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Title: Rapidly dissolving
dosage form and process for making same
United States Patent: 7,182,959
Issued: February 27, 2007
Inventors: Martani; Rosa (Divonne-les-Bains,
FR)
Assignee: Novartis AG (Nyon,
CH)
Appl. No.:
10/075,429
Filed: February 13, 2002
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Training Courses -- Pharm/Biotech/etc.
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Abstract
The invention relates to a solid dosage
form which is rapidly disintegrating in aqueous medium. Especially, the
invention relates to pharmaceutical, orally ingested solid dosage forms,
which are designed to disintegrate rapidly within the mouth, and to
analogous veterinary dosage forms. Moreover, the invention relates to a
unique process for the manufacture of said solid dosage forms.
Description of the Invention
The present invention relates to the
field of solid, rapidly dissolving dosage forms. Wherever a solid dosage
form comprising any kind of active ingredient and bound to dissolve
rapidly in an aqueous medium is needed, the unique dosage forms provided
by the present invention may be applied.
In the first instance, the invention relates to pharmaceutical, orally
ingested solid dosage forms, which are designed to dissolve rapidly within
the mouth. Another preferred field of applying the invention is solid,
rapidly dissolving dosage forms which are administered orally to animals,
especially mammals like e.g. dogs, cats, horses or cattle, e.g. veterinary
dosage forms.
In the pharmaceutical field, there is a great need for said dosage forms
because many people are unwilling and/or unable to swallow tablets,
capsules and other traditional solid dosage forms. The present invention
provides a solid pharmaceutical dosage form adapted for direct oral
administration, i.e. for direct insertion into the mouth of a patient.
This is particularly useful in administration of medicaments to e.g.
children, debilitated patients, patients who have difficulty swallowing
solids and the elderly.
Currently the main technologies to obtain such type of dosage forms are:
(1) The active ingredient is mixed with water-soluble diluents and
compressed on a tableting machine at low to medium compression force. (2)
A suspension is prepared from the active ingredient and appropriate
excipients, which suspension is then dispensed into blister packs and
finally dried, for example freeze-dried (e.g. Zydis.RTM.).
All these technologies have their drawbacks: For example in the case of
(1), the mechanical resistance of the dosage forms is often insufficient
in normal blister packs and the dosage forms often do not disintegrate
rapidly enough (time needed for dissolution may be up to 60 seconds and
more). In the case of (2), again lacking mechanical resistance in normal
blister packs can be a problem but in particular the time-consuming and
costly freeze-drying process is a major disadvantage. Moreover, the
effectiveness of a freeze-drying process always depends on the physico-chemical
parameters of the active substances used. For certain active substances,
especially such having a high solubility in water, it is therefore
difficult or impossible to apply a freeze-drying process and consequently
this technology. Finally, the development of units with high doses (up to
500 mg or even 1000 mg) of active ingredients and/or combinations of
active ingredients may be difficult or even impossible with this
technology.
The present invention addresses the needs mentioned above and the problems
encountered with currently available technologies. The expensive
freeze-drying process is avoided. The manufacture of the dosage form of
the invention is simple and suitable for a broad range of active
ingredients with different physico-chemical parameters, for high dose unit
forms (up to e.g. 1000 mg, in particular 500 mg, of active substance) and
also for combinations of active ingredients, including combinations of a
water-soluble with a water-insoluble active substance. Moreover, it
overcomes the main problems of drying suspensions which are filled in
blister packs, by (a) assuring that the dosage forms always have a uniform
content of the active ingredient(s); (b) assuring that the dosage forms
always have a uniform tablet weight (e.g. dose weights accurate within 2
3%); (c) avoiding a time-consuming process for removing high quantities of
solvent; (d) allowing easy upscaling of the process developed in the
laboratory; and (e) avoiding moisture uptake during storage.
The basis for the new beneficial solid dosage forms is a newly developed
advantageous process of manufacturing them.
