Intrabuccally rapidly disintegrating tablet and a production method of the tablets

Abstract

An intrabuccally rapidly disintegrating tablet which is manufactured by a simple method, has an enough practical hardness and is rapidly disintegrated in the buccal cavity and its production method. The intrabuccally rapidly disintegrating tablet is produced by growing a powder material into a granulated material with a fixed particle diameter, the powder material including a sugar alcohol or a saccharide as main ingredient, each of which is first particle having an average particle diameter of not more than 30 μm, by mixing thus obtained granulated material with an active ingredient and a disintegrant, and by compressing the mixture into a predetermined shape.

Description

BACKGROUND OF THE INVENTION

1. Field of the Invention

This invention relates to tablets rapidly disintegrable in the buccal cavity.

2. Prior Art

There are various types of oral administrative medicines: tablets, capsules, granules, powders, syrups and so on. However, such oral administrative medicines have several problems as follows. As to tablets and capsules, for example, it may be hard for aged person or children whose swallowing power is weak to swallow them. And as to granules and powders, they may cause unpleasantness in the mouth after dosage or they may erroneously happen to enter into a respiratory tract or lungs. Further, they can't be taken where there is no water because water is usually required for dosage. As for syrups, it may be difficult for aged persons or children who can not measure them accurately to take them due to the trouble of measuring them for dosage.

On the other hand, solid medicines which can be rapidly dissolved or disintegrated in the buccal cavity can be taken without measuring nor water, so they may be easily taken by such aged persons or children. Further, such solid medicines can be taken without water.

By the way, there have been developed several types of medicines which can be rapidly dissolved or disintegrated in the buccal cavity on dosing.

For instance, in JP-B-62-50445, solid medicines which can be produced from water solution that mainly contains gelatin including an active ingredient by use of freeze drying method are disclosed. And in WO93/12769, solid medicines which can be produced by drying suspension including agar are also disclosed. However, the medicines produced by the above-mentioned prior methods do not have enough hardness to be taken by pushing out of PTP packages (Press Through Pack) containing the medicines. And, they require a special pharmaceutical technique and also require an enormous investment in plants and equipments.

JP-A-5-271054 and WO93/15724 disclose production methods of tablets wherein tablets composed of a saccharide are produced in such a manner that a saccharide mixture supplied with appropriate water is compressed at a low pressure and then dried to make solid tablets. However, such methods also require a special pharmaceutical technique and have the fear that powder composing the tablets may be adhered to the surface of a metal mold in compression process under moistening condition. It may be therefore difficult to utilize those methods in manufacturing use in a plant.

SUMMARY OF THE INVENTION

From the several pharmaceutical points of view, the inventors of the present invention have examined intrabuccally rapidly disintegrating tablets which don't require a special pharmaceutical production technique and can be simply and easily produced by a normal equipment. As a result, they have developed, as new pharmaceutical tablets, compressed tablets produced by mixing a sugar alcohol such as D-mannitol and a lactose or a saccharide which have an average particle diameter of not more than 30 μm (first particle), an active ingredient and a disintegrant, by granulating the mixture to obtain a granulated material (second particle), and by compressing the granulated material. The tablets can be disintegrated in a buccal cavity within one minute and have hardness without a trouble for practical use, although it has been considered unable to produce for long time.

The present invention relates to the followings;

(1) An intrabuccally rapidly disintegrating tablet comprising: a sugar alcohol or a saccharide, each of which is first particle having an average particle diameter of not more than 30 μm; an active ingredient; and a disintegrant.

(2) An intrabuccally rapidly disintegrating tablet produced by: growing a powder material into a granulated material with a fixed particle diameter, the powder material comprising a sugar alcohol or a saccharide, each of which is first particle having an average particle diameter of not more than 30 μm; mixing thus obtained granulated material with an active ingredient and a disintegrant; and compressing the mixture into a predetermined shape.

(3) An intrabuccally rapidly disintegrating tablet produced by: growing a mixture of a powder material and an active ingredient into a granulated material with a fixed particle diameter, the powder material comprising a sugar alcohol or a saccharide, each of which is first particle having an average particle diameter of not more than 30 μm; mixing thus obtained granulated material with a disintegrant; and compressing the mixture into a predetermined shape.

(4) An intrabuccally rapidly disintegrating tablet produced by: growing a mixture of a powder material and a disintegrant into a granulated material with a fixed particle diameter, the powder material comprising a sugar alcohol or a saccharide, each of which is first particle having an average particle diameter of not more than 30 μm; mixing thus obtained granulated material with an active ingredient; and compressing the mixture into a predetermined shape.

(5) An intrabuccally rapidly disintegrating tablet produced by: growing a mixture of a powder material, an active ingredient and a disintegrant into a granulated material with a fixed particle diameter, the powder material comprising a sugar alcohol or a saccharide, each of which is first particle having an average particle diameter of not more than 30 μm; and compressing the mixture into a predetermined shape.

(6) The intrabuccally rapidly disintegrating tablet as set forth in the above-mentioned (1)-(5) wherein the tablet is compressed into a predetermined shape after adding a lubricant in the granulated material.

(7) The intrabuccally rapidly disintegrating tablet as set forth in the above-mentioned (1)-(5) wherein the tablet is compressed into a predetermined shape after applying a lubricant on material contacting surfaces of punches and dies of a tabletting machine in advance prior to compression procedure.

(8) The intrabuccally rapidly disintegrating tablet as set forth in the above-mentioned (1)-(5) wherein the tablet contains an active ingredient in the amount of 0.01-30% by weight of the tablet, a disintegrant in the amount of 1-10% by weight of the tablet, a sugar alcohol or a saccharide in the amount of 60-95% by weight of the tablet.

(9) The intrabuccally rapidly disintegrating tablet as set forth in the above-mentioned (1)-(5) wherein the tablet contains a disintegrant in the amount of 1-10% by weight.

(10) The intrabuccally rapidly disintegrating tablet as set forth in the above-mentioned (1)-(5) wherein the sugar alcohol is D-mannitol.

(11) The intrabuccally rapidly disintegrating tablet as set forth in the above-mentioned (1)-(5) wherein the saccharide is a lactose.

