U.S. patent application number 11/806206 was filed with the patent office on 2008-10-16 for inhalation particles incorporating a combination of two or more active ingredients.
This patent application is currently assigned to Orion Corporation. Invention is credited to Petri Ahonen, David Brown, Esko Kauppinen, Esa Muttonen, Wiwik Watanabe.
Application Number | 20080254127 11/806206 |
Document ID | / |
Family ID | 8559251 |
Filed Date | 2008-10-16 |
United States Patent
Application |
20080254127 |
Kind Code |
A1 |
Watanabe; Wiwik ; et
al. |
October 16, 2008 |
Inhalation particles incorporating a combination of two or more
active ingredients
Abstract
Crystalline spherical inhalation particles incorporating a
combination of two or more different active ingredients and a
process for the preparation thereof. The particles have a narrow
particle size distribution, rough surfaces and improved stability.
The inhalation particles of the invention are particularly useful
in the administration of a combination medicament, e.g. a
combination of an anti-inflammatory agent and a bronchodilator, by
inhalation in the treatment of asthma and other respiratory
disorders.
Inventors: |
Watanabe; Wiwik; (Sunnyvale,
CA) ; Kauppinen; Esko; (Helsinki, FI) ;
Ahonen; Petri; (Koisjarvi, FI) ; Brown; David;
(Helsinki, FI) ; Muttonen; Esa; (Espoo,
FI) |
Correspondence
Address: |
FINNEGAN, HENDERSON, FARABOW, GARRETT & DUNNER;LLP
901 NEW YORK AVENUE, NW
WASHINGTON
DC
20001-4413
US
|
Assignee: |
Orion Corporation
|
Family ID: |
8559251 |
Appl. No.: |
11/806206 |
Filed: |
May 30, 2007 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
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10398373 |
Aug 14, 2003 |
7267813 |
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PCT/FI01/00863 |
Oct 5, 2001 |
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11806206 |
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Current U.S.
Class: |
424/489 ;
514/171 |
Current CPC
Class: |
A61K 9/0075 20130101;
A61P 11/06 20180101; A61P 31/12 20180101; A61K 31/573 20130101;
A61P 3/10 20180101; A61K 31/165 20130101; Y10S 514/826 20130101;
A61K 2300/00 20130101; A61K 2300/00 20130101; A61K 31/57 20130101;
A61P 11/00 20180101; A61P 25/20 20180101; A61P 11/08 20180101; A61P
5/00 20180101; A61P 3/02 20180101; A61P 43/00 20180101; A61K 31/573
20130101; A61P 25/18 20180101; A61P 37/00 20180101; A61K 45/06
20130101; A61P 9/06 20180101; A61P 11/10 20180101; A61P 35/00
20180101; A61K 31/167 20130101; A61P 31/10 20180101; A61P 29/00
20180101; A61K 31/167 20130101 |
Class at
Publication: |
424/489 ;
514/171 |
International
Class: |
A61K 9/14 20060101
A61K009/14; A61K 31/56 20060101 A61K031/56; A61P 11/00 20060101
A61P011/00 |
Foreign Application Data
Date |
Code |
Application Number |
Oct 6, 2000 |
FI |
20002215 |
Claims
1-21. (canceled)
22. Inhalation particles incorporating, in an unagglomerated
individual particle, a combination of two or more different active
ingredients, wherein said particles are spherical and at least one
of the active ingredients is in crystalline form.
23. Inhalation particles according to claim 22, wherein the mean
mass aerodynamic diameter of said particles is about 1-5 .mu.m.
24. Inhalation particles according to claim 22, wherein the
aerodynamic particle size distribution of said particles is about
0.5-10 .mu.m.
25. Inhalation particles according to claim 22, wherein the ratio
of the active ingredients is constant.
26. Inhalation particles according to claim 22, wherein the
particles have a rough surface.
27. Inhalation particles according to claim 22, wherein the
particles are uncharged.
28. Inhalation particles according to claim 22, incorporating a
combination of beclomethasone dipropionate and formoterol
fumarate.
29. An inhalation composition comprising particles incorporating,
in an unagglomerated individual particle, a combination of two or
more different active ingredients, wherein said particles are
spherical and at least one of the active ingredients is in
crystalline form.
30. An inhalation composition according to claim 29 additionally
comprising one or more pharmaceutically acceptable additives,
diluents or carriers.
31. An inhalation composition according to claim 29 in the form of
dry inhalation powder.
32. An inhalation composition according to claim 29 in the form of
pressurized metered dose inhalation suspension.
33. An inhaler device comprising an inhalation composition
according to claim 29.
34. A method for preparing particles incorporating, in an
unagglomerated individual particle, a combination of two or more
different active ingredients comprising the steps of: providing
liquid feed stock comprising two or more different active
ingredients in a predetermined ratio: atomising said liquid feed
stock to create droplets: suspending said droplets in a carrier
gas; passing said carrier gas and droplets suspended therein
through a heated tube flow reactor under predetermined residence
time and temperature history; and collecting the particles
produced.