The invention therefore relates--in a first embodiment--to a process for
the manufacture of a solid dosage form which is rapidly dissolving in
aqueous medium, which process comprises (a) preparing a powder or
granulate consisting of (1) either the active substance--or part
thereof--and all other ingredients of the solid dosage form; or (2) all
other ingredients of the solid dosage form except the active substance;
(b) dispensing (1) either an auxiliary solvent or (2) a solution or
dispersion (preferably a solution) of the active substance in an auxiliary
solvent, in moulds or in the cavities of the pre-formed container intended
for storage of the solid dosage form; (c) compacting a suitable amount of
the powder or granulate prepared according to (a)(1) or (a)(2) above; (d)
putting the compacted powder or granulate so obtained on the top of the
liquid which according to (b)(1) or (b)(2) is in moulds or in the cavities
of the pre-formed container intended for storage of the solid dosage form;
(e) removing the auxiliary solvent by applying a drying system to the
units in the moulds or in the cavities of the pre-formed container
intended for storage of the solid dosage form; and (f) removing the dried
units from the moulds into a suitable storage container or sealing the
cavities of the pre-formed container intended for storage of the solid
dosage form, respectively.
It will be understood that the order in which certain steps of this
process are carried out is not fixed but interchangeable. For example, (b)
may be carried out before (a), or (c) before (b). All these variations are
intended to be covered by the present invention.
A preferred embodiment of the invention is characterized by the process
for the manufacture of a solid, rapidly dissolving pharmaceutical or
veterinary dosage form for oral administration, which process comprises
(a) preparing a powder or granulate consisting of (1) either the intended
dose of the active substance--or part thereof--and all other ingredients
of the solid dosage form; or (2) all other ingredients of the solid dosage
form except the active substance; (a') transferring said powder or
granulate to a combined compacting/dosing system; (a'') placing moulds or
a pre-formed container intended for storage of the solid pharmaceutical or
veterinary dosage form within the operating range of the combined
compacting/dosing system; (b) dispensing, (1) either an auxiliary solvent
or (2) a solution or dispersion (preferably a solution) of the active
substance in an auxiliary solvent, in moulds or in the cavities of the
pre-formed container intended for storage of the solid pharmaceutical or
veterinary dosage form; (c) compacting--within the combined
compacting/dosing system--a suitable amount of the powder or granulate
prepared according to (a)(1) or (a)(2) above; (d) putting the compacted
powder or granulate on the top of the liquid which according to (b)(1) or
(b)(2) is in moulds or in the cavities of the pre-formed container
intended for storage of the solid pharmaceutical or veterinary dosage
form; (e) removing the auxiliary solvent by applying a drying system
comprising one or more techniques selected from forced warm gas, microwave
radiation and reduced pressure, to the units in the moulds or in the
cavities of the pre-formed container intended for storage of the solid
dosage form; and (f) removing the dried units from the moulds into a
suitable storage container or sealing the cavities of the pre-formed
container intended for storage of the solid pharmaceutical or veterinary
dosage form, respectively.
In particular preferred is the process for the manufacture of a solid,
rapidly dissolving pharmaceutical dosage form for oral administration,
which process comprises (a) preparing a powder or granulate consisting of
the active substance and all other ingredients of the solid dosage form;
(a') transferring said powder or granulate to a combined compacting/dosing
system; (a'') placing a pre-formed container intended for storage of the
solid pharmaceutical dosage form within the operating range of the
combined compacting/dosing system; (b) dispensing an auxiliary solvent in
the cavities of the pre-formed container intended for storage of the solid
pharmaceutical dosage form; (c) compacting--within the combined
compacting/dosing system--an amount of the powder or granulate prepared
according to (a) above, which amount of powder or granulate contains the
intended dose of the active substance; (d) putting the compacted powder or
granulate on the top of the liquid which according to (b) is in the
cavities of the pre-formed container intended for storage of the solid
pharmaceutical dosage form; (e) removing the auxiliary solvent by applying
a drying system comprising at least two different techniques selected from
forced warm gas, microwave radiation and reduced pressure; and (f) sealing
the cavities of the pre-formed container intended for storage of the solid
pharmaceutical dosage form.