(12) The intrabuccally rapidly disintegrating tablet as set forth in the above-mentioned (1)-(5) wherein the disintegrant is at least one selected from the group consisting of crosspovidone, crosscarmellose sodium, or low substituted hydroxypropycellulose.

(13) The intrabuccally rapidly disintegrating tablet as set forth in the above-mentioned (1)-(5) wherein a disintegration time in the buccal cavity of the tablet is not more than 1 minute.

(14) The intrabuccally rapidly disintegrating tablet as set forth in the above-mentioned (1)-(5) wherein the tablet has a hardness of 4 kg and the tablet goes down through a No. 10 mesh wire within 30 seconds when the tablet is placed on the mesh wire and a drop of water is fallen onto the tablet at a speed of 4 ml per minute.

(15) The intrabuccally rapidly disintegrating tablet as set forth in the above-mentioned (1)-(5) wherein the sugar alcohol or the saccharide is prepared in advance to be pulverized into an average particle size of not more than 30 μm.

(16) A production method of an intrabuccally rapidly disintegrating tablet, comprising the steps of:

• • a) growing a powder material comprising a sugar alcohol or a saccharide, each of which is first particle having an average particle size of not more than 30 μm, into a granulated material with predetermined size;
  • b) mixing thus obtained granulated material with an active ingredient and a disintegrant, adding a lubricant; and
  • c) compressing the mixture thus produced as above into a predetermined shape.

(17) A production method of an intrabuccally rapidly disintegrating tablet, comprising the steps of:

• • a) growing a mixture of a powder material and an active ingredient, the powder material comprising a sugar alcohol or a saccharide, each of which is first particle having an average particle size of not more than 30 μm, into a granulated material with a predetermined size;
  • b) mixing thus obtained granulated material with and a disintegrant, adding a lubricant; and
  • c) compressing the mixture thus produced as above into a predetermined shape.

(18) A production method of an intrabuccally rapidly disintegrating tablet, comprising the steps of:

• • a) growing a mixture of a powder material and a disintegrant, the powder material comprising a sugar alcohol or a saccharide, each of which is first particle having an average particle size of not more than 30 μm, into a granulated material with a predetermined size;
  • b) mixing thus obtained granulated material with an active ingredient, adding a lubricant; and
  • c) compressing the mixture thus produced as above into a predetermined shape.

(19) A production method of an intrabuccally rapidly disintegrating tablet, comprising the steps of:

• • a) growing a mixture of a powder material, an active ingredient, and a disintegrant, the powder material comprising a sugar alcohol or a saccharide, each of which is first particle having an average particle size of not more than 30 μm, into a granulated material with a predetermined size;
  • b) mixing thus obtained granulated material, adding a lubricant; and
  • c) compressing the mixture thus produced as above into a predetermined shape.

(20) The production method of an intrabuccally rapidly disintegrating tablet as set forth in the above-mentioned (16)-(19) wherein the sugar alcohol or the saccharide is prepared in advance to be pulverized into an average particle size of not more than 30 μm.

(21) A production method of an intrabuccally rapidly disintegrating tablet, comprising the steps of:

• • a) growing a powder material comprising a sugar alcohol or a saccharide, each of which is first particle having an average particle size of not more than 30 μm, into a granulated material with a predetermined size;
  • b) mixing thus obtained granulated material with an active ingredient and a disintegrant, without adding a lubricant; and
  • c) further comprising the steps for compressing the mixture thus produced as above;
  • d) spraying a lubricant on material contacting surfaces of punches and dies of a tabletting machine as a pre-compression step; and
  • e) compressing the mixture supplied to the die of the tabletting machine into a predetermined shape.

(23) A production method of an intrabuccally rapidly disintegrating tablet, comprising the steps of:

• • a) growing a mixture of a powder material and an active ingredient, the powder material comprising a sugar alcohol or a saccharide, each of which is first particle having an average particle size of not more than 30 μm, into a granulated material with a predetermined size;
  • b) mixing thus obtained granulated material with a disintegrant, without adding a lubricant; and
  • further comprising the steps for compressing the mixture thus produced as above;
  • c) spraying a lubricant on material contacting surfaces of a punches and dies of a tabletting machine as a pre-compression step; and
  • d) compressing the mixture supplied to the die of the tabletting machine into a predetermined shape.

(23) A production method of an intrabuccally rapidly disintegrating tablet, comprising the steps of:

• • a) growing a mixture of a powder material and a disintegrant, the powder material comprising a sugar alcohol or a saccharide, each of which is first particle having an average particle size of not more than 30 μm, into a granulated material with a predetermined size;
  • b) mixing thus obtained granulated material with an active ingredient, without adding a lubricant; and
  • further comprising the steps for compressing the mixture thus produced as above;
  • c) spraying a lubricant on material contacting surfaces of punches and dies of a tabletting machine as a pre-compression step; and
  • d) compressing the mixture supplied to the die of the tabletting machine into a predetermined shape.

(24) A production method of an intrabuccally rapidly disintegrating tablet, comprising the steps of:

• • a) growing a mixture of a powder material, an active ingredient and a disintegrant, the powder material comprising a sugar alcohol or a saccharide, each of which is first particle having an average particle size of not more than 30 μm, into a granulated material with a predetermined size;
  • b) mixing thus obtained granulated material without adding a lubricant; and further comprising the steps for compressing the mixture thus produced as above into a predetermined shape;
  • c) spraying a lubricant on material contacting surfaces of punches and dies of a tabletting machine as a pre-compression step; and d) compressing the mixture supplied to the die of the tabletting machine into a predetermined shape.

(25) The production method of an intrabuccally rapidly disintegrating tablet as set forth in the above-mentioned (21)-(24) wherein the sugar alcohol or the saccharide is prepared in advance to be pulverized into an average particle size of not more than 30 μm.

(26) An intrabuccally rapidly disintegrating tablet comprising: a sugar alcohol or a saccharide of which average particle size is not more than 30 μm as a main ingredient; an active ingredient; and a disintegrant, wherein the main ingredient is contained in the amount of 60-95% by weight of the tablet and the disintegrant is contained in the amount of 1-10% by weight of the tablet.