35. A method of claim 34 wherein the liquid feed stock, comprising
two or more different active ingredients in a predetermined ratio,
is in the form of a solution.
36. A method according to claim 34, wherein the carrier gas is
selected from nitrogen gas or other inert gas.
37. A method according to claim 34, wherein the particles are
collected using a particle collection system selected from an
electrostatic precipitator, a cyclone or a filter.
38. A method according to claim 37, wherein the particle collection
system is heated to a temperature above the boiling point
temperature of the solution to prevent condensation.
39. A method according to claim 34, wherein the liquid feedstock
comprises beclomethasone dipropionate and formoterol fumarate as
active ingredients.
40. A method according to claim 39, wherein the liquid feed stock
comprises ethanol as a solvent.
41. Inhalation particles according to claim 22, wherein the
aerodynamic particle size distribution of said particles is about
1-5 .mu.m.
Description
FIELD OF THE INVENTION
[0001] The present invention relates to inhalation particles and
inhalation compositions suitable for pulmonary drug delivery and to
methods for the preparation thereof. In particular, the present
invention relates to inhalation particles incorporating a
combination of two or more different active ingredients. The
inhalation particles of the invention are particularly useful in
the treatment of asthma and other respiratory disorders.
BACKGROUND OF THE INVENTION
[0002] Inhalation has become the primary route of administration in
the treatment of asthma. This is because, besides providing direct
access to the lungs, medication delivered through the respiratory
tract provides rapid and predictable onset of action and requires
lower dosages compared to the oral route.
[0003] There have been recent advances in the treatment of asthma
resulting from the recognition that asthma is a chronic
inflammatory disease. Current asthma drugs can be classified into
two classes, namely anti-inflammatory agents and bronchodilators.
Anti-inflammatory drugs, such as glucocorticosteroids do not
relieve asthma symptoms once they occur, rather they are used to
control the inflammation. One of the drawbacks of anti-inflammatory
drugs is that their onset of action is relatively slow. Therefore,
patients often do not recognise any immediate therapeutic effects
and tend to stop the medication. This could cause the inflammation
uncontrollable. On the other hand, bronchodilators, such as
.beta..sub.2-agonists and theophylline, are effective to relieve
acute asthma symptoms. They have a potent bronchodilating activity
and rapid onset of action. The short-acting inhaled
.beta..sub.2-agonists e.g. salbutamol and terbutaline, are
important for an immediate symptomatic asthma relieve, while
long-acting .beta..sub.2-agonists, e.g. salmeterol, formoterol and
procaterol, are important for the treatment of moderate and severe
asthma. However, there are currently debates on the safety of a
regular use of .beta..sub.2-agonists as well as efficiency of
long-acting .beta..sub.2-agonists. Also, the short-acting nature of
the drug requires more frequent drug administrations, which tend to
cause patient compliance problem.
[0004] To overcome these problems, inhalation compositions
comprising a combination of anti-inflammatory and bronchodilator
agents have been proposed as described e.g. in patent publications
EP 0416950, EP 0416951, WO 93/11773 and WO 98/15280. Such
combinations include salmeterol with beclomethasone dipropionate,
salmeterol with fluticasone propionate, and formoterol with
budesonide. These patent publications disclose a method of mixing
mechanically the two drug powders and optionally the carrier
material in a certain proportion and placing the resulting
inhalation powder into an inhaler device. When these combinations
are used in dry powder inhalers, the consistency of drug proportion
in each dose cannot be easily controlled. The ratio of drugs in
each dose significantly depends on the forces existing in each
drug, between the drugs, between the drug and carrier material, and
between the drug and the dry powder container of the inhaler
device. It is well acknowledged that the current powder
manufacturing methods, especially the conventional methods, produce
dry powder that is highly charged and therefore very cohesive.
Hence, it is not easy to keep the ratio of the drugs in each dose
constant. The inconsistency of the dose could cause serious
problems especially when a very potent drug is delivered in a much
higher amount than expected.
[0005] A method for the preparation of inhalation particles by
spray-drying a solution of one or several drugs has been disclosed
in U.S. Pat. No. 4,590,206. However, the method produces amorphous
particles, which have stability problems and a high, tendency
toward moisture re-absorption, which is undesirable for
pharmaceutical particles intended for administration by inhalation.
Furthermore the size and the morphology of the particles obtained
are not optimal for pulmonary delivery.
[0006] The object of the invention is to provide a composition that
is better adapted than products of the prior art, for delivery of a
drug combination into the lungs.