The active substance is typically used as the pure substance--which may be
present e.g. in a certain crystalline form or in amorphous form--but it
may also be e.g. microencapsulated, e.g. for the purpose of taste-masking,
as a sustained release microencapsulation or a gastro-resistant
microencapsulation (enteric coating); or in the form of a complex, e.g. a
cyclodextrine complex or an ion exchange resin complex. It may be
water-soluble or water-insoluble. Moreover, the active substance can e.g.
be dissolved in an auxiliary solvent-wholly or only part thereof [see
process variant (b)(2)]. Still another possibility is, for example, that
the active substance together with some of the excipients is dissolved in
an auxiliary solvent.
What the "other ingredients" of the solid dosage form is concerned
[process step (a)], these are not critical and may vary within wide
limits. The kind of ingredients used inter alia depends on the field where
the solid dosage form is intended for, e.g. pharmaceuticals, veterinary
products or other areas of application.
Preferably, the solid dosage form manufactured comprises (1) an active
substance, (2) a filler and (3) a disintegration agent. Other usual
excipients (4), like e.g. sweeteners, lubricants, flavours, taste-masking
agents, binders, buffering agents, colouring agents, stabilisators or
preservatives, may optionally be present.
The auxiliary solvent applied in step (b) is e.g. water, preferably
purified water, or a non-aqueous solvent, e.g. ethanol, acetone or
isopropanol, or any mixture of water with one or more of the non-aqueous
solvents. Preferred are water, water/ethanol mixtures and ethanol;
especially water and water/ethanol mixtures; and in particular water
alone.
In step (b), the auxiliary solvent is dispensed in moulds or in the
cavities of the pre-formed container by any means known in the art to be
suitable for that purpose, e.g. a metered dose pump or a multi-pipette
system.
In a preferred embodiment of the invention, the process steps (c) and (d)
are accomplished with the aid of a combined compacting/dosing system.
In case that a combined compacting/dosing system is used, it must be able
to serve the following functions: (a) dose a precise quantity of powder or
granulate; (b) compact the dosed powder or dosed granulate; and (c)
release the dosed compacted pellet.
In a preferred embodiment of the invention, the combined compacting/dosing
system consists e.g. of a powder feed frame and an assembly of dosers
capable of delivering a charge of the compacted drug powder in the desired
dosage. The movements of the doser assembly and the feed frame can be
driven e.g. pneumatically or electrically. The product powder or granules
are prepared for dosing e.g. by a rotating paddle feed frame capable of
regulating the depth of the powder bed. In a preferred embodiment of the
invention, the doser assembly descends into the powder bed, takes and
compacts the powder charges.
Then the doser assembly raises the dosed compacted drug powder from the
powder bed and releases the dosed compacted powder charge intact into the
moulds or the cavities of the preformed container, e.g. a blister pack.
After depositing the compacted powder into e.g. the blister cavities, the
filled blister card is removed mechanically and replaced with an empty
blister card so that the process may be repeated.
The system can also be adjusted so as to deliver a double-layer compacted
powder into the cavities of the blister, where the first layer is intended
for an immediate release (it disintegrates immediately in the mouth), and
the second layer is for a sustained release (it softens in contact with
saliva). In that case, the doser assembly may e.g. descend into a first
powder bed, take up powder intended for the first layer, descend into a
second powder bed, take up powder intended for the second layer, and
finally compact the powder charges.
