U.S. patent application number 15/324377 was filed with the patent office on 2017-07-06 for method of preparing a pharmaceutical composition.
This patent application is currently assigned to 3M INNOVATIVE PROPERTIES COMPANY. The applicant listed for this patent is 3M INNOVATIVE PROPERTIES COMPANY. Invention is credited to WILLIAM F. HANSEN, DAVID W. SCHULTZ, JOHN K. SIMONS, STEPHEN W. STEIN.
Application Number | 20170189329 15/324377 |
Document ID | / |
Family ID | 53784018 |
Filed Date | 2017-07-06 |
United States Patent
Application |
20170189329 |
Kind Code |
A1 |
STEIN; STEPHEN W. ; et
al. |
July 6, 2017 |
METHOD OF PREPARING A PHARMACEUTICAL COMPOSITION
Abstract
The present disclosure provides a method of preparing a
pharmaceutical composition. The method includes transferring a
predetermined quantity of an excipient mixture from a second vessel
to a first vessel. The excipient mixture transferred from the
second vessel includes a liquid-state second quantity of a
hydrofluoroalkane propellant and a first solubilized excipient
comprising a low-molecular weight poly(ethylene oxide) polymer. The
method further includes contacting at least one
pharmaceutically-active compound with the excipient mixture under
conditions that facilitate forming an intermixture comprising the
propellant, the polymer, and the compound. Before transferring the
excipient mixture, the first vessel contains a vapor-phase first
quantity of the hydrofluoroalkane propellant and an effective
amount of the at least one pharmaceutically-active compound.
Inventors: |
STEIN; STEPHEN W.; (LINO
LAKES, MN) ; SCHULTZ; DAVID W.; (PINE SPRINGS,
MN) ; SIMONS; JOHN K.; (DAVIE, FL) ; HANSEN;
WILLIAM F.; (RIVERFALLS, WI) |
|
Applicant: |
Name |
City |
State |
Country |
Type |
3M INNOVATIVE PROPERTIES COMPANY |
SAINT PAUL |
MN |
US |
|
|
Assignee: |
3M INNOVATIVE PROPERTIES
COMPANY
SAINT PAUL
MN
|
Family ID: |
53784018 |
Appl. No.: |
15/324377 |
Filed: |
July 28, 2015 |
PCT Filed: |
July 28, 2015 |
PCT NO: |
PCT/US15/42429 |
371 Date: |
January 6, 2017 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
|
|
62030350 |
Jul 29, 2014 |
|
|
|
Current U.S.
Class: |
1/1 |
Current CPC
Class: |
A61K 9/1688 20130101;
B65B 31/003 20130101; A61K 31/137 20130101; A61K 47/32 20130101;
A61K 31/167 20130101; A61K 9/0007 20130101; A61K 31/137 20130101;
A61K 47/10 20130101; A61K 2300/00 20130101; A61K 9/008 20130101;
A61M 15/009 20130101; A61K 31/167 20130101; A61K 31/58 20130101;
A61K 45/06 20130101; A61K 47/06 20130101; A61K 31/58 20130101; A61K
2300/00 20130101; A61K 2300/00 20130101 |
International
Class: |
A61K 9/00 20060101
A61K009/00; A61K 9/46 20060101 A61K009/46; A61K 47/10 20060101
A61K047/10; A61M 15/00 20060101 A61M015/00; A61K 31/58 20060101
A61K031/58; A61K 31/137 20060101 A61K031/137; A61K 31/167 20060101
A61K031/167; B65B 31/00 20060101 B65B031/00; A61K 47/06 20060101
A61K047/06; A61K 47/32 20060101 A61K047/32 |
Claims
1. A method, comprising: transferring a predetermined quantity of
an excipient mixture from a second vessel to a first vessel;
wherein the excipient mixture transferred from the second vessel
comprises a liquid-state second quantity of a hydrofluoroalkane
propellant and a first solubilized excipient; wherein the first
solubilized excipient comprises a low-molecular weight
poly(ethylene oxide) polymer; wherein, before transferring the
excipient mixture, the first vessel contains a vapor-phase first
quantity of the hydrofluoroalkane propellant and an effective
amount of at least one pharmaceutically-active compound; and
contacting the at least one compound with the excipient mixture
under conditions that facilitate forming an intermixture comprising
the propellant, the first solubilized excipient, and the
pharmaceutically-active compound.