(27) The intrabuccally rapidly disintegrating tablet as set forth in the above-mentioned (26), the tablet is produced by: granulating a mixture of the main ingredient, the active ingredient and the disintegrant; mixing thus granulated material with a fixed amount of lubricant and a required adjuvant; and compressing thus mixed material into a predetermined shape.

(28) The intrabuccally rapidly disintegrating tablet as set forth in the above-mentioned (26), the tablet is produced by: granulating a mixture of the main ingredient, the active ingredient and the disintegrant; mixing thus granulated material without adding a lubricant; applying a lubricant on punches and dies of a tabletting machine; and compressing thus mixed material into a predetermined shape.

(29) The intrabuccally rapidly disintegrating tablet as set forth in the above-mentioned (26)-(28) wherein the main ingredient is either one of D-mannitol or a lactose.

(30) The intrabuccally rapidly disintegrating tablet as set forth in the above-mentioned (26)-(29) wherein the disintegrant is at least one selected from the group consisting of crosspovidone, crosscarmellose sodium, or low substituted hydroxypropycellulose.

(31) The intrabuccally rapidly disintegrating tablet as set forth in the above-mentioned (30) wherein the tablet contains 1 to 30 mg disintegrant for one dosage.

(32) A production method of an intrabuccally rapidly disintegrating tablet comprising a sugar alcohol or a saccharide of which average particle size is not more than 30 μm as a main ingredient, an active ingredient, and a disintegrant wherein the main ingredient is contained 60-95% by weight of the tablet and the disintegrant is contained 1-10% by weight of the tablet, comprising the steps of: producing a mixture of the main ingredient, the active ingredient and the disintegrant; mixing the mixture with a fixed amount lubricant and a required adjuvant; and compressing thus mixed material into a predetermined shape.

(33) A production method of an intrabuccally rapidly disintegrating tablet comprising a sugar alcohol or a saccharide of which average particle size is not more than 30 μm as a main ingredient, an active ingredient, and a disintegrant wherein the main ingredient is contained in the amount of 60-95% by weight of the tablet and the disintegrant is contained in the amount of 1-10% by weight of the tablet, comprising the steps of: producing a mixture of the main ingredient, the active ingredient and the disintegrant; granulating the mixture into a predetermined size; mixing thus granulated material with a required adjuvant without adding a lubricant; applying a lubricant on punches and dies of a tabletting machine; and compressing thus mixed material into a predetermined shape.

Generally, first particle refers to single particle of raw material. In this specification, first particle means a single particle of raw material in nature and doesn't mean particle of an aggregation. Generally, second particle refers to particle in which special process is executed for the first particle. Second particle in this specification means particle after some process such as granulation is executed, namely particle of granulated material which is an aggregation of first particle (for example granule).

The object of the present invention is to provide an intrabuccally rapidly disintegrating tablet which includes a sugar alcohol or a saccharide of which is first particle having not more than 30 μm in average particle size, further includes an active ingredient and a disintegrant and which is produced by compressing into a predetermined shape.

The method of producing the intrabuccally rapidly disintegrating tablet according to the present invention includes an internal lubrication method in which a powder material and a lubricant are mixed before compression and an external lubrication method in which a lubricant is applied on punches and dies of a tabletting machine before compression.

D-mannitol can be used as a sugar alcohol in the present invention, and a lactose can be used as a saccharide. At least one kind of a sugar alcohol or a saccharide is used.

As active ingredients, followings are used, but other ingredients for oral administration can be also used.

<Drug for Central Nervous System>

hyprotics, anxiolytics . . . amobarbital, alprazolam, flurazepam hydrochloride, diazepam, and so on

NTHEs/antiepileptic . . . valproate sodium, nitrazepam, phenytoin, and so on

analgesic antipyretic agent . . . aspirin, acetaminophen, ibuprofen, diclofenac sodium, ethenzamide, indometacin and so on

drug for Pakinson's disease . . . levodopa, amantadine hydrochloride, trihexyphenidyl hydrochloride, piroheptine hydrochloride, and so on

psychoneurosis agent . . . etizolam, amitriptyline hydrochloride, sulpiride, and so on

<Drug for Peripheral Nervous System>

skeletal muscle relaxant . . . chlorphenesin carbamate, chlormezanone, and so on

autonomic nervous agent . . . valethamate bromide, tofisopam, and so on

antispasmodic . . . afloqualone, and so on

<Drug for Circulatory>

cardiac . . . ubidecarenon, aminophylline, etilefrine hydrochloride, and so on

antiarrhythmic agents . . . atenolol, pindolol, and so on

diuretic . . . spironolactone, trichlormethiazide, furosemide, and so on

antihypertensive agent . . . todrazine hydrochloride, nicardipine hydrochloride, hydralazine hydrochloride, and so on

angiotonic . . . dihydroergotamine mesilate and so on

vasodilator . . . benidipine hydrochloride, diltiazem hydrochloride, isosorbide dinitrate, and so on

hyperlipemia . . . clinofibrate, nicomol, and so on

others . . . flunarizine hydrochloride, meclofenoxate hydrochloride, cinnarizine, and so on

<Antidiarrhea>

antidiarrhoeic . . . loperamide hydrochloride, dimeticone, and so on

drug for peptic ulcer . . . azulene, L-glutamine, aceglutamide aluminium, cetraxate hydrochloride, cimetidine, and so on

cholagogue . . . anetholtrithion, chenodeoxycholic acid, and so on

others . . . donperidone, trimebutine maleate, metoclopramide, cisapride, and so on

<Metabolic Drug>

vitamin . . . alfacarcidol, tiamine hydrochloride, cobamide, vitaroxin, riboflavin butyrate, ascorbic acid, phytonadione, and so on

diabetes mellitus agent . . . glybuzole, tolbutamide, and so on

<Antiallergies>

antihistamine . . . homochlorcyclizine hydrochloride, clemastine fumarate, chlorpheniramine maleate, and so on

others . . . oxatomide, ketotifen fumarate, azelastin hydrochloride, and so on

<Antineoplastics>

metabolic antagoism agent . . . fluorouracil, tegafur, and so on

<Antibiotics>

paromomycin sulfate, amoxicillin, cefaclor, cefalexin, acetylspiramycin, minocycline hydrochloride

Wherein such as crosspovidone, cross sodium carboxymethyl cellulose, low substituted hydroxypropylcellulose or the like, which are widely used for drugs and food can be used as a disintegrant. At least one kind of disintegrant is used.