In a preferred embodiment, blisters (having several cavities) are filled
by a doser/compaction assembly [process steps (c) and (d)]. In this case,
the compaction system is e.g. composed of an assembly of dosers set up on
a driven plate. Said doser/compaction assembly takes and compacts the
powder in a powder feed vat. The thickness and density of the powder bed
are ensured by a successive and automatic passage of a powder decompacting
grid and leveling blade. Once the powder has been taken, the feed vat is
replaced by the blister. Each cavity of the blister is placed under the
doser/compaction assembly filled with compacted powder. A pellet of
compacted powder is then deposited in each cavity of the blister, and the
process starts again.
Removal of the auxiliary solvent [step (e)] is accomplished by applying a
drying system which comprises one or more of the known drying techniques,
e.g. warm forced gas, microwave or reduced pressure (vacuum). Preferably,
at least two different techniques selected from forced warm gas, microwave
radiation and reduced pressure are applied. Especially preferred are the
combinations of forced warm gas together with microwave radiation and
microwave radiation together with reduced pressure, in particular forced
warm gas together with microwave radiation. Said combined techniques may
be applied simultaneously or alternating (interchangeably), preferably
simultaneously.
In a preferred embodiment of the invention, the auxiliary solvent is
removed without applying any freeze-drying process in step (e).
The drying system may be static or dynamic. It may operate continuously or
discontinuously during the drying process. Forced warm gas (e.g. air,
nitrogen or carbon dioxide) has e.g. a temperature of from 30 up to
80.degree. C. Forced warm gas is preferably forced warm nitrogen or forced
warm air. Advantageously, it is heated before entering the drying system.
It can be blown e.g. vertically or horizontally across the product. In
case that the auxiliary solvent used comprises a solvent that may give
rise to explosions when combined with oxygen and microwave radiation, e.g.
ethanol, it is preferable to use non-oxygen-containing forced warm gas,
e.g. nitrogen or carbon dioxide. But forced warm air may nevertheless be
used, if the risk of explosion is avoided by other precautionary measures
in the drying system. The risk of explosion can also be avoided in that
case, if a drying system is used wherein microwave radiation is combined
with reduced pressure (vacuum).
The microwave can be e.g. a mono-mode or multi-mode structure. When
microwave radiation is applied, this is preferably done in a system that
is able to work on-line (continuously) during the manufacturing process.
Typically the wavelength of the microwave radiation is chosen so as to
excite the solvent molecules, especially water, and expedite their
evaporation. Advantageously, the microwave radiation is combined with
forced warm gas which is capable of removing the humidity (gaseous water)
generated.
"Reduced pressure" typically means pressures of from 0.1 mbar up to 500
mbar, and especially of from 20 to 200 mbar. The evaporation is typically
performed at a temperature of from 20 up to 80.degree. C., and preferably
at 30 60.degree. C. Said elevated temperatures are obtained e.g. by
applying forced warm gas and/or microwave radiation.
In process step (f), it is preferred that the cavities of the pre-formed
container intended for storage of the solid dosage form are sealed, e.g.
with a lid. Pre-formed containers intended for storage of the solid dosage
form are in particular blisters. Blisters are well-known in the art; they
may be produced and formed from materials like e.g. polyvinyl chloride
(PVC), PVC/polyvinylidene chloride (PVDC), PVC/Polyethylene (PE)/PVDC,
PVC/PE/PVDC/PE/PVC, oriented polyamide (oPA)/Aluminium (Alu)/oPA or PVC/oPA/Alu/PVC.
In one special embodiment of the invention blisters are sealed with a
lidding foil to obtain a peel off blister. Peel off (lidding) foils are
composed of e.g. Paper/PETP(Polyethylene terephthalate)/Alu or Paper/PETP/Alu)
or PETP/Alu.