2. The method of claim 1, wherein forming the intermixture
comprises forming a pharmaceutical composition.
3. The method of claim 1, wherein the method further comprises
mixing a liquid-state third quantity of the hydrofluoroalkane
propellant with the intermixture to form a pharmaceutical
composition.
4. The method of claim 1 wherein, before transferring the excipient
mixture, the first vessel is substantially free of liquid-state
propellant in fluid contact with the at least one
pharmaceutically-active compound.
5. The method of claim 1, wherein the hydrofluoroalkane propellant
is selected from a group consisting of HFA-227, HFA-134A, and
mixtures thereof.
6. The method of claim 1, wherein the excipient mixture comprises
about 0.01 weight percent to about 3 weight percent of the
poly(ethylene oxide) polymer.
7. The method of claim 1, wherein the pharmaceutical composition
comprises about 0.01 weight percent to about 3.0 weight percent
poly(ethylene oxide) polymer.
8. The method of claim 1, wherein the excipient mixture further
comprises a second solubilized excipient.
9. The method of claim 8, wherein the second solubilized excipient
comprises a polyvinylpyrrolidone polymer.
10. The method of claim 1, wherein the at least one
pharmaceutically-active compound is selected from a group
consisting of formoterol fumarate and hydrates thereof, budesonide,
fluticasone propionate, fluticasone furoate, salmeterol xinafoate,
mometasone furoate, albuterol sulfate, beclomethasone, ipratropium
bromide, tiotropium bromide, ciclesonide, indacaterol, vilanterol,
glycopyrrolate, a generally long acting beta agonist, steroids,
long acting muscarinic agonists, and a combination of any of the
foregoing pharmaceutically-active compounds.
11. The method of claim 1, wherein the at least one
pharmaceutically-active compound comprises formoterol fumarate
dihydrate and budesonide.
12. The method of claim 1, wherein the at least one
pharmaceutically-active compound comprises albuterol sulfate.
13. The method of claim 1, wherein the at least one
pharmaceutically-active compound comprises particles, wherein the
particles have an average particle diameter of less than or equal
to 10 microns.
14. The method of claim 1: wherein transferring a predetermined
quantity of an excipient mixture from a second vessel to a first
vessel comprises placing the first and second vessels in fluid
communication; wherein, while the first and second vessels are in
fluid communication, the first vessel has a first internal pressure
and the second vessel has a second internal pressure; wherein the
first internal pressure is not more than about 210 kPa below the
second internal pressure.
15. The method of claim 1, further comprising forming the excipient
mixture, wherein forming the excipient mixture comprises:
contacting the poly(ethylene oxide) polymer with the second
quantity of the propellant, wherein at least a portion of the
poly(ethylene oxide) polymer contacted with the second quantity is
solid state poly(ethylene oxide) polymer; and heating the
propellant.
16. The method of claim 1, further comprising forming the excipient
mixture, wherein forming the excipient mixture comprises: heating
the poly(ethylene oxide) polymer; and after heating the
poly(ethylene oxide) polymer, contacting the poly(ethylene oxide)
polymer with the second quantity of the propellant.
17. The method of claim 1, further comprising transferring a
predefined mass of the intermixture to a vessel that is configured
to be used in a metered-dose inhaler.
18. The method of claim 1, further comprising transferring a
predefined mass of the pharmaceutical composition to a vessel that
is configured to be used in a metered-dose inhaler.
19. The method of claim 1 wherein, prior to transferring a
predetermined quantity of an excipient mixture from a second vessel
to a first vessel, the first vessel and the second vessel are
substantially free of an alcoholic solvent.
