滑石粉和羧甲淀粉 后压片。  grain. Add magnesium stearate, talc and carboxymethyl starch and compress.
钠后压片。  Tablet after sodium.
实施例 14格列吡嗪片 (2.5mg/片)配方及制备方法 Example 14 Glipizide Tablets (2.5 mg/tablet) Formulation and Preparation Method
Figure imgf000016_0001
实施例 15格列吡嗪片 (5mg/片)配方及制备方法
Figure imgf000016_0001
Example 15 glipizide tablets (5 mg / tablet) formula and preparation method
Figure imgf000017_0001
Figure imgf000017_0001
实施例 16格列吡嗪胶囊(2.5mg/粒)配方及制备方法 取实施例 14压片前的颗粒过 30目筛, 混合均匀后装胶 实施例 17 叶酸颗粒配方及制备方法 (叶酸分子量 441.4)
Figure imgf000017_0002
对比实施例 5和实施例 18 叶酸颗粒配方及制备方法 (叶酸分子量 441.4)
Figure imgf000018_0001
Example 16 glipizide capsule (2.5 mg / granule) formula and preparation method The granules before the tableting of Example 14 were passed through a 30 mesh sieve, and the mixture was uniformly mixed and then filled. Example 17 Folic acid granule formula and preparation method (folic acid molecular weight 441.4) )
Figure imgf000017_0002
Comparative Example 5 and Example 18 Folic acid granule formulation and preparation method (folic acid molecular weight 441.4)
Figure imgf000018_0001
实施例 19叶酸颗粒配方及制备方法Example 19 Folic acid granule formula and preparation method
Figure imgf000018_0002
对比实施例 6叶酸片 (5mg/片)配方及制备方法
Figure imgf000018_0002
Comparative Example 6 Folic Acid Tablets (5 mg/tablet) Formulation and Preparation Method
Figure imgf000019_0001
实施例 21叶酸片 (5mg/片)配方及制备方法
Figure imgf000019_0001
Example 21 Folic acid tablet (5 mg / tablet) formula and preparation method
Figure imgf000020_0001
实施例 23叶酸胶囊(5mg/粒)配方及制备方法
Figure imgf000020_0001
Example 23 Folic acid capsule (5 mg / granule) formula and preparation method
取实施例 21压片前的颗粒过 30目筛, 混合均匀后装胶囊。 实施例 24叶酸片 (5mg/片)配方及制备方法 The granules before the tableting of Example 21 were passed through a 30-mesh sieve, uniformly mixed, and then filled. Example 24 Folic acid tablet (5 mg / tablet) formula and preparation method
Figure imgf000021_0001
实施例 26 甲氨蝶呤颗粒配方及制备方法
Figure imgf000021_0001
Example 26 Methotrexate particle formula and preparation method
实施例 28 甲氨蝶呤片 (2.5mg/片)配方及制备方法 Example 28 Methotrexate tablets (2.5 mg / tablet) formula and preparation method
Figure imgf000023_0001
实施例 30 吲达帕胺片 (2.5mg/片)配方及制备方法
Figure imgf000023_0001
Example 30 Indapamide Tablets (2.5 mg/tablet) Formulation and Preparation Method
Figure imgf000024_0001
实施例 32格列吡嗪片 (5mg/片)配方及制备方法
Figure imgf000024_0001
Example 32 Glipizide Tablets (5 mg/tablet) Formulation and Preparation Method
Figure imgf000025_0001
实施例 34 叶酸片 (5mg/片)配方及制备方法
Figure imgf000025_0001
Example 34 Folic acid tablet (5 mg / tablet) formula and preparation method
Figure imgf000026_0001
实施例 36 甲氨蝶吟片配方及制备方法
Figure imgf000027_0001
Figure imgf000026_0001
Example 36 Methotrexate tablet formulation and preparation method
Figure imgf000027_0001
实施例 37苄氟噻嗪片 (2.5mg/片)配方及制备方法
Figure imgf000027_0002
实施例 38苄氟噻嗪颗粒配方及制备方法
Figure imgf000028_0001
Example 37 Benzyl fluorothiazide tablets (2.5 mg / tablet) formulation and preparation method
Figure imgf000027_0002
Example 38 Benzyl fluorothiazide particle formulation and preparation method
Figure imgf000028_0001
实施例 39苄氟噻嗪片 (5mg/片)配方及制备方法
Figure imgf000028_0002
实施例 40吲达帕胺片 (2.5mg/片)配方及制备方法
Example 39 Benzyl fluorothiazide tablets (5 mg / tablet) formulation and preparation method
Figure imgf000028_0002
Example 40 Indapamide Tablets (2.5 mg/tablet) Formulation and Preparation Method
Figure imgf000029_0001
效果实施例 1 粒径比较试验
Figure imgf000029_0001
Effect Example 1 Particle size comparison test
测试仪器: BT-9300S激光粒度分布仪; BT-800自动循环进样系统。 测试条件: 循环进样系统中的介质为水, 体积为 570ml左右, 离心泵转 速为 1600rpm。  Test equipment: BT-9300S laser particle size distribution instrument; BT-800 automatic cycle injection system. Test conditions: The medium in the circulating injection system is water, the volume is about 570ml, and the centrifugal pump has a rotation speed of 1600rpm.