From the description of the unique process of manufacture above it has
become clear that the solid dosage form of the present invention is
manufactured without applying any compression force to the mixture of its
components (1), (2), (3) and optionally (4) during the last step of
manufacture concerning the solid dosage form, i.e. process step (e). As a
result of the particular process of manufacture used, the dosage form of
the invention normally has a density of 300 1000 mg/ml, preferably of 400
900 mg/ml, and more preferably of 500 800 mg/ml, and especially of 500 700
mg/ml. This is a density that is much lower than that of compressed dosage
forms like normal tablets etc. (having densities of above 1100 mg/ml). As
a result of its unusually low density, the dosage form of the invention
disintegrates more rapidly than would be the case, if the mixture of its
components (1), (2), (3) and optionally (4) were subjected to compression
force during the last step of manufacture concerning the solid dosage
form, i.e. process step (e). When taken into the mouth, it typically
disintegrates within 30 seconds, preferably within 20 seconds, more
preferably within 10 seconds and most preferably within 8 seconds.
The invention therefore further relates to a solid dosage form which is
rapidly dissolving in aqueous medium, which dosage form comprises (1) an
active substance, (2) a filler, and (3) a disintegration agent, which
dosage form disintegrates when taken into the mouth within 30 seconds, and
which dosage form has a density of 300 1000 mg/ml.
Preferred are solid pharmaceutical or veterinary solid dosage forms for
oral administration consisting essentially of a homogeneous mixture of (1)
at least one pharmaceutically or veterinary active substance, (2) at least
one filler, (3) at least one disintegration agent, and (4) optionally
other usual excipients, which dosage form disintegrates when taken into
the mouth within 30 seconds, and which dosage form has a density of 400
900 mg/ml.
In a preferred embodiment of the invention, the solid dosage forms
mentioned herein before do contain at least one other usual excipient.
Further preferred are those solid pharmaceutical or veterinary dosage
forms of the invention, wherein the composition contains as other usual
excipients (4) a lubricant and optionally other usual excipients.
Especially preferred are those solid pharmaceutical or veterinary dosage
forms of the invention, wherein the composition contains as other usual
excipients (4) a lubricant, one or more sweeteners and optionally other
usual excipients.
More precisely, the solid pharmaceutical or veterinary dosage form
consists essentially of a mixture, especially a homogeneous mixture, of
the components (1), (2), (3) and optionally (4) mentioned above.
The term "pharmaceutically active substance" is intended to be understood
broadly so as to include not only pharmaceuticals but also e.g. vitamins,
minerals, dietary supplements, nutritional supplements or infant formula
products. Pharmaceuticals may include, without limitation, antacids, e.g.
calcium or magnesium carbonate; analgesics, anti-inflammatories,
antibiotics, laxatives, antidiarrheals, e.g. loperamide, anthelminthics;
antifungals, e.g. terbinafine or a pharmaceutically acceptable salt
thereof; emetics, antiemetics, anorexics, stimulants, antihaemorrhoids,
antiasthmatics, antidiuretics, antiflatulents, antimigraine agents,
antispasmodics, sedatives, antihyperactives, tranquilizers;
antihistamines, e.g. loratidine; decongestants, e.g. pseudoephedrine or a
pharmaceutically acceptable salt thereof; betablockers, hormones,
weight-control substances and combinations thereof. Preferred active
substances are analgesics and non-steroidal anti-inflammatory drugs, such
as diclofenac, ketoprofen, ibuprofen, aspirin or paracetamol and
pharmaceutically acceptable salts thereof, as well as hormones, e.g.
melatonin. Minerals are e.g. pharmaceutically acceptable salts of calcium,
magnesium or zinc, e.g. calcium carbonate, magenesium carbonate, magnesium
L-aspartate or zinc gluconate.
Especially preferred is diclofenac which may be present either as free
acid or as a pharmaceutically acceptable salt thereof, e.g. the potassium
or sodium salt, and also diclofenac tromethamine salt or the diclofenac
hydroxyethylpyrrolidinium salt, and also e.g. diclofenac complexes, e.g.
diclofenac cyclodextrin complexes. In particular preferred is diclofenac
potassium.