SUMMARY OF THE INVENTION
[0007] It has now been found that, by using an aerosol flow reactor
method, it is possible to prepare uncharged, spherical and
crystalline inhalation particles incorporating, in an individual
particle, a combination of two or more drugs in a predetermined and
constant ratio. The particles provide more controlled delivery of
combination medicaments by inhalation, since it is now possible to
keep the ratio of the drugs in each dose constant. The particles
exhibit improved dispersibility and good stability as a result of
their crystalline nature. The particles have a narrow aerodynamic
particle size distribution, typically between about 1-5 .mu.m,
which is especially suitable for the preparation of compositions
for dry powder inhalers. Moreover, particle surfaces are spherical
and generally rough, which reduces the force required to break-up
the aggregates of the particles or detach the particle from a
coarse carrier. Furthermore, the method of the invention provides a
high purity product since the product purity only depends on the
purity of solution precursors. Moreover, the method is simple and
can be easily scaled-up to higher production rates.
[0008] In one aspect the present invention provides inhalation
particles incorporating a combination of two or more different
active ingredients, wherein said particles are spherical and at
least one of the active ingredients is in crystalline form. The
mean mass aerodynamic diameter of the particles is typically
between about 0.5-10 .mu.m, more typically between about 1-5 .mu.m.
The aerodynamic particle size distribution of said particles is
typically between about 0.5-10 .mu.m, more typically between 1-5
.mu.m.
[0009] In another aspect the present invention provides an
inhalation composition comprising particles incorporating a
combination of two or more different active ingredients, wherein
said particles are spherical and at least one of the active
ingredients is in crystalline form. The particles may be formulated
into an inhalation composition together with one or more
pharmaceutically acceptable additives, diluents or carriers.
Preferably, the composition is provided in the form of dry
inhalation powder.
[0010] In still another aspect, the present invention provides a
method for preparing particles incorporating a combination of two
or more different active ingredients, comprising the steps of:
[0011] providing liquid feed stock comprising two or more different
active ingredients in a predetermined ratio;
[0012] atomising said liquid feed stock to create droplets;
[0013] suspending said droplets in a carrier gas;
[0014] passing said carrier gas and droplets suspended therein
through a heated tube flow reactor under predetermined residence
time and temperature history; and collecting the particles
produced.
[0015] The present invention is particularly useful in the
preparation of combination medicaments, e.g. for the treatment of
asthma and other respiratory disorders. Especially preferred drug
combination is a combination of an anti-inflammatory agent and a
bronchodilator, for example a combination of a glucocorticosteroid
and a .beta..sub.2-agonist.
BRIEF DESCRIPTION OF THE DRAWINGS
[0016] FIGS. 1a, 1b and 1c are schematic diagrams showing parts of
the apparatus used in the method of the invention.
[0017] FIG. 2 is a schematic diagram of the electrostatic
precipitator.
[0018] FIGS. 3a and 3b show the normalised and cumulative mass size
distribution of the drug combination particles of the
invention.
[0019] FIG. 4 shows the XRD pattern of the combination powder of
the invention.
[0020] FIG. 5 shows moisture absorption profile of the combination
powder of the invention when exposed in different humidity
levels.
[0021] FIG. 6 depicts a scanning electron microscopy image of the
combination powder of the invention.
DETAILED DESCRIPTION OF THE INVENTION
[0022] The particles of the invention can be used to deliver
locally or systemically to a patient a variety of drug
combinations. Particularly suitable are drug combinations which are
typically used in the pulmonary delivery by inhalation, such as
combinations used in the treatment of asthma and other respiratory
diseases. These include, but are not limited to, a combination of
an anti-inflammatory agent and a bronchodilator, e.g. a combination
of a glucocorticosteroid and a .beta..sub.2-agonist. Examples of
anti-inflammatory glucocorticosteroids include beclomethasone,
budesonide, fluticasone, mometasone, betamethasone, triamcinolone,
flunisonide and the like and their salts and hydrates. Examples of
.beta..sub.2-agonists include salbutamol, formoterol, fenoterol,
procaterol, salmeterol, clenbuterol and the like and their salts
and hydrates. Typical combinations include beclomethasone
dipropionate and formoterol fumarate, beclomethasone dipropionate
and salbutamol, budesonide and formoterol fumarate, fluticasone
propionate and salmeterol, beclomethasone dipropionate and
salmeterol. Finding suitable ratio of the active ingredients in a
given combination is considered to be a routine for one skilled in
the art.
[0023] Any inhalable pharmaceutically active compound which can be
formulated into a powder is suitable for use in the present
invention. Examples of other inhalable drugs include drugs for the
treatment of respiratory disorders such as anticholinergic
bronchodilators such as ipratropium bromide and the like,
anti-allergic drugs such as nedocromil sodium, expectorants,
mucolytics, antihistamines, cyclooxygenase inhibitors, leukotriene
synthesis inhibitors, leukotriene antagonists, PLA2 inhibitors, PAF
antagonists and prophylactics of asthma and combinations thereof.