测试方法: 取颗粒约 2g, 加入循环进样系统, 使系统吸光度达到 15% 左右, 开启超声分散 3分钟, 连续 6次采样测试, 得到粒径平均值。 D10、 D50和 D90分别是累计粒度分布百分数达到 10%、 50%和 90%时所对应的粒 径。 1 ) 吲达帕胺粒径对比: Test method: Take about 2g of particles, add to the circulating injection system, make the absorbance of the system reach about 15%, turn on the ultrasonic dispersion for 3 minutes, and test the sample for 6 consecutive times to obtain the average particle size. D10, D50 and D90 are the corresponding particle sizes when the cumulative particle size distribution percentage reaches 10%, 50% and 90%, respectively. 1) Indapamide particle size comparison:
Figure imgf000030_0001
Figure imgf000030_0001
由上述数据可见,采用本发明的方法制得的吲达帕胺颗粒中吲达帕胺体 积平均粒径减小至原料药粒径的 8.5~21.8%, 达到 4.78~12.25微米。  From the above data, it can be seen that the intrinsic average particle size of indapamide in the indapamide particles obtained by the method of the present invention is reduced to 8.5 to 21.8% of the particle diameter of the drug substance, reaching 4.78 to 12.25 μm.
2 ) 格列吡嗪粒径对比: 2) Glipizide particle size comparison:
Figure imgf000030_0002
Figure imgf000030_0002
由上述数据可见,采用本发明的方法制得的格列吡嗪颗粒中的格列吡嗪 体积平均粒径减小至经微粉处理的原料药粒径的 8.8~8.5%, 达到 0.62~0.60 微米。 3 ) 叶酸粒径对比: It can be seen from the above data that the volume average particle diameter of glipizide in the glipizide particles prepared by the method of the invention is reduced to 8.8 to 8.5% of the particle size of the raw material treated by the micropowder, and reaches 0.62 to 0.60 micron. . 3) Folic acid particle size comparison:
Figure imgf000031_0001
Figure imgf000031_0001
由上述数据可见,采用本发明的方法制得的叶酸颗粒中的叶酸体积平均 粒径减小至经微粉处理的原料药粒径的 15.9~34.6%, 达到 0.89~1.94微米。  From the above data, it can be seen that the average volume fraction of folic acid in the folic acid granules obtained by the method of the present invention is reduced to 15.9 to 34.6% of the particle size of the raw material treated with the fine powder, and is 0.89 to 1.94 μm.
4 ) 甲氨蝶呤粒径: 4) Methotrexate particle size:
Figure imgf000031_0002
Figure imgf000031_0002
由上述数据可见,采用本发明的方法制得的甲氨蝶呤颗粒中的甲氨蝶呤 体积平均粒径减小至原料药粒径的 5.2~10.9%, 达到 4.43~9.37微米。  From the above data, it can be seen that the volume average particle diameter of methotrexate in the methotrexate particles obtained by the method of the present invention is reduced to 5.2 to 10.9% of the particle diameter of the drug substance, which is 4.43 to 9.37 μm.
4) 苄氟噻嗪粒径: 4) Benzyl fluorothiazide particle size:
Figure imgf000031_0003
Figure imgf000031_0003
由上述数据可见,采用本发明的方法制得的苄氟噻嗪颗粒中的苄氟噻 体积平均粒径减小至原料药粒径的 8.9%, 达到 6.43微米。 效果实施例 2 溶出度比较试验 From the above data, it is seen that the volume average particle diameter of benzyl fluorothiazide in the benzfluorothiazine particles obtained by the method of the present invention is reduced to 8.9% of the particle diameter of the drug substance to 6.43 μm. Effect Example 2 Dissolution comparison test
1 ) 吲达帕胺片溶出度试验  1) Indapamide tablets dissolution test
溶出度测定方法: 取样品, 照溶出度测定法(中国药典 2010年版二部 附录 X C第二法), 溶出液 900 ml , 取 0.2mol/l磷酸二氢钾溶液 250ml, 加 0.2mol/氢氧化钠溶液 118m加水稀释至 1000ml, 调节 pH至 6.8, 转速为每 分钟 100转, 依法操作, 并配制对照溶液。 照分光光度法 (中国药典 2010 年版二部附录 IV A) ,在 240nm的波长处测定吸收度, 计算出每片的溶出量。  Dissolution method: Take the sample, according to the dissolution method (Chinese Pharmacopoeia 2010 edition two appendix XC second method), the dissolution solution 900 ml, take 0.2mol / l potassium dihydrogen phosphate solution 250ml, add 0.2mol / KOH The sodium solution was diluted with water to 1000 ml of 118 m, the pH was adjusted to 6.8, the rotation speed was 100 rpm, and the control solution was prepared according to the law. According to the spectrophotometry (Chinese Pharmacopoeia 2010 edition two appendix IV A), the absorbance was measured at a wavelength of 240 nm, and the amount of dissolution per tablet was calculated.