Next, a production method of tablets according to the present invention will be described hereinafter.

The tablets of the present invention can be obtained by compressing and tabletting after granulating a mixed powdered components containing a sugar alcohol or a saccharide of which is first particle having an average particle diameter of not more than 30 μm, an active ingredient, and a disintegrant by means of a hammer mill, a jet mill or the like.

The amount of sugar alcohol or saccharide is preferably about 60-95 weight % in the amount of a resulting tablet, more preferably about 80-95 weight % of a resulting tablet.

The amount of active ingredient is different depending on the kind and dosage amount of active ingredient, however, about 0.01-30 weight % in the amount of a resulting tablet is preferable, and more preferably about 0.01-10 weight % of a resulting tablet.

The amount of disintegrant present is preferably about 1-30 mg per dosage, and more preferably about 1-10 weight % in the amount of a resulting tablet.

A granulation method isn't limited, however a wet granulation method using purified water, ethanol or the like can be preferably used. In the method, for example, granulation can be executed by means of a fluid-bed granulator, a rotary stirring granulator or an extruding granulator. The granulated material is dried, mixed with a lubricant, and thereafter compressed into a predetermined shape. Binders, sour agents, foaming agents, sweetening agents, flavoring agents, or colorants can be added as additives. Otherwise, a dry granulation method may be used.

As a lubricant, such as magnesium stearate, calcium stearate stearic aid, stearic acid, stearyl alcohol, sucrose esters of fatty acid, talc, light anhydrous silicic acid, or like present. Binders present, for example, hydroxypropyl-cellulose, polyvinylphrrolidone, hydroxypropyl-methylcellulose, partially saponificated polyvinyl alcohol, methylcellulose, pullulan or the like. Sour agents present citric acid, malic acid, adipic acid, ascorbic acid, and the like. Foaming agents are sodium bicarbonate, sodium carbonate, calcium carbonate, and the like. Sweetening agents are aspartame (TM), saccharin, glycyrrhizic acid or the like. Flavoring agents are lemon, orange, pine, mint, menthol or the like. Colorants are yellow iron sesquioxide, red iron sesquioxide, tar color or the like.

The amount of lubricant is preferably about 0.01-2 weight % in the amount of a tablet and more preferably about 0.01-0.5 weight %.

Such an intrabuccally rapidly disintegrating tablet of the present invention can be produced by an internal lubrication method wherein a lubricant is internally contained in the tablet by mixing a lubricant into the granule prior to compression. Further, it can be produced also by an external lubrication method wherein a lubricant isn't included in the tablet and is externally attached to the outer surface of the tablet by applying a lubricant onto the material contacting surfaces of punches and dies of a tabletting machine.

In both of the internal lubrication method and the external lubrication method, there are several compression methods: after granulating a sugar alcohol or a saccharide, an active ingredient and a disintegrant are mixed and compression is executed; after granulating a sugar alcohol or a saccharide and an active ingredient, a disintegrant is mixed and compression is executed; after granulating a sugar alcohol or a saccharide and a disintegrant, an active ingredient is mixed and compression is executed; after granulating a sugar alcohol or a saccharide, an active ingredient and a disintegrant, compression is executed.

Although a tabletting method isn't limited in the present invention, a rotary tabletting machine, a hydraulic press machine or a single punch tabletting machine which have high productivity can be more preferably used.

The shape of tablets obtained in the present invention can be pills or other shapes such as normal R surface (concave plane surface) tablets, a sugar coated R surface tablets, tablets with square edges, tablets with rounded edges, or tablets with two R surfaces, or the like.

The tablet may be a dividable tablet with a dividing line.

DESCRIPTION OF THE PREFERRED EMBODIMENTS

The present invention will be concretely explained according to preferable embodiments and comparative embodiments as described in following experimental data.

[Comparison 1]

1890 g of D-mannitol (Towa Kasei Co., Ltd., average particle diameter of about 60 μm) and 100 g of crosspovidone (POLYPLASDONE XL-10: GAF Co., Ltd.) were fed in a fluid-bed granulation dryer (Gratt Co., Ltd.: WSG-type 5), and purified water was sprayed in the dryer to produce a granulated material and the material thus grown after the granulation was dried. 10 g of magnesium stearate was added and mixed with the granulated material, and they were compressed and tabletted with a rotary tabletting machine (Kikusui Co., Ltd., clean press collect type 12) in which the tabletting conditions were as follows; tablet weight was 200 mg, a metal mold was 8 mm diameter flat-type, and compression pressure was varied such as 150 kg, 300 kg, 450 kg, 600 kg, and 800 kg to produce resulting tablets.

Embodiment 1

D-mannitol (Towa Kasei Co., Ltd.: average particle diameter of about 60 μm) was previously ground by a jet mill (Japan Pneumatic Co., Ltd.: type PJM-I-1.5) and the pulverized D-mannitol with average particle diameter of 20 μm was obtained. 1890 g of the pulverized D-mannitol and 100 g of crosspovidone (POLYPLASDONE XL-10: GAF Co. Ltd.) were fed in a fluid-bed granulation dryer (Gratt Co., Ltd.: WSG-type 5), purified water was sprayed, and a granulated material was obtained after granulation and drying process. 10 g of magnesium stearate was added and mixed with the granulated material and they were compressed and tabeletted with a rotary tabletting machine (Kikusui Co., Ltd., clean press collect type 12) in which tabletting conditions were the same as that in the Comparison 1.