Alternatively, the pharmaceutically active agent can be any of
several types of inhalable, systemically active drugs including
antiarrhythmic drugs, tranquilizers, cardiac glycosides, hormones,
antihypertensive drugs, antidiabetic drugs, anticancer drugs,
sedatives, analgesic drugs, antibiotics, antirheumatic drugs,
immunotherapeutics, antifungal drugs, vaccines, antiviral drugs,
proteins, peptides, vitamins and combinations thereof. A
combination of an anti-inflammatory agent and a bronchodilator is
particularly preferred.
[0024] The particles of the present invention are preferably
prepared using an aerosol flow reactor method (aerosol synthesis
method). It is a one-step continuous process, which can directly
produce desirable particle size range. The method has been used to
produce various materials, e.g. ceramic powder (U.S. Pat. No.
5,061,682) or zirconia powder (U.S. Pat. No. 4,999,182), at high
operation temperatures. However, the method has not been used to
produce pharmaceutical materials, which requires a significantly
lower-temperature operation (less than 300.degree. C.).
[0025] The aerosol flow reactor method comprises generally the
following steps; (a) providing liquid feed stock comprising two or
more different active ingredients in a predetermined ratio, (b)
atomising said liquid feed stock to create droplets, (c) suspending
said droplets in a carrier gas, (d) passing said carrier gas and
droplets suspended therein through a heated tube flow reactor under
predetermined residence time and temperature history, and (e)
collecting the particles produced.
[0026] The above method differs significantly from the conventional
spray-drying process. In spray-drying, hot gas is used as a source
of heat to evaporate the solvent. The spray-drying chamber is only
used as a place for the heat transfer to occur, the chamber itself
is not heated. The temperature of the gas is changing across the
chamber as heat transfer occurs between the cold feed and the hot
gas. Furthermore, the evaporation is so rapid that it is not easy
to properly control the temperature history and the residence time
of each droplet and product particle. The crystallization can not
be easily controlled either, and therefore the particles formed are
commonly amorphous.
[0027] In the present method, the droplets are already suspended in
the carrier gas before they are fed into the tubular flow reactor,
which is placed in an oven set at a constant temperature. The
carrier gas flows evenly in the tubular reactor with a constant
rate, uniform temperature field and non-circulating flow.
Therefore, the temperature history and the residence time of each
droplet and product particle can be properly controlled and
excellent uniformity of the particles can be ensured. Accordingly,
the method provides better control of the droplet size
distribution, and thus the particle size distribution such that
particles with optimal aerodynamic particle size distribution
typically between about 1-5 .mu.m can be obtained. Furthermore, in
contrast to spray drying, the method allows essentially complete
crystallization of the particles. Thus, the method is able to
produce consistent and controlled particle properties, including
particle size and size distribution, shape, crystallinity,
polymorphic phase, surface roughness and chemical purity.
[0028] The liquid feed stock of step (a) may be prepared by mixing
each active ingredient with a suitable liquid solution, e.g.
solvent. The two or more liquid feed stocks are then mixed to form
a solution, suspension, dispersion, gel, emulsion, slurry or the
like, and is preferably homogenous to ensure uniform distribution
of the components in the mixture. It is also possible to mix all
active ingredients directly in one liquid feed stock. The liquid
feed stock in the form of a solution is preferred.
[0029] Various solvents may be employed in the preparation of the
liquid feed stock, including but not limited to, water,
hydrocarbons, halogenated hydrocarbons, alcohols, ketones and the
like. Examples of suitable solvents include water, hexane,
perfluorohexane, ethanol, methanol, acetone, chloroform, methylene
chloride and combinations thereof.
[0030] In case the liquid feed stock is a solution, the active
ingredients should be sufficiently soluble in the solvent of the
solution so as to obtain, from the atomized droplets of the liquid
feed stock, uniform particles with the desired particle size, size
distribution and drug ratio. The total solids dissolved may be
present in wide range of concentrations, typically from about 0.1%
to about 10% by weight, for example from about 1% to about 5% by
weight. A liquid feed stock containing relatively low concentration
of solids results in particles having relatively small diameter.
The finding of suitable liquid feed stock concentrations for each
active agents/solvent combinations is considered to be a routine to
one skilled in the art. Usually, the liquid feed stock
concentration is firstly chosen at its maximum solubility so as to
obtain the largest particle size with the atomizer and atomizer
conditions used. From the results, the liquid feed stock
concentration required to obtain the desired particle size range
with the atomizer and the atomizer conditions used can be
approximated.