Figure imgf000032_0001
Figure imgf000032_0001
2 ) 格列吡嗪片溶出度试验 2) Glipizide tablet dissolution test
溶出度测定方法 (1 ) : 取样品, 照溶出度测定法 (中国药典 2010年版 二部附录 X C第二法), 溶出液为磷酸盐缓冲液 (pH7.4) 500ml , 转速为 每分钟 100转, 依法操作, 并配制对照溶液。 照分光光度法(中国药典 2010 年版二部附录 IV A) ,在 222nm的波长处测定吸收度, 计算出每片的溶出量。  Dissolution method (1): Take the sample, according to the dissolution method (Chinese Pharmacopoeia 2010 edition two appendix XC second method), the eluate is phosphate buffer (pH 7.4) 500ml, the rotation speed is 100 rpm , operate according to law, and prepare a control solution. According to the spectrophotometry (Chinese Pharmacopoeia 2010 edition two appendix IV A), the absorbance was measured at a wavelength of 222 nm, and the amount of dissolution per tablet was calculated.
Figure imgf000032_0002
溶出度测定方法 (2 ): 取样品, 照溶出度测定法 (中国药典 2010年版 二部附录 X C第二法), 溶出液为水 500ml , 转速为每分钟 100转, 依法操 作, 并配制对照溶液。 照分光光度法 (中国药典 2010年版二部附录 IV A), 在 222nm的波长处测定吸收度, 计算出每片的溶出量。
Figure imgf000032_0002
Dissolution method (2): Take the sample, according to the dissolution method (Chinese Pharmacopoeia 2010 edition two appendix XC second method), the eluate is water 500ml, the rotation speed is 100 rpm, operate according to the law, and prepare the control solution . According to the spectrophotometry (Chinese Pharmacopoeia 2010 edition two appendix IV A), the absorbance was measured at a wavelength of 222 nm, and the amount of dissolution per tablet was calculated.
Figure imgf000033_0001
Figure imgf000033_0001
3 ) 叶酸片溶出度试验 3) Folic acid tablet dissolution test
溶出度测定方法 (1 ): 取样品, 照溶出度测定法 (中国药典 2010年版 二部附录 X C第二法), 溶出液为磷酸盐缓冲液(pH6.8)缓冲液 900ml, 转 速为每分钟 100转, 依法操作, 并配制对照溶液。 照分光光度法(中国药典 2010年版二部附录 IV A), 在 281nm的波长处测定吸收度, 计算出每片的溶  Dissolution method (1): Take the sample, according to the dissolution method (Chinese Pharmacopoeia 2010 edition two appendix XC second method), the eluate is phosphate buffer (pH 6.8) buffer 900ml, the rotation speed is every minute 100 rpm, operate according to law, and prepare a control solution. According to the spectrophotometry (Chinese Pharmacopoeia 2010 edition two appendix IV A), the absorbance is measured at a wavelength of 281 nm, and the dissolution of each tablet is calculated.
Figure imgf000033_0002
Figure imgf000033_0002
溶出度测定方法 (2 ): 取样品, 照溶出度测定法 (中国药典 2010年版 二部附录 X C第二法), 溶出液为水 900ml, 转速为每分钟 100转, 依法操 作, 并配制对照溶液。 照分光光度法 (中国药典 2010年版二部附录 IV A), 在 281nm的波长处测定吸收度, 计算出每片的溶出量。 溶出度 (%) Dissolution method (2): Take the sample, according to the dissolution method (Chinese Pharmacopoeia 2010 edition two appendix XC second method), the eluate is 900ml of water, the rotation speed is 100 rpm, operate according to the law, and prepare the control solution . According to the spectrophotometry (Chinese Pharmacopoeia 2010 edition two appendix IV A), the absorbance was measured at a wavelength of 281 nm, and the amount of dissolution per tablet was calculated. Dissolution (%)
实施例  Example
5min 15min 30min 45min 对比 6 32.18 42.70 46.26 49.51  5min 15min 30min 45min comparison 6 32.18 42.70 46.26 49.51
20 42.85 55.69 61.88 63.7420 42.85 55.69 61.88 63.74
21 57.40 62.81 65.29 66.3721 57.40 62.81 65.29 66.37
22 60.30 66.41 69.76 71.04 22 60.30 66.41 69.76 71.04
35 59.78 65.34 68.33 69.49 35 59.78 65.34 68.33 69.49
效果实施例 3 稳定性比较试验 Effect Example 3 Stability Comparison Test
1 ) 吲达帕胺  1) indapamide
将试验样品分别置高密度聚乙烯塑料瓶中, 密封, 放入加速考察箱中, 于温度 40°C±2°C,相对湿度 75%±5%条件进行 3个月的加速试验后,进行相 关项目的稳定性测定。  The test samples were placed in high-density polyethylene plastic bottles, sealed, placed in an accelerated inspection box, and subjected to an accelerated test for 3 months at a temperature of 40 ° C ± 2 ° C and a relative humidity of 75% ± 5%. Stability determination of related items.