20. The method of claim 1 wherein, prior to transferring a
predetermined quantity of an excipient mixture from a second vessel
to a first vessel, the first vessel and the second vessel are
substantially free of a polar co-solvent.
Description
CROSS REFERENCE TO RELATED APPLICATIONS
[0001] This application claims priority to U.S. Provisional Patent
Application No. 62/030,350, filed Jul. 29, 2014, the disclosure of
which is incorporated by reference in its entirety herein.
BACKGROUND
[0002] Pressurized metered dose inhalers (MDIs) are widely used
devices for the delivery of medicaments to the respiratory tract by
inhalation via the oral and nasal routes. Though MDIs are used
primarily for topical delivery of drugs to the respiratory tract
for treatment of such diseases as asthma and chronic obstructive
pulmonary disease (COPD), there is increasing interest in their use
for systemic drug delivery. Classes of medicaments commonly
delivered by MDIs include bronchodilators (e.g. beta-agonists and
anticholinergics), corticosteroids, and anti-allergies.
[0003] MDI compositions are comprised of at least a medicament and
a propellant, but the MDI compositions may further comprise one or
more excipients other than propellant.
[0004] MDI compositions are generally characterized as either
solutions or suspensions. A solution composition comprises the
medicament dissolved or solubilized in propellant or in a mixture
of propellant and one or more excipients. A suspension composition
contains the medicament in the form of particles which are
dispersed in the propellant or in a mixture of propellant and one
or more other excipients.
[0005] Hydrofluroalkane (HFA) propellants, particularly
1,1,1,2-tetrafluoroethane (HFA-134a) and
1,1,1,2,3,3,3-heptafluoropropane (HFA-227), are currently favored
for respiratory drug delivery. Other alternatives to CFCs have been
proposed, including dimethyl ether and low molecular weight
hydrocarbons, such as propane and butane.
[0006] The efficiency of an aerosol device, such as an MDI, is a
function of the dose deposited at the appropriate site in the
respiratory tract. Deposition is affected by several factors
including, for example, the aerodynamic particle size. The
distribution of aerodynamic particle sizes of solid particles
and/or droplets in an aerosol can be characterized by their mass
median aerodynamic diameter (MMAD, the diameter around which the
mass aerodynamic diameters are distributed equally) and geometric
standard deviation (GSD, the measure of variability of the
aerodynamic particle diameters).
[0007] For inhalation therapy targeting the lungs, there is a
preference for aerosols in which the particles for inhalation have
an MMAD of about 0.5 to 10 .mu.m, more preferably about 0.5 to 5
.mu.m, and most preferably about 0.5 to 3 .mu.m. Particles larger
than about 5 .mu.m in diameter are primarily deposited by inertial
impaction in the oropharynx, particles of about 0.5 to 5 .mu.m in
diameter are ideal for deposition in the conducting airways, and
particles of about 0.5 to 3 .mu.m in diameter are desirable for
aerosol delivery to the lung periphery.
[0008] Methods are known in the art for the preparation of
suspension aerosol compositions for MDIs. The known methods
generally comprise the mixing of preformed medicament powders,
which are of a size suitable for inhalation therapy, with
propellant and optionally one or more other excipients. Control of
the particle size distribution of the aerosol particles generated
from the suspension aerosol composition is accomplished primarily
via control of the particle size distribution of the medicament
powders used to prepare the composition. Thus, considerable care is
normally taken to avoid dissolution of the medicament powder in the
excipients, as any dissolution of the medicament powder during
manufacture of the composition would result in loss of particle
size control. Conventional methods for generating medicament
powders suitable for preparation of compositions for inhalation
therapy, such as suspension aerosol compositions for MDIs, include
milling (micronization), spray drying, and supercritical fluid
recrystallization.
[0009] Suspension aerosol compositions are known in the art and
examples of such compositions are disclosed in WO 04/069225, EP
518601, U.S. Pat. No. 5,182,097, WO 93/11743, WO 93/11745, WO
98/05302, U.S. Pat. No. 6,261,539, EP 920302, WO 93/05765, WO
92/00061, EP 513127 and WO 01/47493; which are all incorporated by
reference in their entirety.
