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Title: Method of producing a solid dispersion of a poorly
water soluble drug
United States Patent: 5,985,326
Inventors: Butler; James Matthew (Romford, GB)
Assignee: ICOS Corporation (Bothell, WA)
Appl. No.: 952938
Filed: February 6, 1998
Abstract
Solid dispersions of poorly soluble drugs, such as
(6R,12aR)-2,3,6,7,12,12a-hexahydro-2-methyl-6-(3,4-methylenedioxyphenyl)-p
yrazino[2',1':6,1]pyrido[3,4-b]indole-1,4-dione and
(+)-N-[1-(adamantanmethyl)-2,4-dioxo-5-phenyl-2,3,4,5-tetrahydro-1H-1,5-be
nzodiazepin-3-yl]-N'-phenylurea, methods of preparing the solid
dispersions, and use of the solid dispersions in pharmaceutical
compositions are disclosed.
SUMMARY DESCRIPTION OF THE INVENTION
The present invention relates to the field of solid dispersions of
poorly water soluble drugs, to processes for their preparation and their
use in pharmaceutical compositions. More particularly the present
invention relates to solid dispersions in the form of co-precipitates of
poorly water soluble drugs and their compositions with a pharmaceutically
acceptable carrier or excipient therefor. Specifically, the invention
relates to co-precipitates of (a) a potent and selective inhibitor of
cyclic guanosine 3',5'-monophosphate specific phosphodiesterase (cGMP
specific PDE) and (b) a potent and selective gastrin and CCK B antagonist,
processes for the preparation of such solid dispersions, pharmaceutical
compositions containing the same and their use thereof in therapy.
Co-precipitation is a recognised technique for increasing the dissolution
of poorly water soluble drugs, such as griseofulvin, ketoprofen,
sulphathiazide, spirinolactone, tolbutamide and nifedipine, so as to
consequently improve bioavailability thereof. Techniques such as solvent
deposition, lyophilization, solvate formation and solid dispersion (of
which co-precipitation is an example as described above) have therefore
been developed to try to overcome the problem of poor water solubility and
resultant low bioavailability.
Solid dispersions in the pharmaceutical field are dispersions of one or
more active ingredients, generally poorly water soluble drugs, in an inert
carrier or matrix at solid state, which are prepared by either melting the
two (fusion), or dissolving them in a solvent, or a combination of
approaches, followed by removal of the solvent.
Manufacture of pharmaceutical dispersions by the above referred to melting
or fusion technique, involves fusion of the two components where the drug
and the carrier are allowed to melt at temperatures at or above the
melting point of both the drug and carrier. In the fusion process, the
drug and carrier are first blended and both melted in a suitable mixer.
The molten mixture is then cooled rapidly to provide a congealed mass
which is subsequently milled to produce a powder. The fusion process is
technically simple provided that the drug and carrier are miscible in the
molten state but this is not always the case and furthermore, the process
is limited in that it tends to lead to drug decomposition due to the high
temperatures required to melt the two components.
The solvent-based process uses organic solvents to dissolve and intimately
disperse the drug and carrier molecules. Identification of a common
solvent for both drug and carrier can be problematic, and complete solvent
removal from the product can be a lengthy process. In addition, large
volumes of solvents are generally required which can give rise to
toxicological problems. The drug and carrier are typically dissolved in a
solvent such as methylene chloride, acetone, ethanol and mixtures thereof
and the solvent is later removed by precipitation techniques, evaporation
or the like, while the drug/carrier solid dispersion is collected as a
powdered mass.
In the case where there is difficulty with thermal instability and
immiscibility between the drug and the carrier, the hybrid fusion-solvent
method can be employed. The drug is first dissolved in a small quantity of
organic solvent and added to the molten carrier. The solvent is then
evaporated to generate a product that is subsequently milled to produce a
powder. The pharmacokinetics, dissolution rates and processes for
formulation of many different solid pharmaceutical dispersions is
discussed at length in an article by Ford J., in Pharm. Acta. Helv. 61, 3;
69-88 (1986).