有关物质的测定方法: 避光操作。 取本品细粉适量, 加流动相适量, 置 热水浴中振摇 5分钟, 使吲达帕胺溶解, 用流动相稀释制成每 lml中约含吲 达帕胺 0.5mg的溶液, 滤过, 取续滤液作为供试品。 照高效液相色谱法(中 国药典 2010年版二部附录 V D), 用十八垸基硅垸键合硅胶为填充剂, 分别 测定。 照面积归一法进行计算。  Method for determining the substance: Protect from light. Take the appropriate amount of fine powder, add appropriate amount of mobile phase, shake in a hot water bath for 5 minutes, dissolve indapamide, dilute with mobile phase to make a solution containing about 0.5 mg of indapamide per 1 ml, filter After that, the filtrate was taken as the test sample. According to high performance liquid chromatography (Chinese Pharmacopoeia 2010 edition two appendix V D), octadecyl silicon germanium bonded silica was used as a filler and determined separately. Calculated according to the area normalization method.
溶出度试验方法同效果实施例 2。  The dissolution test method was the same as in the effect example 2.
Figure imgf000034_0001
效果实施例 4 含量均勾度比较实验
Figure imgf000034_0001
Effect Example 4 Comparison of the content of the hooks
1 ) 吲达帕胺片  1) Indapamide tablets
含量均匀度的测定方法: 取本品 1 片, 置乳钵中, 加乙醇适量, 研磨, 并用乙醇分次转移至 100ml 量瓶中, 振摇, 使吲达帕胺溶解, 加乙醇稀释 至刻度, 摇匀, 滤过, 精密量取续滤液 10ml, 置 50ml量瓶中, 加乙醇稀释 至刻度, 摇匀, 取此溶液与含量测定项下的对照品溶液, 照紫外-可见分光 光度法 (中国药典 2010年版二部附录 IV A) , 在 242nm 的波长处测定吸收 度, 计算。  Determination of content uniformity: Take 1 tablet of this product, place it in the milk, add appropriate amount of ethanol, grind, and transfer it to 100ml volumetric flask with ethanol, shake it, dissolve indapamide, dilute with ethanol to scale Shake well, filter, and accurately measure 10ml of the filtrate. Place in a 50ml volumetric flask, dilute to the mark with ethanol, shake well, take the reference solution under the solution and the content determination, and observe the UV-visible spectrophotometry. Chinese Pharmacopoeia 2010 edition two appendix IV A), the absorbance is measured at a wavelength of 242 nm, calculated.
Figure imgf000035_0001
Figure imgf000035_0001
2 ) 格列吡嗪片 2) Glipizide tablets
含量均匀度的测定方法: 取本品 1 片, 研细, 加磷酸盐缓冲液 (PH7.4) 适量研磨, 并用磷酸盐缓冲液 (pH7.4 ) 分次转移至 200ml量瓶中, 摇匀,滤 过,取续滤液作为供试品溶液; 另取格列吡嗪对照品适量, 同法制成每 1ml 中约含 25 的溶液, 作为对照品溶液。取上述两种溶液, 在 275nm的波长 处分别测定吸光度, 计算。  Determination of content uniformity: Take 1 piece of this product, grind it, add phosphate buffer (pH 7.4), grind it in an appropriate amount, and transfer it to a 200ml volumetric flask with phosphate buffer (pH 7.4). Shake well. , filtered, take the filtrate as the test solution; take the appropriate amount of glipizide reference substance, the same method to make a solution containing about 25 per 1ml, as a reference solution. The above two solutions were taken, and the absorbance was measured at a wavelength of 275 nm, and calculated.
Figure imgf000035_0002
3) 叶酸片
Figure imgf000035_0002
3) Folic acid tablets
含量均匀度的测定方法: 取本品 1片, 置 25ml量瓶中, 加 0.5%氨溶液 约 15ml, 置热水浴中加热 20分钟, 时时振摇使叶酸溶解, 放冷, 用水稀释 至刻度, 摇匀, 滤过, 取续滤液作为供试品溶液, 照高效液相色谱法 (中国 药典 2010年版二部附录 V D), 用十八垸基硅垸键合硅胶为填充剂, 记录色 谱图; 另取叶酸对照品, 同法测定,按外标法以峰面积计算含量,应符合(中 国药典 2010年版二部附录 X E)。
Figure imgf000036_0001
Determination of content uniformity: Take 1 piece of this product, place it in a 25ml volumetric flask, add about 15ml of 0.5% ammonia solution, heat in a hot water bath for 20 minutes, shake it to dissolve the folic acid, let cool, dilute with water to the scale Shake, filter, and take the filtrate as the test solution, according to high performance liquid chromatography (Chinese Pharmacopoeia 2010 edition two appendix VD), using 18 垸 垸 silicon germanium bonded silica as a filler, record the chromatogram Another folic acid reference substance, determined by the same method, according to the external standard method to calculate the content of the peak area, should be consistent with (Chinese Pharmacopoeia 2010 edition two appendix XE).