Another field of application of the solid dosage form according to the
invention is the veterinary field, which concerns e.g. the protection of
domestic animals or productive livestock against parasites that live in or
on the animals, and the treatment of sick animals that are in need of a
certain active substance.
The filler used can be any of those known in the art, e.g. mannitol,
lactose, calcium phosphates, dibasic calcium phosphates, cellulose
microcrystalline, cyclodextrine, starch, laevulose, maltitol, polydextrose,
sucrose, glucose, inulin, sorbitol or xylitol. Preferred fillers are
mannitol, lactose, sucrose, glucose, sorbitol, laevulose, microcrystalline
cellulose and starch, and especially preferred are mannitol, lactose,
starch and microcrystalline cellulose. It has been found that a
particularly advantageous filler is mannitol, because it is particularly
useful in forming the low density matrix of the dosage form that
disintegrates rapidly within the mouth. Furthermore, mannitol is
favourable in the drying process of the formulation [see step (e) of
process hereinabove] because of its non-hygroscopic character. The filler
is typically present in an amount of at least 30, preferably at least 50,
more preferably at least 60, and especially at least 70 weight-% of the
total dosage form.
The disintegration agent can be any of those known in the art, e.g.,
croscarmellose Na; sodium glycolates of starch, e.g., Explotab.RTM. and
Primojel.RTM.; cross-linked poly-N-vinyl-2-pyrrolidones, e.g.,
Polyplasdone.RTM. XL and Kollidon.RTM. CL; polymethylmethacrylates, e.g.,
Eudispert.RTM. HV; polysaccharides, e.g., Emcosoy.RTM.; or synthetic
resins, e.g., Amberlite.RTM. IRP88. Preferred disintegration agents are
croscarmellose Na, sodium starch glycolate (e.g., Primojel.RTM.) and
cross-linked poly-N-vinyl-2-pyrrolidones (especially Polyplasdone.RTM.
XL). The disintegration agent is typically present in an amount of at
least 1, preferably of at least 5, and especially of at least 10 weight-%
of the total dosage form, e.g. of from 1 up to 20 weight-%, especially of
from 1 up to 15 weight-%.
Lubricants which can optionally be present in the dosage form are e.g.
talc, magnesium stearate, compritol.RTM. [corresponds to a behenic acid
derivative, especially glyceryl behenate (also called "tribehenin") which
corresponds to a mixture of glycerides (mainly triglycerides) of fatty
acids (mainly behenic acid)]; polyethylene glycol, especially polyethylene
glycol 6000, stearic acid, sodium stearyl fumarate, hydrogenated vegetable
oil, sodium benzoate, L-leucine or silicon dioxide. If used, the lubricant
is typically present in an amount of up to 10 weight-%, preferably up to 5
weight-%, e.g. in an amount of from 0.3 to 10 weight %, and especially in
an amount of from 0.3 up to 5 weight-% of the total dosage form. Preferred
as lubricant is talc.
Sweeteners which can optionally be present in the dosage form are e.g.
sodium saccharin, aspartame, acesulfame K, neohesperidine (dihydrochalcone),
thaumatin, miraculine or ammonium glycyrrhizinate. If used, the sweetener
is typically present in an amount of up to 15 weight-% and especially in
an amount of from 0.5 up to 15 weight-% of the total dosage form.
A combination of sweeteners which is of particular value for taste-masking
of pharmaceutically active substances, especially of bitter active
substances, e.g. diclofenac, terbinafine or pseudoephedrine or any
pharmaceutically acceptable salts thereof, is characterized by the
combination of (1) at least one of neohesperidine, thaumatin and ammonium
glycyrrhizinate, (2) mint flavour and (3) at least one of aspartame and
acesulfame or a pharmaceutically acceptable salt thereof, especially
acesulfame K. Said combination of sweeteners combined with a
pharmaceutically active substance, especially one requiring effective
taste-masking, forms another embodiment of the invention.