Co-precipitation techniques employ the use of an organic solvent or
solvents to dissolve and intimately disperse the drug and carrier
molecules as hereinbefore described. Separation of the drug and carrier
from the solvent on precipitation can rely on the solubility properties of
either the drug or carrier. For example, Simonelli et al, Journal of
Pharmaceutical Sciences, Vol. 58, No. 5, May 1969, describes a
co-precipitation process wherein sulfathiazole is dissolved in sodium
hydroxide, followed by addition of polyvinylpyrrolidone; hydrochloric acid
is then added to effect co-precipitation. This process is based on
co-precipitation employing the solubility of the drug at different pH
values. Such reliance on the solubility of the drug may be problematic in
that it is not generally applicable to poorly water soluble drugs, as many
such drugs do not exhibit a pH dependent solubility. Florence et al,
Communications, J. Pharm. Pharmac., 1976, 28 601, describes
co-precipitation of trifluoperazine embonate and the polymers poly DL-aspartic
acid and polymethylmethacrylate. The co-precipitates were prepared by
dissolving the drug and polymer in dimethylformamide and adding the
solution to a rapidly stirred volume of water. Both polymers and drug are
insoluble in water.
In general terms, problems which can be associated with known
co-precipitation techniques can include excess solvent usage, identifying
carrierldrug combinations which can be effectively precipitated and
enhance bioavailability, the use of heat to effect solution which may
detrimentally affect the drug, and the like. Co-precipitation techniques
are however attractive for the preparation of solid dispersions, in that
less solvents and heat are employed when compared to techniques such as
co-evaporation and solvent removal may therefore be facilitated.
We have now developed a co-precipitation technique which alleviates the
above described disadvantages associated with known techniques, and have
also found that co-precipitation offers an advantageous preparation route
for solid dispersions of poorly water soluble drugs.
There is therefore provided in a first aspect of the present invention a
process of preparing a solid dispersion comprising a poorly water soluble
drug or salts or solvates (e.g. hydrates) thereof, and a pharmaceutically
acceptable carrier or excipient therefor, which process comprises:
(i) providing an intimate mixture comprising the carrier or excipient and
a non-aqueous, water miscible solvent or combination of solvents, and
optionally, water;
(ii) co-mixing the intimate mixture obtained in step (a) with a poorly
water soluble drug; and
(iii) co-precipitating the poorly water soluble drug and the carrier or
excipient.
As used herein, the term "intimate mixture" can denote a
solution, suspension, emulsion, colloid, dispersion or the like.
Generally, the term "intimate mixture" as used herein denotes a
solution.
It has been found surprisingly that small amounts of water in the intimate
mixture can aid dissolution of the subsequently added poorly water soluble
drug. For example, a 10% ratio of water in a solvent may aid dissolution
of the poorly water soluble drug.
In a further aspect, the invention describes a process of preparing a
solid dispersion comprising a particular cGMP specific PDE (PDEV)
inhibitor. More particularly, co-precipitation overcomes problems
associated with other preparatory processes for formulating the subject
PDEV inhibitor.
There is therefore provided by the present invention a process of
preparing a solid dispersion comprising
(6R,12aR)-2,3,6,7,12,12a-Hexahydro-2methyl-6-(3,4-methylenedioxyphenyl)-py
razino[2',1':6,1]pyrido[3,4-b]indole-1,4-dione (hereinafter referred to as
Compound A) or salts or solvates (e.g. hydrates) thereof, and a
pharmaceutically acceptable carrier or excipient therefor, which process
comprises co-precipitating Compound A and the pharmaceutically acceptable
carrier or excipient.
In a yet further aspect, the invention describes a process of preparing a
solid dispersion comprising a particular gastrin and CCK-B antagonist.
More particularly, co-precipitation overcomes problems associated with
other preparatory processes for formulating the subject gastrin and CCK-B
antagonist.
There is therefore provided by the present invention a process of
preparing a solid dispersion comprising
(+)-N-[1-(Adamantanmethyl)-2,4dioxo-5-phenyl-2,3,4,5-tetrahydro-1H-1,5benz
odiazepin-3-yl]-N'-phenylurea (hereinafter referred to as Compound B) or
salts or solvates (e.g. hydrates) thereof, and a pharmaceutically
acceptable carrier or excipient therefor, which process comprises
co-precipitating Compound B and the pharmaceutically acceptable carrier or
excipient. The synthesis and use of Compound B has been previously
described in WO93.14074.
Suitably the co-precipitation of Compound A or B comprises the steps of:
(a) providing an intimate mixture of a poorly water soluble drug selected
from Compound A or Compound B, the carrier or excipient therefor and a
non-aqueous, water miscible solvent or combination of solvents, and
optionally, water; and
(b) co-precipitating the compound and the carrier or excipient.