Figure imgf000036_0001
4) 苄氟噻嗪片  4) Benzyl fluorothiazide tablets
含量均匀度测定方法: 取本品 1片, 置乳钵中, 研细, 加 0.4%氢氧化 钠溶液适量, 研磨, 并用 0.4%氢氧化钠溶液分次转移至 25ml量瓶中, 充分 振摇使苄氟噻嗪溶解, 加 0.4%氢氧化钠溶液稀释至刻度, 摇匀, 滤过, 精 密量取续滤液 2ml, 置 25ml量瓶中, 加水稀释至刻度, 摇匀, 照分光光度 法 (中国药典 2010年版二部附录 IV A), 在 274nm 的波长处测定吸光度; 另精密称取苄氟噻嗪对照品, 加 0.01mol/L氢氧化钠液溶解并定量稀释制成 每 lml 中约含 15 g 的溶液, 同法测定吸光度, 计算。  Determination of content uniformity: Take 1 tablet of this product, place it in a mortar, grind it, add 0.4% sodium hydroxide solution, grind it, and transfer it to a 25ml volumetric flask with 0.4% sodium hydroxide solution, shake it thoroughly. Dissolve the benzyl fluorothiazide, dilute to the mark with 0.4% sodium hydroxide solution, shake well, filter, accurately measure the 2ml of the filtrate, place in a 25ml volumetric flask, dilute with water to the mark, shake well, according to spectrophotometry ( Chinese Pharmacopoeia 2010 edition two appendix IV A), absorbance at 274nm wavelength; another precision weighed benzyl fluorothiazide reference substance, add 0.01mol / L sodium hydroxide solution dissolved and quantitatively diluted to make each lml 15 g of solution, the same method of measuring absorbance, calculated.
Figure imgf000036_0002
Figure imgf000036_0002

Claims

权利要求 Rights request
1、 一种药物固体制剂的制备方法, 其特征在于其包括如下步骤: 将水 不溶性和 /或水难溶性酸性药物活性成分溶于含碱化剂的碱性溶液中,制得含 药碱性液; 之后, 将辅料和所述的含药碱性液均匀混合, 进行湿法制粒。 A method for preparing a pharmaceutical solid preparation, which comprises the steps of: dissolving a water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient in an alkaline solution containing an alkalizing agent to obtain a drug-containing alkaline After the solution, the excipient and the medicated alkaline solution are uniformly mixed and subjected to wet granulation.
2、 如权利要求 1所述的方法, 其特征在于: 所述的水不溶性和 /或水难 溶性酸性药物活性成分为在固体制剂中含量 20%以下, 较佳的为 10%以下, 更佳的为 5%以下的水不溶性或水难溶性酸性药物活性成分; 百分比为质量 百分比。  2. The method according to claim 1, wherein: the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient is 20% or less, preferably 10% or less, more preferably in the solid preparation. The water-insoluble or poorly water-soluble acidic pharmaceutical active ingredient is 5% or less; the percentage is the mass percentage.
3、 如权利要求 1所述的方法, 其特征在于: 所述的水不溶性和 /或水难 溶性碱性药物活性成分为格列吡嗪、 叶酸、 布美他尼、 双氯非那胺、 异卡波 肼、 苄氟噻嗪、 对氟噻嗪、 甲氨蝶呤、 维生素 H、 己垸雌酚、 吲达帕胺、 呋 塞米、 硫鸟剽呤、 别嘌醇、 格列喹酮、 辛伐他汀、 来氟米特、 氢氯噻嗪或苯 巴比妥。  3. The method according to claim 1, wherein: the water-insoluble and/or poorly water-soluble basic pharmaceutically active ingredient is glipizide, folic acid, bumetanide, diclofenac, Isocyanol, benzfluorothiazide, p-fluorothiazide, methotrexate, vitamin H, hexaerythritol, indapamide, furosemide, thioguanine, allopurinol, gliclazone , simvastatin, leflunomide, hydrochlorothiazide or phenobarbital.
4、 如权利要求 1~3任一项所述的方法, 其特征在于: 所述的碱化剂为 无机碱和 /或有机碱, 或者强碱和 /或弱碱, 较佳的选自氢氧化钠、 氢氧化钾、 碳酸钠、 碳酸钾、 乙醇钠、 甲葡胺、 二乙醇胺和三乙醇胺中的一种或多种。  The method according to any one of claims 1 to 3, wherein the alkalizing agent is an inorganic base and/or an organic base, or a strong base and/or a weak base, preferably selected from hydrogen. One or more of sodium oxide, potassium hydroxide, sodium carbonate, potassium carbonate, sodium ethoxide, meglumine, diethanolamine, and triethanolamine.