[Comparison 2]

100 g of donperidone, gastrointestinal motility improvement agent, 1790 g of lactose (DMV Co., Ltd.: average particle diameter of about 80 μm) and 100 g of crosspovidone (POLYPLASDONE XL-10: GAFCo., Ltd.) were fed in a fluid-bed granulation dryer (Gratt Co., Ltd.: WSG-type5), purified water was sprayed in the dryer, and a granulated material was obtained after granulation and drying process. 10 g of magnesium stearate was added and mixed with the granulated material and they were compressed and tabeletted with a rotary tabletting machine (Kikusui Co., Ltd.: CLEAN PRESS COLLECT type 12) in which tabletting conditions were the same as that in the Comparison 1.

Embodiment 2

Lactose (DMV Co., Ltd.: average particle diameter of about 80 μm) was previously ground by a jet mill (Japan Pneumatic Co., Ltd.: type PJM-I-1.5) to produce pulverized lactose with average particle diameter of 15 μm. 1790 g of the pulverized lactose, 100 g of donperidone, and 100 g of crosspovidone (POLYPLASDONE XL-10: GAF Co., Ltd.) were fed in a fluid-bed granulation dryer (Gratt Co., Ltd.: WSG-type 5), purified water was sprayed in the dryer, and a granulated material was obtained after granulation and drying process. 10 g of magnesium stearate was added and mixed with the granulated material and they were compressed and tabeletted with a rotary tabletting machine (Kikusui Co., Ltd., CLEAN PRESS COLLECT TYPE 12) in which tabletting conditions were the same as that in the Comparison 1.

Embodiment 3

The granulated material obtained in the Embodiment I was tabletted under the condition that the tablet weight was 200 mg and the compression pressure was 50 kg/cm², and a little magnesium stearate was coated on a metal mold (8 mm diameter flat-type) and dies of a hydraulic press machine (Riken Seiki Co., Ltd.: type P-1B) to obtain a tablet.

Table 1 shows the evaluation result of the hardness and disintegration time of the tablets obtained by the Embodiments 1 and 2 and the Comparisons 1 and 2.

The hardness of the tablets was measured by a tablet destructive strength measuring instrument (Toyama Sangyo Co., Ltd.: TH-203CP type), and as for the disintegration time test of the tablets, a unique measuring method (called as DW (Drops Water) method hereinafter) was used because a disintegration test method according to the Japanese Pharmacopoeia is different from the actual condition in the buccal cavity. In the DW method, while resulting tablets were placed on a No. 20 wire cloth, onto which water was dropped at a speed of 4 ml/min., and the time till the tablets fall down through the wire cloth was measured as the disintegration time.

TABLE 1
sample/
compression	pressure	150 kg	300 kg	450 kg	600 kg	800 kg
Comparison 1	Hardness	hard to be	hard to be	hard to be	1.9	kgf	2.3	kgf
		tableted	tableted	tableted
	disintegration	—	—	—	20	sec.	22	sec.
Embodiment 1	Hardness	1.9	kgf	3.9	kgf	5.1	kgf	6.2	kgf	7.3	kgf
	disintegration	10	sec.	l5	sec.	16	sec.	19	sec.	27	sec.
Comparison 2	Hardness	hard to be	hard to be	hard to be	1.5	kgf	2.1	kgf
		tableted	tableted	tableted
	disintegration	—	—	—	18	sec.	21	sec.
Embodiment 2	Hardness	1.6	kgf	4.0	kgf	4.9	kgf	5.8	kgf	6.5	kgf
	disintegration	10	sec.	16	sec.	20	sec.	25	sec.	29	sec.

In the Comparisons 1 and 2, it was found that it was hard to mold a tablet by adding under 450 kg compression pressure but it was possible to mold a tablet by adding more than around 600 kg compression pressure, while the hardness of the resulting tablets wasn't enough to practical use.

In the Embodiments 1 and 2, it was found that the tablet hardness enough for practical use could be obtained by adding more than 300 kg compression pressure and its disintegration time was very fast.

When the resulting tablet produced at 450 kg compression pressure according to the Embodiment 1 was dosed, the tablet was disintegrated at 10 seconds in the buccal cavity.

On the other hand, such resulting tablets with less than 30 seconds of the disintegration time of which testing was conducted in the above mentioned DW method were dissolved within 10 seconds in the buccal cavity, and represented such rapid disintegration speed that hasn't been experienced as a prior disintegrating tablets.

The tablets obtained by the Embodiments 3 were also measured of its hardness and disintegration time in the same way as above mentioned. As the result, the resulting tablets had enough hardness of about 6.5 kgf and its disintegration time was 10 seconds.

Embodiment 4

D-mannitol with average particle diameter of 60 μm (Towa Kasei Co., Ltd.) was previously ground by a jet mill (Japan Pneumatic Co, Ltd.: type PJM-I-1.5) to obtain D-mannitol with average particle diameter of 15 μm as first particle.

D-mannitol thus pulverized of 1880 g by weight and crosspovidone (POLYPLASDONE XL-10: ISP Co., Ltd.) of 100 g by weight were fed into a mixing granulator (Powrex Corporation: type VG-25), mixed with each other, and then the mixture was subjected to granulation with purified water for growing. Thereafter, the granulated material thus grown was dried by a fluid bed dryer to obtain a granulated material with average particle diameter of about 342 μm as second particle. Then 20 g of magnesium stearate was added into the granulated material and 200 g of the mixed granulated material were compressed and tabletted with a rotary tabletting machine (CLEAN PRESS COLLECT TYPE 12, 8 mmφ flat mold, Kikusui Co., Ltd.) at a pressure of 500 kg.

Embodiment 5

Second particle with average particle diameter of 334 μm as a granulated material was produced from the first particle with average particle diameter of about 30 μm and a tablet was obtained by executing compressing and tabletting as in the same manner as in the Embodiment 4.

[Comparison 3]

Second particle with average particle diameter of 315 μm as a granulated material was produced from the first particle with average particle diameter of about 60 μm and a tablet was obtained by executing compressing and tabletting as in the same manner as in the Embodiment 4.

Embodiment 6

Second particle with average particle diameter of 158 μM as a granulated material was produced from the first particle with average particle diameter of about 15 μm and a tablet was obtained by executing compressing and tabletting as in the same manner as in the Embodiment 4.

Embodiment 7

Second particle with average particle diameter of 554 μm as a granulated material was produced from the first particle with average particle diameter of about 15 μm and a tablet was obtained by executing compressing and tabletting as in the same manner as in the Embodiment 4.