[0010] The conventional processes of MDI manufacture are generally
characterized as either "pressure filling" or "cold filling". In
pressure filling, the powdered medicament, optionally combined with
one or more excipients, is placed in a suitable aerosol container
capable of withstanding the vapor pressure of the propellant and
fitted with a metering valve. The propellant is then forced as a
liquid through the valve into the container. In an alternate
process of pressure filling, the particulate drug is combined in a
process vessel with propellant and optionally one or more
excipients, and the resulting drug suspension is transferred
through the metering valve fitted to a suitable MDI container. In
cold filling; the powdered medicament, propellant which is chilled
below its boiling point and, optionally, one or more excipients;
are added to the MDI container. In addition, a metering valve is
fitted to the container. For both pressure filling and cold filling
processes, additional steps; such as mixing, sonication, and
homogenization; are often advantageously included.
[0011] The dose limits of aerosol medication delivered to the
patient must consistently meet the specifications claimed by the
manufacturer and comply with the strict requirements of the
regulatory authorities.
SUMMARY
[0012] It is now known that processes used to form a mixture
comprising hydrofluoroalkane propellant, at least one
pharmaceutically-active compound, and a solubilized excipient
(e.g., a low-molecular weight poly(ethylene oxide) polymer) can be
improved by dissolving the solubilized excipient in the propellant
before contacting the propellant with the at least one
pharmaceutically-active compound. The inventive process of the
present disclosure facilitates rapid suspension of the at least one
pharmaceutically-active compound in the propellant.
[0013] In one aspect, the present disclosure provides a method of
preparing a pharmaceutical composition. The method can comprise
transferring a predetermined quantity of an excipient mixture from
a second vessel to a first vessel, wherein the excipient mixture
transferred from the second vessel comprises a liquid-state second
quantity of a hydrofluoroalkane propellant and a first solubilized
excipient; and contacting at least one pharmaceutically-active
compound with the excipient mixture under conditions that
facilitate forming an intermixture comprising the propellant, the
solubilized excipient, and the compound. The first solubilized
excipient can be a low-molecular weight poly(ethylene oxide)
polymer. Before transferring the excipient mixture, the first
vessel can contain a vapor-phase first quantity of the
hydrofluoroalkane propellant and an effective amount of the at
least one pharmaceutically-active compound.
[0014] In any embodiment, before transferring the excipient
mixture, the first vessel can be substantially free of liquid-state
propellant in fluid contact with the at least one
pharmaceutically-active compound. In any of the above embodiments,
the excipient mixture further can comprise a second solubilized
excipient. In any of the above embodiments, the at least one
pharmaceutically-active compound can be selected from a group
consisting of formoterol fumarate and hydrates thereof, budesonide,
fluticasone propionate, fluticasone furoate, salmeterol xinafoate,
mometasone furoate, albuterol sulfate, beclomethasone, ipratropium
bromide, tiotropium bromide, ciclesonide, indacaterol, vilanterol,
glycopyrrolate, generally long acting beta agonists, steroids, long
acting muscarinic agonists, and a combination of any of the
foregoing pharmaceutically-active compounds.
[0015] In any of the above embodiments, the at least one
pharmaceutically-active compound comprises a combination of two
compounds (e.g., a corticosteroid and a long-acting beta
agonist.
[0016] In any of the above embodiments, transferring a
predetermined quantity of an excipient mixture from a second vessel
to a first vessel can comprise placing the first and second vessels
in fluid communication. While the first and second vessels are in
fluid communication, the first vessel has a first internal pressure
and the second vessel has a second internal pressure and the first
internal pressure is not more than about 140 kPa below the second
internal pressure.
[0017] In any of the above embodiments, the method further can
comprise transferring a predefined mass of the intermixture or the
pharmaceutical composition to a vessel that is configured to be
used in a metered-dose inhaler.