5、 如权利要求 1所述的方法, 其特征在于:  5. The method of claim 1 wherein:
所述的水不溶性和 /或水难溶性酸性药物活性成分为吲达帕胺时,所述的 碱化剂为氢氧化钠、 氢氧化钾或乙醇钠;  When the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient is indapamide, the alkalizing agent is sodium hydroxide, potassium hydroxide or sodium ethoxide;
所述的水不溶性和 /或水难溶性酸性药物活性成分为格列吡嗪时,所述的 碱化剂为氢氧化钠或氢氧化钾;  When the water-insoluble and/or water-insoluble acidic pharmaceutical active ingredient is glipizide, the alkalizing agent is sodium hydroxide or potassium hydroxide;
所述的水不溶性和 /或水难溶性酸性药物活性成分为叶酸时,所述的碱化 剂为氢氧化钠、 氢氧化钾、 乙醇钠、 碳酸钠或碳酸钾;  When the water-insoluble and/or water-insoluble acidic pharmaceutical active ingredient is folic acid, the alkalizing agent is sodium hydroxide, potassium hydroxide, sodium ethoxide, sodium carbonate or potassium carbonate;
所述的水不溶性和 /或水难溶性酸性药物活性成分为甲氨蝶呤时,所述的 碱化剂为氢氧化钠、 氢氧化钾、 碳酸钠或碳酸钾; 所述的水不溶性和 /或水难溶性酸性药物活性成分为苄氟噻嗪时,所述的 碱化剂为氢氧化钠或氢氧化钾。 When the water-insoluble and/or water-insoluble acidic pharmaceutical active ingredient is methotrexate, the alkalizing agent is sodium hydroxide, potassium hydroxide, sodium carbonate or potassium carbonate; When the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient is benzfluorothiazide, the alkalizing agent is sodium hydroxide or potassium hydroxide.
6、 如权利要求 1、 4或 5所述的方法, 其特征在于: 所述的碱化剂的用 量为能使水不溶性和 /或水难溶性酸性药物活性成分完全溶解的最小量的 1~1.5倍, 更佳的为 1~1.05倍。  6. The method according to claim 1, 4 or 5, wherein: the alkalizing agent is used in an amount such that the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient is completely dissolved. 1.5 times, more preferably 1 to 1.05 times.
7、 如权利要求 1、 4或 5所述的方法, 其特征在于: 所述的碱化剂与水 不溶性和 /或水难溶性酸性药物活性成分的摩尔比值为 0.1~2.5, 更佳的为 0·9~1·5。  The method according to claim 1, 4 or 5, wherein the molar ratio of the alkalizing agent to the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient is from 0.1 to 2.5, more preferably 0·9~1·5.
8、 如权利要求 1所述的方法, 其特征在于:  8. The method of claim 1 wherein:
所述的水不溶性和 /或水难溶性酸性药物活性成分为吲达帕胺时,所述的 碱化剂为吲达帕胺摩尔量 0.7~1.1倍的氢氧化钠或乙醇钠;  When the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient is indapamide, the alkalizing agent is sodium hydroxide or sodium ethoxide in an amount of 0.7 to 1.1 times the molar amount of indapamide;
所述的水不溶性和 /或水难溶性酸性药物活性成分为格列吡嗪时,所述的 碱化剂为格列吡嗪摩尔量 0.95~1.1倍的氢氧化钠;  When the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient is glipizide, the alkalizing agent is sodium hydroxide having a molar amount of glipizide of 0.95 to 1.1 times;
所述的水不溶性和 /或水难溶性酸性药物活性成分为叶酸,所述的碱化剂 为叶酸摩尔量 1.8~2.1倍的氢氧化钠或其摩尔量 0.95~1.1倍的碳酸钠或碳酸 钾;  The water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient is folic acid, and the alkalizing agent is sodium hydroxide having a molar amount of folic acid of 1.8 to 2.1 times or a molar amount of 0.95 to 1.1 times of sodium carbonate or potassium carbonate. ;
所述的水不溶性和 /或水难溶性酸性药物活性成分为甲氨蝶呤,所述的碱 化剂为甲氨蝶呤摩尔量 1.4~1.6倍的氢氧化钠或摩尔量 0.85~1.1倍的碳酸钠; 所述的水不溶性和 /或水难溶性酸性药物活性成分为苄氟噻嗪,所述的碱 化剂为苄氟噻嗪摩尔量 0.9~1.6倍的氢氧化钠。  The water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient is methotrexate, and the alkalizing agent is a molar amount of methotrexate of 1.4 to 1.6 times sodium hydroxide or a molar amount of 0.85 to 1.1 times. Sodium carbonate; the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient is benzfluorothiazide, and the alkalizing agent is sodium hydroxide having a molar amount of benzyl fluorothiazide of 0.9 to 1.6 times.