[0031] The liquid feed stock is atomized to create droplets in a
suitable atomizer, which are well known in the art, such as a spray
nozzle (e.g. a two fluid nozzle), an ultrasonic or air assisted
nebuliser or a spinning disc, an ultrasonic nebulizer being
preferred. Examples of the devices used in this process include
ultrasonic generators sold under trademarks Omron NE-U12 and RBI
Pyrosol 7901. While there are no special restrictions placed on the
atomisers used in the process, it is recommended to use an
atomiser, which can produce uniform droplets of constant
composition and in a specific size range. Such devices are suitable
to produce dry powders of controlled composition and with particle
size range suitable for dry powder inhalation.
[0032] The droplets of the liquid feed stock are suspended in a
carrier gas before passing through a heated tube flow reactor. The
carrier gas must be inert with respect to the drug molecules and
the solvent. It is recommended to use nitrogen gas or other inert
gases. The temperature of the carrier gas is typically ambient. To
maintain a uniform solution concentration in the droplets in the
suspending phase, it is preferred to bubble the carrier gas through
a bottle containing the same solvent as the liquid feed stock
before entering the atomizer.
[0033] Because the droplets are already suspended in the carrier
gas when fed into the reactor (i.e. the droplet generation and flow
reactor are separated), the temperature history and residence time
of each droplet and product particle can be better controlled than
in the conventional spray-drying method. Therefore, excellent
uniformity of the resulted particles and narrow particle size
distribution can be ensured.
[0034] The droplets suspended in the carrier gas are passed through
a tubular flow reactor, which is maintained at a constant
temperature. The temperature and the flow rate of the carrier gas
are adjusted to evaporate the solvent and to allow the
crystallisation process to complete. The particles formed are then
collected using an electrostatic precipitator, a cyclone, a planar
filter (e.g. nylon) or other particle collecting devices.
[0035] The particle size may be controlled to any expected particle
size ranges by selection of the atomizer and concentration of the
liquid feed stock. It is also possible to employ a droplet size
modification apparatus (e.g. impactor or virtual impactor, or using
size selective collection of particles, e.g. a cyclone) upstream
and/or downstream of the flow reactor.
[0036] For the tubular flow reactor, while there are no particular
restrictions, it is recommended to use a vertical, rather than
horizontal configuration in order to minimise buoyancy effects and
related losses due to recirculating flow. A laminar flow is
preferred. To ensure uniform temperature and flow fields in the hot
zone of the reactor, CFD (Computational Fluid Dynamics)
calculations have shown that it is preferable that the aerosol
flows against gravity. Flow in any other direction tends to produce
undesirable reactor conditions. The reactor tube is preferably
placed inside an oven to maintain a uniform reactor wall
temperature during the process. The oven can be of any kind, which
has sufficient temperature control (i.e. +1.degree. C. or less) at
low temperatures (less than 300.degree. C.). The temperature of the
oven is set such that the materials being processed do not
decompose. Typically the select oven temperature is within the
range of about 30 to 300.degree. C., more typically between about
70 to 200.degree. C. For the combination of beclomethasone
dipropionate and formoterol fumarate, for example, since the
melting point of beclomethasone dipropionate is about 210.degree.
C. and the melting point of formoterol fumarate is about
138.degree. C., the range of oven temperature used for the
combination particle production may vary between 30 to 110.degree.
C., preferably between 70 to 100.degree. C.
[0037] While there are no particular restrictions placed on the
particle collection, it is recommended to use a system, which can
be heated to prevent the re-condensation process. Electrostatic
precipitators, cyclones and/or filters can be used for this
purpose. Accordingly, the particle collection system and the line
from the flow reactor outlet to the particle collection system are
preferably heated to a temperature above the boiling point of the
solution to prevent the re-condensation process to occur. However,
the temperature should not be too high so as to cause material
degradation. For example, for the combination of beclomethasone
dipropionate and formoterol karate dissolved in ethanol, the
temperature of the collection system and the line may be kept
constant at a temperature between 80 to 100.degree. C., preferably
between 80 and 90.degree. C. To further prevent the re-condensation
process to occur, dry carrier gas may be flown to the particle
collection system. The carrier gas is preferably heated at a
temperature between 80 to 90.degree. C.
[0038] It is preferred that the aerosol flow reactor conditions are
selected such that crystalline spherical particles of homogeneous
constituents having a narrow particle size distribution and rough
surfaces are formed. The particle size of the resulting powder is
such that the mean mass aerodynamic diameter of said particles is
between about 0.5-10 .mu.m more typically between about 1-5 .mu.m.
Particularly it is preferred that more than 98% of the mass is in
particles having a diameter of 5 .mu.m or less, and less than about
5% of the mass being in particles having a diameter of 0.5 .mu.m or
less. It is particularly preferred that the aerodynamic particle
size distribution of said particles is between about 0.5-10 .mu.m,
more preferably between about 1-5 .mu.m.
[0039] The particles obtained incorporate, in an individual
particle, a combination of two or more drugs. An individual
particle means here an unagglomerated particle which have the
typical spherical form.