[Comparison 4]

D-mannitol with average particle diameter of 60 μm (Towa Kasei Co., Ltd.) was previously ground by a jet mill (Japan Pneumatic Co., Ltd.: type PJM-I-1.5) to obtain D-mannitol with average particle diameter of 15 μm as first particle.

D-mannitol thus pulverized of 1880 g by weight and crosspovidone (POLYPLASDONE XL-10: ISP Co., Ltd.) of 100 g by weight were fed into a mixing granulator (Powrex Corporation: type VG-25), and mixed with each other, then the mixture was subjected to granulation with purified water with 40 g of polyvinyl-pyrrolidone K30 dissolved for growing to obtain a granulated material. Then the granulated material thus grown was dried by a fluid bed dryer, thereby producing a granulated material with average particle diameter of about 350 μm as second particle. Thereafter, 20 g of magnesium stearate was added into the granulated material and 200 mg of the mixed granulated material was compressed and tabletted with a rotary tabletting machine (CLEAN PRESS COLLECT TYPE 12, 8 mmφ flat mold, Kikusui Co., Ltd.) under a pressure of 500 kg to produce a resulting tablet with a specific shape.

[Comparison 5]

Second particle with average particle diameter of 325 μm as a granulated material was produced from the first particle with average particle diameter of about 60 μm and a tablet was produced by executing compressing and tabletting as in the same manner as in Comparison 4.

[Comparison 6]

1780 g of D-mannitol with average particle diameter of 60 μm was fed into a mixing granulator (Powrex Corporation: type VG-25), was subjected to granulation with purified water being dissolved with 200 g of maltose for growing, and then dried to obtain a granulated material with average particle diameter of about 333 μm as second particle. Thereafter, 20 g of magnesium stearate was added into the granulated material and 200 mg of the mixed granulated material was compressed and tabletted with a rotary tabletting machine (CLEAN PRESS COLLECT TYPE 12, 8 mmφ flat mold, Kikusui Co., Ltd.) under a pressure of 500 kg to produce a resulting tablet with a specific shape.

[Comparison 7]

D-mannitol with average particle diameter of 60 μm and crosspovidone (POLYPLASDONE XL-10: ISP Co., Ltd.) of 100 g by weight were fed into a mixing granulator (Powrex Corporation: type VG-25), mixed with each other, and then the mixture was subjected to granulation with purified water with 200 g of maltose dissolved for growing, and then dried to obtain a granulated material with average particle diameter of about 339 μm as second particle. Thereafter, 20 g of magnesium stearate was added into the granulated material and 200 g of the mixed granulated material was compressed and tabletted with a rotary tabletting machine (CLEAN PRESS COLLECT TYPE 12, 8 mmφ flat mold, Kikusui Co., Ltd.) with a pressure of 500 kg.

[Comparison 8]

D-mannitol with average particle diameter of 60 μm (Towa Kasei Co., Ltd.) was previously ground by a jet mill (Japan Pneumatic Co., Ltd.: type PJM-I-1.5) to obtain D-mannitol with average particle diameter of 15 μm as first particle. D-mannitol of 1840 g thus pulverized, crosspovidone (POLYPLASDONE XL-10: GAF Co., Ltd.) of 100 g were fed into a mixing granulator (Powrex Corporation: type VG-25) to be mixed with each other, and the mixture was subjected to granulation with purified water dissolving 40 g of hydroxypropylcellulose (L-HPC, Shin-Etsu Chemical Co., Ltd.) for growing. Then 20 g of magnesium stearate was added into the granulated material and 200 mg of the mixed material was compressed and tabletted with a rotary tabletting machine (CLEAN PRESS COLLECT TYPE 12, 8 mmφ flat mold, Kikusui Co., Ltd.) with a pressure of 500 kg to obtain a resulting tablet with a specific shape.

The intrabuccal method in the table 2 was measured as follows:

Each one of five healthy adults took one tablet in the mouth and the time the tablet was dissolved in the buccal cavity with saliva was measured. The average value of five persons was calculated and considered as disintegration time in the buccal cavity.

TABLE 2
Effect of Particle Size on the hardness of resulting tablet
	1st	2nd	hardness	disintegration time (sec)
	particle	particle	(kg)	intrabuccal	DW	JP
Embodiment 4	15	342	5.2	kg	9	9	4
Embodiment 5	30	334	3.5		8	10	5
Comparison 3	60	315	1.2		10	15	7
Embodiment 6	15	158	5.5		8	8	5
Embodiment 7	15	554	5.6		10	7	5
Comparison 4	15	350	4.9		350	152	139
Comparison 5	60	325	3.5		303	146	121
Comparison 6	60	333	3.5		286	125	105
Comparison 7	60	339	4.1		215	99	95
Comparison 8	15	350	4.3		101	76	64

Preparation using a saccharide or a sugar alcohol which is first particle having an average particle diameter not more than 30 μm could obtain a practical tablet hardness and rapid disintegration time despite of the size of second particle. On the other hand, if a saccharide or a sugar alcohol of which average particle diameter had 60 μm was used, rapid disintegration time was achieved but enough tablet hardness wasn't obtained. Accordingly it was found that the size of first particle, not secondary particle, was important in order to obtain enough tablet hardness and rapid disintegration.

Comparing with disintegration time in a buccal cavity, that by DW method and that by the Japanese Pharmacopeia (JP) method, the tablet showing about 10 seconds of disintegration time in a buccal cavity showed the same disintegration time in DW method and the JP method. However, the tablet showing more than 100 seconds of disintegration time in the buccal cavity showed faster disintegration time in DW method and the JP method than that in the buccal cavity. Comparing DW method and the JP method, DW method showed disintegration time closer to that in the buccal cavity. The tablet showing about 60 seconds of disintegration time in the JP method required about 100 seconds to be disintegrated in the buccal cavity, namely it couldn't be rapidly disintegrated in the buccal cavity.