9、 如权利要求 1所述的方法, 其特征在于: 所述的含碱化剂的碱性溶 液中的溶剂为水、 有机溶剂或者水和有机溶剂的混合液, 且碱化剂中离子可 在该溶剂中解离;  9. The method according to claim 1, wherein: the solvent in the alkaline agent-containing alkaline solution is water, an organic solvent or a mixture of water and an organic solvent, and the ions in the alkalizing agent are Dissociation in the solvent;
所述的有机溶剂为对水不溶性和 /或水难溶性酸性药物活性成分的溶解 性优于水的药剂领域可接受的溶剂, 较佳的为水溶性醇类或酮类溶剂, 更佳 的为乙醇、 丙酮、 丙二醇和丙三醇中的一种或多种。 The organic solvent is a solvent acceptable for the field of the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient which is superior to water, preferably a water-soluble alcohol or a ketone solvent, more preferably One or more of ethanol, acetone, propylene glycol, and glycerol.
10、 如权利要求 1或 9所述的方法, 其特征在于: 所述的碱性溶液中溶 剂的用量为湿法制粒干物料的质量百分比 5~100%, 较佳的为 10~50%。 The method according to claim 1 or 9, wherein the amount of the solvent in the alkaline solution is from 5 to 100% by mass, preferably from 10 to 50% by mass based on the dry granulated dry material.
11、 如权利要求 1 所述的方法, 其特征在于: 在所述的将水不溶性和 / 或水难溶性酸性药物活性成分溶于含碱化剂的碱性溶液中的同时和 /或之后, 还加入表面活性剂、 增溶剂和固体分散体的水溶性载体中的一种或多种, 然 后将所得含药碱性液进行后续步骤, 即与辅料均匀混合, 进行湿法制粒; 在将水不溶性和 /或水难溶性酸性药物活性成分溶于含碱化剂的碱性溶 液中的同时, 还加入固体分散体的水溶性载体时, 所述的固体分散体的水溶 性载体的量控制在能保证水不溶性和 /或水难溶性酸性药物活性成分完全溶 解于含碱化剂的碱性溶液中的量以下;  11. The method according to claim 1, wherein: while and/or after the water-insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient is dissolved in the alkaline solution containing the alkalizing agent, Further adding one or more of a surfactant, a solubilizing agent and a water-soluble carrier of the solid dispersion, and then subjecting the obtained medicated alkaline liquid to a subsequent step, that is, uniformly mixing with the auxiliary material, performing wet granulation; When the insoluble and/or poorly water-soluble acidic pharmaceutical active ingredient is dissolved in the alkaline solution containing the alkalizing agent, and the water-soluble carrier of the solid dispersion is also added, the amount of the water-soluble carrier of the solid dispersion is controlled at It can ensure that the water-insoluble and/or water-insoluble acidic pharmaceutical active ingredient is completely dissolved in the alkaline solution containing the alkalizing agent;
所述的表面活性剂、增溶剂和固体分散体的水溶性载体中的一种或多种 较佳的为聚维酮、 聚乙二醇 400-8000、 十二垸基硫酸钠、 泊洛沙姆、 聚氧乙 烯蓖麻油、 吐温 80、 硬脂酸聚烃氧 40酯、 乳糖、 甘露醇、 蔗糖、 羟丙基 -β- 环糊精、 β-环糊精和麦芽糖醇中的一种或多种;  One or more of the water-soluble carrier of the surfactant, solubilizer and solid dispersion are preferably povidone, polyethylene glycol 400-8000, sodium dodecyl sulfate, and poloxa a kind of polyoxyethylene castor oil, Tween 80, polyoxyl 40 stearate, lactose, mannitol, sucrose, hydroxypropyl-β-cyclodextrin, β-cyclodextrin and maltitol Or a variety;
所述的表面活性剂和 /或增溶剂的加入量较佳的为水不溶性和 /或水难溶 性酸性药物活性成分质量的 0.05~5倍, 更佳的为 0.05~2倍;  The surfactant and/or the solubilizing agent are preferably added in an amount of 0.05 to 5 times, more preferably 0.05 to 2 times, the mass of the water-insoluble and/or water-insoluble acidic pharmaceutical active ingredient;
所述的固体分散体的水溶性载体的加入量较佳的为水不溶性和 /或水难 溶性酸性药物活性成分质量的 0.5~20倍, 更佳的为 0.5~2倍。  The water-soluble carrier of the solid dispersion is preferably added in an amount of from 0.5 to 20 times, more preferably from 0.5 to 2 times, the mass of the water-insoluble and/or water-insoluble acidic pharmaceutical active ingredient.
12、 如权利要求 1所述的方法, 其特征在于: 在制备所述的含药碱性液 时, 按照下述操作进行溶液配制: 当以水为溶剂时, 升温至 40~80°C ; 当以 水和有机溶剂的混合溶液为溶剂时, 升温至 40~70°C ; 当以乙醇为溶剂时, 升温至 30~50°C。 12. The method according to claim 1, wherein: in preparing the medicated alkaline solution, the solution is prepared according to the following operation: when water is used as a solvent, the temperature is raised to 40 to 80 ° C ; When a mixed solution of water and an organic solvent is used as a solvent, the temperature is raised to 40 to 70 ° C ; when ethanol is used as a solvent, the temperature is raised to 30 to 50 ° C.