[0040] ID the particle of the invention, at least one of the active
ingredients is in a crystalline form, i.e. has a relative degree of
crystallinity preferably 90% or higher, more preferably 95% or
higher, most preferably 99% or higher. Preferably the aerosol flow
reactor conditions are selected such that all active ingredients in
the particle are in a crystalline form. The relative degree of
crystallinity can be determined based on the x-ray powder
diffraction patterns. The value of the relative degree of
crystallinity can be estimated by a known method of broadening of
the diffraction maxima (FWHM-values).
[0041] The particles of the invention are essentially spherical,
i.e. the spherical form is consistent and apparent when examined
under a scanning electron microscope. The spherical form reduces
the contact areas between particles and thereby improves
aerosolization and deagglomeration of the particles upon
inhalation.
[0042] Generally, the surface of the spherical particles is rough,
i.e. the roughness is consistent over the entire surface of the
particle, apparent when examined under the scanning electron
microscope, and the ratio of the maximum aid minimum diameter of
the particle is between 1.001-1.5, preferably between 1.002-1.2,
more preferably between 1.01-1.1. Rough surface is advantageous
since it increases the effective separation distance of the
particles, and thus improves aerosolization and deagglomeration
properties of the particles.
[0043] If desired, various additives known in the art may be
additionally incorporated in the particles together with the active
ingredients. Such additives include e.g. diluents such as lactose,
carriers and stabilizers and the like. In such case the additives
are included in the liquid feed stock of the process together with
the active ingredients. Also such additives incorporated in the
particle are preferably in crystalline form. It is particularly
preferred that at least about 90 w-% of the total weight of the
particle is in crystalline form.
[0044] However, in order to reduce the amount of material other
than the active ingredients potentially reaching the lungs, it is
preferred that the active ingredients constitute at least 90 w-%,
preferably at least 95 w-%, more preferably at least 99 w-%, of the
total weight of particles. Most preferably the particles are free
from other material than the active ingredients.
[0045] The particles of the invention may be formulated into an
inhalation composition together with one or more pharmaceutically
acceptable additives, diluents or carriers. Examples of suitable
solid diluents or carriers comprise lactose, dextran, mannitol and
glucose, lactose being preferred. Examples of aerosol carriers
include non-chlorofluorocarbon-based carriers such as HFA
(hydrofluoroalkane). The use of aqueous carriers is also possible.
Typical additives include solubilizers, stabilizers, flavouring
agents, colorizing agents and preserving agents.
[0046] The particles of the invention are preferably administered
in the form of a dry powder composition. The particles obtained are
generally in the form of individual (unagglomerated) particles
which are well suited for pulmonary drug delivery by inhalation as
such, e.g. they can be filled directly into capsules, cartridges,
blister packs or reservoirs of dry powder inhalers. However, if
desired the particles may be adapted to form loose agglomerates of
several individual particles, said agglomerates breaking into
individual particles upon dispersion in the inhaled air stream. The
particles may also be combined with pharmaceutically acceptable
carrier materials or excipients typically used in dry inhalation
powders. Such carriers may be used simply as bulking agents or to
improve the dispersibility of the powder. For example, the
particles may be used in admixture with carrier particles, e.g.
lactose, having larger particle size than the active ingredients,
typically in the range of 5 to 100 .mu.m. If the composition
contains a carrier, the total amount of the active ingredients is
typically about 0.1-50% (w/w), preferably about 1-10% (w/w), based
on total weight of the composition. Such compositions can be
prepared by methods known in the art.
[0047] The particles of the invention can be also administered in
the form of pressurized metered dose inhalation suspension, where
the particles are suspended in pressurized aerosol carrier and
delivered using pressurized metered dose inhaler (pMDI).
[0048] The invention is further illustrated by the following
experiments, which are not meant to limit the scope of the
invention.
EXPERIMENTS
[0049] All compositions produced according to the present invention
fulfill the strict specification for content and purity required
for pharmaceutical products.
Example 1
Preparation of Inhalation Particles Incorporating a Combination of
Beclomethasone Dipropionate and Formoterol Fumarate
[0050] Preparation of the Liquid Feed Stock
[0051] Beclomethasone dipropionate is an anti-inflammatory
glucocorticosteroid, which is practically insoluble in water,
freely soluble in acetone and in chloroform, and sparingly soluble
in alcohol. Thus, the solvent could be acetone, chloroform,
methanol, ethanol, or other alcohols. In the current experiments,
ethanol was used as a solvent, not only because ethanol is cheap
and readily available but it is also recommended for use in
production of pharmaceutical agents because it is non-toxic.
[0052] The beclomethasone dipropionate liquid feed stock was
prepared by dissolving 1 gram of beclomethasone dipropionate powder
in 40 ml of ethanol (99.5%) at room temperature.