[0018] The words "preferred" and "preferably" refer to embodiments
of the invention that may afford certain benefits, under certain
circumstances. However, other embodiments may also be preferred,
under the same or other circumstances. Furthermore, the recitation
of one or more preferred embodiments does not imply that other
embodiments are not useful, and is not intended to exclude other
embodiments from the scope of the invention.
[0019] The terms "comprises" and variations thereof do not have a
limiting meaning where these terms appear in the description and
claims.
[0020] The term "excipient mixture", as used herein, refers to a
composition that includes one or more excipient compound
solubilized (e.g., dissolved) in a liquid-state,
pharmaceutically-acceptable propellant.
[0021] The term "propellant" as used herein, means one or more
pharmacologically inert liquids or gases which exert a vapor
pressure at room temperature sufficient to propel a medicament from
a container (e.g., a canister) to a patient upon actuation of a
valve (e.g., a metering valve).
[0022] The term "pharmaceutical composition", as used herein,
refers to a mixture comprising at least one pharmaceutically-active
compound, at least one solubilized excipient, and a propellant;
each at a concentration that is pharmacologically suitable for
delivery to a patient from a metered-dose inhaler.
[0023] As used herein, "a," "an," "the," "at least one," and "one
or more" are used interchangeably. Thus, for example, "a" metered
dose inhaler can be interpreted to mean "one or more" metered dose
inhalers.
[0024] The term "and/or" means one or all of the listed elements or
a combination of any two or more of the listed elements.
[0025] Also herein, the recitations of numerical ranges by
endpoints include all numbers subsumed within that range (e.g., 1
to 5 includes 1, 1.5, 2, 2.75, 3, 3.80, 4, 5, etc.).
[0026] The above summary of the present invention is not intended
to describe each disclosed embodiment or every implementation of
the present invention. The description that follows more
particularly exemplifies illustrative embodiments. In several
places throughout the application, guidance is provided through
lists of examples, which examples can be used in various
combinations. In each instance, the recited list serves only as a
representative group and should not be interpreted as an exclusive
list.
[0027] Additional details of these and other embodiments are set
forth in the accompanying drawings and the description below. Other
features, objects and advantages will become apparent from the
description and drawings, and from the claims.
BRIEF DESCRIPTION OF DRAWINGS
[0028] FIG. 1 is a block diagram of one embodiment of a method
according to the present disclosure.
[0029] FIG. 2 is a schematic view of one embodiment of process
equipment used to practice a method according to the present
disclosure.
DETAILED DESCRIPTION
[0030] Before any embodiments of the present disclosure are
explained in detail, it is to be understood that the invention is
not limited in its application to the details of construction and
the arrangement of components set forth in the following
description or illustrated in the following drawings. The invention
is capable of other embodiments and of being practiced or of being
carried out in various ways. Also, it is to be understood that the
phraseology and terminology used herein is for the purpose of
description and should not be regarded as limiting. The use of
"including," "comprising," or "having" and variations thereof
herein is meant to encompass the items listed thereafter and
equivalents thereof as well as additional items. It is to be
understood that other embodiments may be utilized and structural or
logical changes may be made without departing from the scope of the
present disclosure.
[0031] The present disclosure provides a method. The method can be
used to manufacture a pharmaceutical composition that is used in a
metered-dose inhaler device. The pharmaceutical composition can
comprise a pharmaceutically-acceptable propellant (e.g., a
hydrofluoroalkane propellant), at least one pharmaceutically-active
agent, and at least one solubilized excipient. The at least one
solubilized excipient functions to facilitate suspension of the at
least one pharmaceutically-active compound in the propellant, to
lubricate the valve, and/or to manipulate the aerodynamic
properties of the delivered aerosol. A poly(ethylene oxide) polymer
is one example of a suitable solubilized excipient according to the
present disclosure.