It is generally advantageous in step (a) to first co-mix the carrier or
excipient together with the solvent or solvents and optional water,
thereby providing an initial intimate mixture, prior to addition of the
poorly water soluble drug thereto. Subsequently, the drug can be added to
the initial intimate mixture. Optionally, the carrier or excipient and
solvent initial intimate mixture can be subjected to heating sufficient to
facilitate dissolving of the former in the latter. Such a sequence of
steps (also substantially as hereinbefore described according to the first
aspect of the present invention) can be beneficial in allowing the employ
of heat to effect dissolving, whilst obviating any detrimental affect by
the heat on the drug.
A co-precipitation step, substantially as described in step (iii), or
substantially as described in step (b), can aptly comprise adding the
drug, carrier or excipient and solvent to a co-precipitation medium in
which the carrier or excipient is insoluble. The resultant co-precipitate
can be separated from the remaining components, suitably by filtering or
the like, and the co-precipitate washed to remove residual solvent, and
dried. The co-precipitate can then be formulated in a suitable
pharmaceutical form employing known formulatory techniques, substantially
as hereinafter described.
The carrier or excipient for the drug, and the co-precipitation medium,
are respectively chosen so that the carrier or excipient is substantially
insoluble in the co-precipitation medium. It is also advantageous that the
carrier or excipient has selected dissolution properties in vivo; for
example, the carrier or excipient may be such so as to dissolve rapidly
(within about 15 to 60 minutes) in vivo, alternatively the carrier or
excipient may be such so as to dissolve over a relatively prolonged period
of time (typically, 2 to 4 hours) so as to achieve sustained release of
drug in vivo.
Suitable carrier or excipients include pharmaceutically acceptable
polymeric materials, typical examples being hydroxypropyl methyl cellulose
phthalate, polymethylacrylate, hydroxypropyl cellulose and other like
carrier or excipient materials. Particularly preferred is hydroxypropyl
methyl cellulose phthalate as a carrier or excipient, and there is further
provided by the present invention co-precipitates consisting of Compound A
and hydroxypropyl methyl cellulose phthalate, and Compound B and
hydroxypropyl methyl cellulose phthalate.
Aptly the co-precipitation medium comprises an aqueous medium, which is
optimally such that the carrier or excipient is substantially insoluble
therein as substantially hereinbefore described.
Conveniently the following combinations of carrier or excipient and
co-precipitation medium can be employed in a process according to the
present invention:
(a) in the case where the carrier or excipient is hydroxypropyl methyl
cellulose phthalate, the co-precipitation medium is suitably a weakly
acidic medium (pH in the range of 0.5 to 5.0, typically 0.8 to 2.0),
typically 0.5N hydrochloric acid or acetic acid;
(b) in the case where the carrier or excipient is an acid soluble
polymethylacrylate, the co-precipitation medium is suitably a neutral or
basic medium, (pH in the range 6.0 to 13.0), water or dilute alkali being
appropriate representatives of suitable co-precipitation media; and
(c) in the case where the carrier or excipient is hydroxypropylcellulose,
an appropriate co-precipitation medium is again water, aptly with a
temperature of greater than about 40oC., such as 70 to 80oC.
It is of course envisaged that other suitable combinations of carrier or
excipient and co-recipitation media may be employed, as will be envisaged
by a person skilled in the art. A particularly appropriate combination of
carrier or excipient and co-precipitation medium, is hydroxypropyl methyl
cellulose phthalate and a dilute acidic medium, substantially as
hereinbefore described in point (a) above.
Appropriately, the solvent employed in a process according to the present
invention is selected from the group consisting of acetone, methanol,
dimethylacetamide, dimethylsulphoxide, dimethylformamide, tetrahydrofuran,
and combinations thereof, and optionaly, water, although other suitable
solvents could be employed. Generally 9:1 acetone/water, 9:1
tetrahydrofuran/water, or 1:1 acetone/methanol mixtures are employed in a
process according to the present invention.
There is still further provided by the present invention a solid
dispersion consisting essentially of Compound A or Compound B and a
pharmaceutically acceptable carrier or excipient therefor.
Claim 1 of 28 Claims
1. A process of preparing a solid dispersion comprising a
poorly water soluble drug or salts or solvates thereof, and a
pharmaceutically acceptable carrier or excipient therefor, which process
comprises:
(a) providing an intimate mixture comprising: (i) the carrier or excipient
and (ii) a neutral, nonaqueous, water miscible solvent or combination of
solvents, and optionally, water;
(a) co-mixing the intimate mixture obtained in step (a) with a poorly
water soluble drug to form a mixture; and
(c) co-precipitating the poorly water soluble drug and the carrier or
excipient by admixing the mixture of step (b) and water having a pH of 0.5
to 13.
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