[0053] Formoterol fumarate is a .beta..sub.2-agonist
bronchodilator, which is freely soluble in glacial acetic acid,
soluble in methanol, sparingly soluble in ethanol. Thus, the
solvent could be glacial acetic acid, methanol or ethanol. In the
current experiments, ethanol was used as a solvent, not only
because ethanol is cheap and readily available but it is also
harmless and recommended for use in production of
pharmaceuticals.
[0054] The formoterol fumarate liquid feed stock was prepared by
dissolving 1 gram of formoterol fumarate powder in 613 ml of
ethanol (99.5%) at room temperature.
[0055] The two liquid feed stocks were then mixed in such a way
that ratio between beclomethasone dipropionate and formoterol
fumarate in the mixture is 200:6 (weight basis), which was
considered to be a suitable drug ratio for the treatment of
asthma.
[0056] Aerosol Synthesis
[0057] FIG. 1a shows the experimental set-up of the particle
synthesis, and FIGS. 1b and 1c show optional configurations used
for particle analysis. The liquid feed stock described above was
atomised using an ultrasonic atomizer (2), sold under trademark RBI
Pyrosol 7901. The resulted droplets, which were suspended into a
carrier gas, were then passed through a heated tube flow reactor
(4). Nitrogen gas was used as a carrier gas, with a constant flow
rate of 1.5 l/min. To maintain a uniform solution concentration in
the atomizer, the carrier gas was bubbled through ethanol in a
saturation bottle (1) before entering the atomizer. A vertical
tube, which was inserted into an oven (3), was used to dry up the
droplets. The oven used was a WTB Binder FD/FED 400, which has
temperature variations of .+-.1 and .+-.2.degree. C. for
temperature at 70 and 110.degree. C., respectively. The tube was
made of stainless steel, with an inner diameter and a heated length
of 30 and 800 mm, respectively. The oven temperature was set at
100.degree. C. The minimum particle residence time in the heated
zone under the selected process conditions was approximately 12
seconds. From the CFD calculation, it is shown that temperature
field is uniform and the velocity is fully developed and
non-circulating in the heated zone.
[0058] The resulted particles were then collected using an
electrostatic precipitator (ESP) (5) connected to a high voltage
generator (6). A carrier gas, preferably nitrogen gas, may be flown
to the ESP to further prevent the re-condensation process to occur.
The exhaust gas was led from ESP via a dripping bottle (7) to exit
(9). FIG. 2 shows the schematic diagram of ESP having inlet (16)
and exit for exhaust gas (19). The ESP was made of a tubular
stainless steel collection plate (20) with inside diameter and
length of 10 and 50 cm, respectively. A 0.05 mm diameter tungsten
wire was placed on the center axis of the collection plate and a
high voltage (18) of 16 kV was applied between the wire and the
plate. The high electric field formed a corona discharge (17) on
the wire and charged the gas molecules. The gas ions were then
formed. These ions migrated across the space between the wire and
the plate under the influence of the applied electric field. During
the migration, the ions collided with the aerosol particles, which
thus acquired charge. The charged particles then migrated toward
the grounded surface electrode. When the particles struck the
grounded plate, they lost their charges and adhered to the plate
surface via surface forces. Therefore, the particles collected were
not charged. Dry nitrogen gas with a flow rate of 22.5 l/min was
flowed into the ESP and temperature in the ESP and in the line from
tubular tube outlet to the ESP were maintained at a constant
temperature of 85.degree. C., to avoid condensation of organic
vapours and moisture to occur. Condensation particle counter (CPC)
model 3022, shown as (8) in FIG. 1a, was used to determine
efficiency of the ESP. Particles collected were then removed from
the plate surface of ESP by scraping, and then placed in a tight
glass bottle to avoid moisture penetration or other
contamination.
[0059] Characterisation
[0060] i. Particle Size Analysis
[0061] Referring now to FIG. 1b, the particle size distribution was
measured by an electrical low pressure impactor (12) (ELPI)
connected to a vacuum (13). The particles exiting the tubular tube
were passed into a diluter (10), with a dilution ratio of 1:10,
before entering the ELPI. Exhaust gas exit (11) was arranged in the
diluter. To minimize temperature gradient, and thus to reduce the
moisture condensation, the diluter, the line to the diluter and the
gas line into the diluter were layered with heating elements, which
were kept at a temperature higher than that of the solution dew
point. FIGS. 3a and 3b show normalised and cumulative mass size
distributions of beclomethasone dipropionate/formoterol fumarate
particles, respectively, measured gravimetrically. It is shown that
a narrow size distribution within the range of aerodynamic particle
size of interest, i.e. at around 1-5 .mu.m, was obtained.
[0062] ii. Particle Crystallinity
[0063] Crystallinity of the sample was studied by X-ray powder
diffraction (Diffractometer D500, Siemens GmbH, Karlsruhe,
Germany). A copper target X-ray (wavelength 0.1541 nm) tube was
operated with the power of 40 kV.times.40 mA.