[0032] As used herein, a poly(ethylene oxide) polymer (PEG polymer)
is a compound comprising one or more --(CH.sub.2CH.sub.20).sub.n--
recurring units, wherein n is an integer .gtoreq.5. For example, in
any embodiment, n is .about.6, .about.8, .about.20, .about.25,
.about.50, or .about.75. Preferred PEG polymers are linear. Most
preferably the PEG polymer is polyethylene glycol (PEG), i.e.
HO--(CH.sub.2CH.sub.20).sub.n--H. In any embodiment, the weight
average molecular weight of the PEG polymer is about 200 to about
3000 Da. In any other embodiment, the weight average molecular
weight of the PEG polymer is about 800 to about 2000 Da. In any
embodiment, the weight average molecular weight of the PEG polymer
is about 1000.
[0033] The at least one pharmaceutically-active agent can be an
agent that is delivered into the body in the form of particles. The
particles of the pharmaceutically-active agent are generally
micronized particles or particles processed by other methods known
in the art. In any embodiment, the particles can have a mass median
diameter equal to or greater than 1 micron. In any embodiment, the
particles can have a mass median diameter from about 1 micron to
about 5 microns or from about 1 micron to about 10 microns. Smaller
particles having a mass median diameter of less than one micron may
also be suitable.
[0034] In any embodiment, the at least one pharmaceutically-active
agent can be selected from a group of pharmaceutically-active
agents that are suitable for suspending in a hydroxyfluoroalkane
propellant and are capable of being delivered into a body using a
metered dose inhaler. Non-limiting examples of suitable
pharmaceutically-active agents include formoterol fumarate and
hydrates thereof, budesonide, fluticasone propionate, fluticasone
furoate, salmeterol xinafoate, mometasone furoate, albuterol
sulfate, beclomethasone, ipratropium bromide, tiotropium bromide,
ciclesonide, indacaterol, generally long acting beta agonist,
steroids, long acting muscarinic agonists, and a combination of any
of the foregoing pharmaceutically-active compounds.
[0035] Processes of the present disclosure include the use of
formoterol as a pharmaceutically-active compound. As would be
appreciated by the skilled person, formoterol includes two
asymmetric centers, and mometasone contains several asymmetric
centers. The present disclosure includes the use of each isomer of
formoterol either in substantially pure form or admixed in any
proportions or a racemic mixture, particularly the (R,R)-isomer.
The enantiomers of formoterol have been described previously, for
example, in WO 98/21175 and U.S. Pat. No. 5,795,564.
[0036] The use of pharmaceutically-active agents (e.g., formoterol)
in a process according to the present disclosure includes the use
of suitable salts of the pharmaceutically-active agents. Suitable
salts include, for example, those formed with both organic and
inorganic acids. Pharmaceutical acceptable acid addition salts
include but are not limited to those formed from hydrochloric,
hydrobromic, sulphuric, citric, tartaric, phosphoric, lactic,
pyruvic, acetic, trifluoroacetic, succinic, oxalic, fumaric,
maleic, oxaloacetic, methanesulphonic, ethanesulphonic,
p-toluenesulphonic, benzenesulphonic, isethionic, and
naphthalenecarboxylic, such as 1-hydroxy-2-naphthalenecarboxylic
acids.
[0037] Pharmaceutically acceptable esters of a
pharmaceutically-active agent (e.g., formoterol), for example, may
have a hydroxyl group converted to a C.sub.1-6 alkyl, aryl, aryl
C.sub.1-6 alkyl, hetaryl (such as furanyl) or amino acid ester.
[0038] In preferred embodiments of the invention, formoterol
fumarate (suitably as in the form of the dihydrate) is combined
with budesonide.
[0039] Hereinafter, the term "formoterol" is understood to include
formoterol or a pharmaceutical acceptable salt, solvate, or
physiologically functional derivative thereof. By the term
"physiologically functional derivative" is meant a chemical
derivative of formoterol having the same physiological function as
the free compound, for example, by being convertible in the body
thereto. According to the present invention, examples of
physiologically functional derivatives include esters.