Flavours (aromas) or taste-masking agents which can optionally be present
in the dosage form are known in the art. Examples are sodium chloride,
vanillin, citric acid, mint flavour, lemon flavour, orange flavour,
grapefruit flavour, cream flavour, raspberry flavour, strawberry flavour,
anise flavour or cherry flavour.
Binders which can optionally be present in the dosage form are e.g.
polyvinylpyrrolidones, methyl hydroxypropyl cellulose and other cellulose
materials, e.g. sodium carboxymethyl cellulose or hydroxypropyl cellulose,
or gums, e.g. xanthan gum, guar gum, arabic gum, carrageenan, and, in
particular, gellan gum.
If used, the binder is typically present in an amount of up to 10 weight-%
and especially in an amount of from 0.5 up to 10 weight-% of the total
dosage form.
Further excipients optionally present may be, for example, colorants,
buffering agents, acidifying agents or preservatives.
According to the unique process of the invention, it is possible to
provide solid dosage forms for a broad range of active ingredients with
different physico-chemical parameters, for high dose unit forms (e.g. up
to 1000 mg, in particular 500 mg of active substance) and also for
combinations of active ingredients.
In the pharmaceutical (and veterinary) field, the solid dosage form is
presented as a single dose unit, e.g. a tablet, of a size and shape
adapted for direct oral administration to a patient (or a warm-blooded
animal, respectively). The tablet is pleasant to take and, once placed
into the mouth, will disintegrate substantially and instantly without any
voluntary action by the patient, such as e.g. chewing. Upon disintegration
of the tablet, the active ingredient is released and can be swallowed or
is absorbed from the buccal cavity. Buccal absorption can be particularly
advantageous for substances submitted to a high first hepatic metabolism.
Drugs coming into consideration are in particular those with a relatively
low molecular weight and pKa values enabling the presence of non-ionized
drug at buccal pH.
In the pharmaceutical (and veterinary) field, the solid dosage form
according to the present invention is convenient to use for the consumer
(or warm-blooded animal, respectively) without the need of water or
additional devices. Moreover, the instant disintegration and/or
dissolution gives a sensation of a rapid and powerful action of the
pharmaceutical dosage form and makes it unique and motivating for the
patient to take.
Claim 1 of 9 Claims
1. A process for the manufacture of a
solid dosage form which is rapidly dissolves in aqueous medium, wherein
the solid dosage form comprises an active substance and other
pharmaceutical ingredients suitable for a pharmaceutical or veterinary
dosage form for oral administration, which process comprises (a) preparing
a powder or granulate consisting of (1) either the active substance or
part thereof and the other pharmaceutical ingredients of the solid dosage
form, or (2) the other pharmaceutical ingredients of the solid dosage
form; (b) dispensing (1) either an auxiliary solvent, if (a)(1) includes
all of the active substance, or (2) a solution or dispersion of the active
substance in an auxiliary solvent, in cavities of a pre-formed container
intended for storage of the solid dosage form or molds; (c) compacting a
suitable amount of the powder or granulate prepared according to (a)(1) or
(a)(2) above; (d) putting the compacted powder or granulate prepared
according to (c) on the top of the solvent which according to (b)(1) or
(b)(2) is in the molds or in the cavities of the pre-formed container
intended for storage of the solid dosage form; (e) removing the auxiliary
solvent by applying a drying system to the molds or the cavities of the
pre-formed container intended for storage of the solid dosage form after
(d); and (f) removing the dried solid dosage form from the molds into a
suitable storage container or sealing the cavities of the pre-formed
container intended for storage of the solid dosage form, respectively,
wherein the manufactured solid pharmaceutical or veterinary dosage form
for oral administration is in the form of a tablet, and wherein in step
(c) the suitable amount of the powder or granulate which is subjected to
compaction contains an intended dose of the active substance. ____________________________________________
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