[0064] For x-ray powder diffraction analysis, 500 mg of the powder
was mounted to a cylindrical sample stage which has a diameter of
20 mm and height of approximately 2 mm.
[0065] The relative degree crystallinity of the powder was also
determined based on the x-ray powder diffraction patterns shown in
FIG. 4, wherein "A" means typical beclomethasone dipropionate, "B"
means typical formoterol fumarate and "C" means the (200:6)
combination of beclomethasone dipropionate (BDP) and formoterol
fumarate. It is noticed that the diffraction pattern of the
combination of beclomethasone dipropionate (BDP) and formoterol
fumarate resembles very much to the diffraction pattern of pure
BDP. Hence, formoterol fumarate may be partly or totally in
amorphous state. For BDP, it can be seen that the maximum
intensities were sharp and well above background intensities, which
indicates that the BDP in the powder was well crystallised. The
determined relative degree of crystallinity for BDP was 100%. The
estimation was based on the broadening of the diffraction maxima
(FWHM-values) positioned at 11.3.degree. and 18.4.degree..
[0066] iii. Powder Stability
[0067] The ratio of BDP to formoterol fumarate in the powder is
200:6 (formoterol fumarate is about 2.9% w/w). As shown from the
XRD pattern, formoterol fumarate in the powder may be in amorphous
state. Despite of the small formoterol concentration in the powder,
it was desirable to conduct stability tests to ensure that the
powder remains stable in various conditions. The stability tests
were carried out by observing moisture adsorption profiles of the
powder when exposed to different relative humidity levels. From
FIG. 5, it can be seen that the combination powder of the invention
is stable when exposed to different humidity levels, with a maximum
weight increase of 0.02% when exposed to 80% relative humidity for
24 h.
[0068] iv. Particle Shape and Surface Structure
[0069] Referring now to FIG. 1c, individual particles were
collected on the surface of a holey carbon film TEM grid (14)
connected to a vacuum (15) after particle collection. The
morphology of the particles were then imaged using a field emission
low voltage scanning electron microscope (FE-SEM) operated at 2 kV
acceleration voltage. FIG. 6 is a scanning electron microscope
image of the powder (magnification .times.27000). It is shown that
the particles are spherical with rough surfaces and diameter of
about 2-3 .mu.m.
[0070] v. Chemical Analysis
[0071] The product purity was analysed using Hewlett_Packard HP
1090 liquid Chromatograph equipped with diode array detector. The
column used is Hewlett-Packard Hypersil ODS, 5 .mu.m, 100.times.2.1
mm.
[0072] To analyse formoterol fumarate, the powder was dissolved
into 25 ml of a mixture of water-methanol (25:75). The sample was
then analysed using the high performance liquid chromatograph with
diode array detector (wavelengths 200 nm and 214 nm), and the
quantitative analyses were carried out using external standard
method with four standard concentrations. Eluents used were 0.01M
ammonium dihydrogen phosphate (NH.sub.3 is added to obtain pH 8)
(solvent A) and acetonitrile (solvent B) with gradient elution of
40% B for 2 minutes followed by 100% B in 5 minutes. The flow rate
and injection volume used were 0.4 ml/min and 5 .mu.l,
respectively, and the oven temperature was set to 40.degree. C.
[0073] To analyse beclomethasone dipropionate, the powder was
dissolved into 25 ml of a mixture of water-methanol (25:75) and
then diluted (1:50) using water-methanol (25:75). Samples were then
analysed with the high performance liquid, chromatograph using
diode array detector (wavelength 241 nm) and quantitative analyses
were carried using external standard method (four different
standard concentrations). Eluents used were water (solvent A) and
acetonitrile (solvent B) with gradient elution of 65% B for 2
minutes followed by 100% B in 5 minutes. The flow rate and
injection volume used were 0.4 ml/min and 8 .mu.l, respectively,
and the oven temperature was set to 40.degree. C.
[0074] The analysis results show beclomethasone dipropionate 97.1%
and formoterol fumarate 2.9%, the same as concentration of solution
precursor.
Example 2
Dry Inhalation Powder
TABLE-US-00001 [0075] Per dose Formoterol fumarate 6 .mu.g
Beclomethasone dipropionate 200 .mu.g Lactose monohydrate Ph. Eur.
8 mg
[0076] Particles of Example 1 and part of lactose is added into a
blender. The powder mixture is mixed until it is homogenous. The
mixture is sieved to reduce the number of particle clusters
present. Thereafter the rest of lactose is added and the powder is
again mixed until it is homogenous. Powder is poured into a supply
chamber of the multi-dose powder inhaler Easyhaler (Orion
Corporation trademark) for a supply of 200 doses.
* * * * *