Embodiment 8

D-mannitol with average particle diameter of 60 μm (Towa Kasei Co., Ltd.) was previously ground by a jet mill (Japan Pneumatic Co., Ltd.: type PJM-I-1.5) to obtain D-mannitol with average particle diameter of 20 μm as first particle. D-mannitol thus pulverized of 1710 g, donperidone of 170 g, and cross carmellose sodium of 100 g (Ac-Di-Sol, Asahi Kasei Corporation) were fed into a mixing granulator (Powrex Corporation: type VG-25) to be mixed with each other, and the mixture was subjected to granulation with purified water for growing. Thereafter the granulated material thus grown was dried by a fluid bed dryer and classified by a No. 20 wire mesh. Then 20 g of magnesium stearate was added into the granulated material and 120 mg of thus obtained material was compressed and tabletted with a rotary tabletting machine (CLEAN PRESS COLLECT TYPE 12, 8 mmφ flat mold, Kikusui Co., Ltd.) with a pressure of 500 kg to obtain a resulting tablet of which hardness was 4.2 kg, disintegration time in the buccal cavity was 28 seconds and disintegration time by DW method was 26 seconds.

Embodiment 9

D-mannitol with average particle diameter of 60 μm (Towa Kasei Co., Ltd.) was previously ground by a jet mill (Japan Pneumatic Co., Ltd.: type PJM-I-1.5) to obtain D-mannitol with average particle diameter of 15 μm as first particle. D-mannitol of 1710 g thus pulverized, donperidone of 170 g, and low substituted hydroxypropylcellulose of 100 g (L-HPC, Shin-Etsu Chemical Co., Ltd.) were fed into a mixing granulator (Powrex Corporation: type VG-25) to be mixed with each other, and the mixtures was subjected to granulation with purified water for growing. Thereafter, the granulated material was dried by a fluid bed dryer and classified by a No. 20 wire mesh. Then 20 g of magnesium stearate was added into the granulated material and 120 mg of thus obtained material was compressed and tabletted with a rotary tabletting machine (CLEAN PRESS COLLECT TYPE 12, 8 mmφ flat mold, Kikusui Co., Ltd.) with a pressure of 500 kg to obtain a resulting tablet of which hardness was 5.0 kg, disintegration time in the buccal cavity was 30 seconds and disintegration time by DW method was 21 seconds.

Embodiment 10

D-mannitol (average particle diameter: 65 μm, Towa Kasei Co., Ltd.) was previously ground by a jet mill (Japan Pneumatic Co., Ltd.: type PJM-I-1.5) to obtain D-mannitol with average particle diameter of 25 μm. D-mannitol thus pulverized of 1790 g and donperidone of 100 g were fed into a mixing granulator (Powrex Corporation: type VG-25) to be mixed with each other, and the mixture was subjected to granulation with purified water for growing. Thereafter, the granulated material thus grown was dried by a fluid bed dryer (Gratt Co., Ltd.: WSG-type 5) and classified by a No. 20 wire mesh. Then 1512 g of thus obtained granulated material, 80 g of crosspovidone (POLYPLASDONE XL-10: GAF Co., Ltd.) and 8 g of magnesium stearate were mixed and compressed to be tabeletted with a rotary tabletting machine (CLEAN PRESS COLLECT TYPE 12, Kikusui Co., Ltd.). The tabletting conditions were such that the weight of tablet was 200 mg, the mold was 8 mm diameter and flat type and the tabletting pressure was 800 kg. The obtained tablet had 5.7 kgf of hardness and 12 seconds of disintegration time by a DW method. The actual disintegration time in the buccal cavity was about 10 seconds.

Embodiment 11

1790 g of pulverized D-mannitol which had been obtained like in the Embodiment 10 was fed into a mixing granulator (Powrex Corporation: type VG-25), and mixed with each other, then the mixture was subjected to granulation with purified water for growing. Thereafter, the granulated material thus grown was dried by a fluid bed dryer (Gratt Co., Ltd.: WSG-type 5) and classified by a No. 20 wire mesh. Then 1432 g of thus obtained granulated material, 80 g of donperidone as active ingredient, 80 g of crosspovidone, 8 g of magnesium stearate were mixed and compressed to be tabletted with a rotary tabletting machine (CLEAN PRESS COLLECT TYPE 12, Kikusui Co., Ltd.). The tabletting conditions were the same as the Embodiment 10. The obtained tablet had 5.2 kgf of hardness and 14 seconds of disintegration time by a DW method. The actual disintegration time in the buccal cavity was about 10 seconds.

Embodiment 12

1790 g of pulverized D-mannitol which had been obtained like in the Embodiment 10 and 100 g of crosspovidone were fed into a mixing granulator (Powrex Corporation: type VG-25), and mixed with each other, then the mixtures was subjected to granulation with purified water for growing. Thereafter, the granulated material thus grown was dried by a fluid bed dryer (Gratt Co., Ltd.: WSG-type 5) and classified by a No. 20 wire mesh. Then 1512 g of thus obtained granulated material, 80 g of donperidone as active ingredient, 8 g of magnesium stearate were mixed and compressed to be tabletted with a rotary tabletting machine (CLEAN PRESS COLLECT TYPE 12, Kikusui Co., Ltd.). The tabletting conditions were the same as the Embodiment 10. The obtained tablet had 5.9 kgf of hardness and 12 seconds of disintegration time by DW method. The actual disintegration time in the buccal cavity was about 10 seconds.

Embodiment 13

1790 g of pulverized D-mannitol which had been obtained like in the Embodiment 10, 100 g of donperidone as active ingredient and 100 g of crosspovidone were fed into a mixing granulator (Powrex Corporation: type VG-25), and mixed with each other, then the mixture was subjected to granulation with purified water for growing. Thereafter the granulated material thus grown was dried by a fluid bed dryer (Gratt Co., Ltd.: WSG-type 5) and classified by a No. 20 wire mesh. Then 1592 g of thus obtained granulated material, 8 g of magnesium stearate were mixed and compressed to be tabletted with a rotary tabletting machine (CLEAN PRESS COLLECT TYPE 12, Kikusui Co., Ltd.). The tabletting conditions were the same as the Embodiment 10. The obtained tablet had 6.0 kgf of hardness and 15 seconds of disintegration time by DW method. The actual disintegration time in the buccal cavity was about 10 seconds.