13、 如权利要求 1~12任一项所述的方法, 其特征在于: 在进行所述的 将辅料和所述的含药碱性液均匀混合, 进行湿法制粒的步骤时, 还加入酸化 剂, 使酸化剂与含药碱性液的混合液的碱性相对于含药碱性液的碱性降低。  The method according to any one of claims 1 to 12, wherein: in the step of uniformly mixing the auxiliary material and the medicated alkaline liquid to perform wet granulation, acidification is further added. The agent lowers the alkalinity of the mixture of the acidifying agent and the medicated alkaline solution with respect to the alkalinity of the medicated alkaline solution.
14、 如权利要求 13所述的方法, 其特征在于: 所述碱化剂为无机强碱、 有机强碱或无机中强碱, 所述的酸化剂为无机强酸; 14. The method according to claim 13, wherein: the alkalizing agent is an inorganic strong base, An organic strong base or an inorganic medium strong base, wherein the acidifying agent is an inorganic strong acid;
更佳的, 所述的碱化剂和酸化剂为下述组合: 氢氧化钠和盐酸、 氢氧化 钾和盐酸、 乙醇钠和盐酸、 碳酸钠和盐酸、 以及碳酸钾和盐酸。  More preferably, the alkalizing agent and acidifying agent are the combination of sodium hydroxide and hydrochloric acid, potassium hydroxide and hydrochloric acid, sodium ethoxide and hydrochloric acid, sodium carbonate and hydrochloric acid, and potassium carbonate and hydrochloric acid.
15、 如权利要求 13或 14所述的方法, 其特征在于: 所述的碱化剂与酸 化剂的用量满足下述关系: 式 1所得值为 0.01~1.5, 较佳的为 0.2~1.1, 更佳 的为 0.9-1.1;  The method according to claim 13 or 14, wherein the amount of the alkalizing agent and the acidifying agent satisfies the following relationship: The value obtained by the formula 1 is 0.01 to 1.5, preferably 0.2 to 1.1. More preferably 0.9-1.1;
(酸化剂摩尔数 xA ) I (碱化剂摩尔数 xB ) 式 1  (number of moles of acidifier xA) I (number of moles of alkalizing agent xB)
其中, A为酸化剂分子中的氢离子数, B为碱化剂分子阴离子总价态数。 Wherein A is the number of hydrogen ions in the acidifier molecule, and B is the total number of valence states of the alkalinizer molecular anion.
16、 如权利要求 13所述的方法, 其特征在于: 按下述方式中的任一种 进行具体操作:  16. The method of claim 13 wherein: the specific operation is performed in any of the following ways:
方式 (1 ) 将酸化剂或含酸化剂的溶液和辅料均匀混合, 再与含药碱性 液均匀混合, 进行挤压制粒或搅拌制粒;  Mode (1) uniformly mixing the acidifying agent or the acidifying agent-containing solution and the auxiliary material, and uniformly mixing with the medicated alkaline liquid, and performing extrusion granulation or stirring granulation;
方式 (2 ) 将含药碱性液与, 酸化剂或含酸化剂的溶液均匀的混合, 得 制粒液, 之后再将该制粒液与辅料进行挤压制粒、 搅拌制粒、 流化喷雾制粒 或离心喷雾制粒等;  Mode (2) uniformly mixing the medicated alkaline solution with an acidifying agent or a solution containing an acidifying agent to obtain a granulating liquid, and then pulverizing, agitating, granulating, and fluidizing the granulating liquid and the auxiliary material. Spray granulation or centrifugal spray granulation, etc.;
方式 (3 ) 将含药碱性液与辅料均匀的混合, 之后再与含酸化剂的溶液 均匀的混合, 进行挤压制粒或搅拌制粒;  Mode (3) uniformly mixing the medicated alkaline solution with the auxiliary material, and then uniformly mixing with the acidifying agent-containing solution, and performing extrusion granulation or stirring granulation;
方式 (4 )将含药碱性液与, 1/3以下的辅料, 以及酸化剂或含酸化剂的 溶液均匀的混合, 之后再与剩余辅料混合进行挤压制粒或搅拌制粒; 所述的 1/3以下的辅料中的辅料较佳的为水溶性辅料。  (4) uniformly mixing the medicated alkaline liquid with 1/3 or less of the auxiliary material, and the acidifying agent or the acidifying agent-containing solution, and then mixing with the remaining auxiliary materials for extrusion granulation or stirring granulation; The excipients in the excipients of 1/3 or less are preferably water-soluble excipients.
17、 如权利要求 1所述的方法, 其特征在于: 将如权利要求 1所述的方 法制得的固体颗粒, 经进一步的常规步骤, 制得片剂或胶囊剂。  17. The method of claim 1 wherein: the solid granules obtained by the process of claim 1 are subjected to further conventional procedures to produce tablets or capsules.
18、 如权利要求 1~17任一项所述的方法制得的药物固体制剂。  18. A pharmaceutical solid preparation prepared by the method according to any one of claims 1 to 17.
PCT/CN2011/083285 2010-12-28 2011-12-01 Process for preparing solid medicine preparation and solid medicine preparation therefrom WO2012088992A1 (en)

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