[0040] Processes of the present disclosure include the use of at
least one solubilized excipient (e.g., a first solubilized
excipient such as a poly(ethylene oxide) polymer). The solubilized
excipient may be a homopolymer, that is the polymer consists of the
same recurring structural units, or it may be a co-polymer, that is
the polymer contains recurring units that are not the same.
[0041] In any embodiment, a method according to the present
disclosure can comprise a second solubilized excipient. Preferred
solubilized excipients include recurring structural units
containing an amide group, such as polyvinylpyrrolidone, for
example.
[0042] In general, it has been found that polyvinylpyrrolidones
having a wide range of average molecular weights give excellent
aerosol pharmaceutical compositions, in particular suspensions.
Particularly preferred embodiments of the invention are when the
second solubilized excipient is polyvinylpyrrolidone (PVP), also
known as povidone. Different types of PVP may be characterized by
their viscosity in solution, expressed as a K-value (see European
Pharmacopoeia, 5th ed., 2004, vol. 2, page 2289). Preferably the
K-value of the PVP used is between 10 and 150, more preferably
between 15 and 80, more preferably between 20 and 40, most
preferably about 25. Suitable polyvinylpyrrolidones are PVP (K25),
PVP (K30), Povidone K30, PVP (K29/32), PVP (K90), PVP (K120), PVP
(C15), PVP (C30) or PVP/17PF.
[0043] In any embodiment, the second solubilized excipient is a
co-polymer of vinyl acetate and vinyl pyrrolidone.
[0044] Alternative solubilized excipients also include those
containing carboxylic acid ester containing recurring structural
units such as polyvinyl acetate and co-polymers of vinyl acetate
and vinyl pyrrolidone, e.g. polyvinylpyrrolidone/vinyl acetate
co-polymer.
[0045] In any embodiment of the present disclosure, the aerosol
pharmaceutical composition may comprise at least one
pharmaceutically-active compound; HFA-134a, HFA-227, or mixtures
thereof; and a PEG polymer; wherein said composition contains no
alcoholic co-solvent. Preferably said composition contains no polar
protic co-solvent, more preferably said composition contains no
polar co-solvent.
[0046] In any embodiment of the present disclosure, the aerosol
pharmaceutical composition may comprise at least one
pharmaceutically-active compound; HFA-134a, HFA-227, or mixtures
thereof; a PEG polymer; and polyvinylpyrrolidone; wherein said
composition contains no alcoholic co-solvent. Preferably said
composition contains no polar protic co-solvent, more preferably
said composition contains no polar co-solvent.
[0047] In any embodiment of the present disclosure, the aerosol
pharmaceutical composition may comprise fluticasone or a
pharmaceutically acceptable derivative thereof, a hydrofluoroalkane
and a PEG polymer. In any embodiment said composition contains no
alcoholic co-solvent, preferably no polar protic co-solvent, more
preferably no polar co-solvent. Preferably said composition
contains only fluticasone or a pharmaceutically acceptable
derivative thereof, a hydrofluoroalkane, a PEG polymer; and
optionally one or more other pharmacologically active agents e.g.,
budesonide). Alternatively, preferably said composition contains
only fluticasone or a pharmaceutically acceptable derivative
thereof, a hydrofluoroalkane, a PEG polymer and, optionally, one or
more other pharmacologically active agents (e.g., budesonide).
[0048] The amount of PEG polymer (first solubilized excipient) in a
pharmaceutical composition made according to the present disclosure
will depend on the active ingredient to be dispersed, the
concentration of the active ingredient and the particular polymer
selected. However, in general the amount of PEG polymer in the
pharmaceutical composition is from 0.01 to 5 weight % of the
pharmaceutical composition (i.e., the composition that is used to
fill the canisters of a metered dose inhaler) made according to the
method of the present the present disclosure, more preferably the
amount of PEG polymer in the pharmaceutical composition is about
0.01 to about 1.0 weight %.