Embodiment 14

1790 g of pulverized D-mannitol which had been obtained like in the Embodiment 10, 100 g of donperidone as active ingredient and 100 g of cross carmellose sodium (Ac-Di-Sol, Asahi Kasei Corporation) were fed into a mixing granulator (Powrex Corporation: type VG-25), and mixed with each other, then the mixture was subjected to granulation with purified water for growing. Thereafter the granulated material thus grown was dried by a fluid bed dryer (Gratt Co., Ltd.: WSG-type 5) and classified by a No. 20 wire mesh. Then 1592 g of thus obtained granulated material, 8 g of magnesium stearate were mixed and compressed to be tabletted with a rotary tabletting machine (CLEAN PRESS COLLECT TYPE 12, Kikusui Co., Ltd.). The tabletting conditions were the same as the Embodiment 10. The obtained tablet had 4.5 kgf of hardness and 26 seconds of disintegration time by DW method. The actual disintegration time in the buccal cavity was about 20 seconds.

Embodiment 15

1790 g of pulverized D-mannitol which had been obtained like in the Embodiment 10, 100 g of donperidone as active ingredient and 100 g of low substituted hydroxypropylcellulose (L-HPC, Shin-Etsu Chemical Co., Ltd) were fed into a mixing granulator (Powrex Corporation: type VG-25), and mixed with each other, then the mixture was subjected to granulation with purified water for growing. Thereafter, the granulated material thus grown was dried by a fluid bed dryer (Gratt Co., Ltd.: WSG-type 5) and classified by a No. 20 wire mesh. Then 1592 g of thus obtained granulated material, 8 g of magnesium stearate were mixed and compressed to be tabletted with a rotary tabletting machine (CLEAN PRESS COLLECT TYPE 12, Kikusui Co., Ltd.). The tabletting conditions were the same as the Embodiment 10.

The obtained tablet had 6.2 kgf of hardness and 25 seconds of disintegration time by W method. The actual disintegration time in the buccal cavity was about 20 seconds.

Embodiment 16

1790 g of pulverized D-mannitol which had been obtained like in the Embodiment 10, 100 g of donperidone as active ingredient and 100 g of crosspovidone were fed into a mixing granulator (Powrex Corporation: type VG-25), and mixed with each other, then the mixture was subjected to granulation with purified water for growing. Thereafter, the granulated material thus grown was dried by a fluid bed dryer (Gratt Co. Ltd.: WSG-type 5) and classified by a No. 20 wire mesh. Thus obtained granulated material was tabletted with a rotary tabletting machine (Hata Seisakusho, Type AP-15) with a pressure of 500 kg while spraying stearate magnesium from a lubricant spray attached to the tabletting machine. The obtained tablet had 6.7 kgf of hardness and 12 seconds of disintegration time by a DW method. The actual disintegration time in the buccal cavity was about 6 seconds.

According to the above-mentioned experimental data, it has been confirmed that the intrabuccally rapidly disintegrating tablet as mentioned in the present invention has enough practical hardness and can be rapidly dissolved in the buccal cavity.

INDUSTRIAL APPLICABILITY

According to the present invention, a tablet which can be rapidly disintegrated in oral cavity can be obtained.

Claims

1. A method of producing an intrabuccally rapidly disintegrating tablet, said intrabuccally rapidly disintegrating tablet comprising: a sugar alcohol or saccharide in the form of primary particles having an average particle size of not more than 30 μm;an active ingredient; andone or more disintegrants selected from the group consisting of crospovidone, croscarmellose sodium, low substituted hydroxypropylcellulose, and a mixture thereof, andsaid method comprising the steps of:(a) granulating a powder material comprising the sugar alcohol or saccharide and said active ingredient, thereby producing granulated material having a predetermined size;(b) mixing said granulated material and said one or more disintegrants; and(c) compressing the mixture into an intrabuccally rapidly disintegrating tablet.

2. The method of claim 1, wherein the tablet disintegrates within 30 seconds, determined by measuring the time required for the tablet to fall through no. 10 wire mesh when water is added dropwise to the tablet at a rate of 4 mL/min.

3. The method of claim 1, wherein the amount of active ingredient ranges from 0.01-30% by weight of the intrabuccally rapidly dispersing tablet.

4. The method of claim 1, wherein the sugar alcohol or saccharide is pulverized in advance to an average particle size of not more than 30 μm.

5. The method of claim 1, wherein the sugar alcohol or saccharide is selected from the group consisting of mannitol, lactose, and mixtures thereof.

6. The method of claim 1, wherein said method further comprises mixing the granulated material with a lubricant before said compressing step.

7. The method of claim 1, further comprising spraying a lubricant on material contacting surfaces of punches and dies of a tabletting machine before said compressing step.

8. The method of claim 6, wherein said granulating step comprises granulating a sugar alcohol or saccharide, said active ingredient, and said one or more disintegrants to produce a granulated material.

9. The method of claim 7, wherein said granulating step comprises granulating a sugar alcohol or saccharide, said active ingredient, and said one or more disintegrants to produce a granulated material.

10. The method of claim 6, wherein said intrabuccally rapidly disintegrating tablet comprises about 60-95% by weight of said sugar alcohol or saccharide and about 1-10% by weight of said disintegrant.

11. The method of claim 7, wherein said intrabuccally rapidly disintegrating tablet comprises about 60-95% by weight of said sugar alcohol or saccharide and about 1-10% by weight of said disintegrant.

12. The method of claim 1, wherein said method comprises: (a-1) granulating a wet formulation comprising said sugar alcohol or saccharide, said active ingredient, thereby producing granulated material having a predetermined size;(a-2) drying the granulated material;(b) mixing the dried granulated material and said one or more disintegrants; and(c) compressing the mixture into an intrabuccally rapidly disintegrating tablet.

13. An intrabuccally rapidly disintegrating tablet, made by the process of claim 1.

14. An intrabuccally rapidly disintegrating tablet, made by the process of claim 6.

15. An intrabuccally rapidly disintegrating tablet, made by the process of claim 7.

16. An intrabuccally rapidly disintegrating tablet, made by the process of claim 12.