[0049] The amount of second solubilized excipient (e.g., PVP) in a
pharmaceutical composition made according to the present disclosure
will depend on the active ingredient to be dispersed, the
concentration of the active ingredient and the particular polymer
selected. However, in general the amount of PVP is from 0.0001 to 1
weight % of the pharmaceutical composition (i.e., the composition
that is used to fill the canisters of a metered dose inhaler) made
according to the method of the present the present disclosure, more
preferably the amount of PVP in the pharmaceutical composition is
about 0.0005 to 0.1
[0050] Pharmaceutical compositions made according to the present
disclosure comprise a propellant. Preferably, the propellant will
be a weak solvent or a non-solvent for the medicament; most
preferably, the propellant will be a non-solvent for the
medicament. Suitable propellants include, for example,
hydrofluoroalkanes such as 1,1,1,2-tetrafluoroethane
(CF.sub.3CH.sub.2F) (HFA-134a) and 1,1,1,2,3,3,3-heptafluoropropane
(CF.sub.3CHFCF.sub.3) (HFA-227), perfluoroethane,
monochloro-difluoromethane, 1,1-difluoroethane (HFA-152a),
tetrafluoromethane (PFC-14), trifluoromethane (HFA-23),
difluoromethane (HFA-32), fluoromethane (HFA-41),
1,1,2,2,2-pentafluoroethane (HFA-125), 1,1,2,2-tetrafluoroethane
(HFA-134), decafluorobutane (CF.sub.3CF.sub.2CF.sub.2CF.sub.3);
dialkyl ethers such as dimethyl ether; and low molecular weight
hydrocarbons such as n-butane, isobutane, propane, and
1,3,3,3-tetrafluoropropene (HFO-1234ze). Propellants may be used
singly or in combination. Preferably, the propellant is in a
substantially liquid state as it is mixed with the at least one
pharmaceutically-active compound and/or the one or more excipients
that are solubilized in the propellant. The propellant may be used
in a non-supercritical state.
[0051] Preferably the propellant used in the method of the present
disclosure is HFA-227 or HFA-134a or mixtures thereof, but most
preferably it is HFA-227.
[0052] The present disclosure provides a method. The method can be
used to prepare a pharmaceutical composition that is used in a
metered-dose inhaler device. The method involves the use of a
plurality of vessels. Each vessel may be any suitable vessel for
holding a quantity of propellant that is used in the pharmaceutical
composition. The propellant used to make a pharmaceutical
composition according to the present disclosure comprises a
hydrofluoroalkane propellant (e.g., HFA-227, HFA-134A, or mixtures
thereof) known in the art for use in a metered-dose inhaler
device.
[0053] The method includes a step that involves transferring at
least a portion of the contents of one vessel to another vessel.
FIG. 1 shows a block diagram of one embodiment of a method 1000
according to the present disclosure.
[0054] Prior to the transferring step described below, a first
vessel contains a vapor-state first quantity of a hydrofluoroalkane
propellant (e.g., HFA-227, HFA-134A, or mixtures thereof) and an
effective amount of at least one pharmaceutically-active compound
(e.g., at least one of the pharmaceutically-active compounds
suitable for distributing (e.g., suspending) in a
hydroxyfluoroalkane propellant and capable of being delivered into
a body using a metered dose inhaler, as described herein). Thus, in
any embodiment, a method according to the present disclosure
comprises adding the at least one pharmaceutically-active compound
to the first vessel, as shown in step 102 of the method 1000 of
FIG. 1. In any embodiment, prior to the transferring step described
below, the at least one pharmaceutically-active compound in the
first vessel is not in fluid contact with propellant.
[0055] The method further comprises adding the vapor-state first
quantity of hydrofluoroalkane propellant to the first vessel, as
shown in step 104 of the method 1000 of FIG. 1. Preferably, prior
to the transferring step described below, the first vessel is
substantially free of liquid-state propellant in fluid contact with
the at least one pharmaceutically-active compound. "Substantially
free of liquid-state propellant", as used herein means that less
than 5%, less than 4%, less than 3%, less than 2%, less than 1%,
less than 0.5%, or 0% of the mass of the liquid-state propellant
used to make the intermixture according to the present disclosure
is in fluid contact with the at least one pharmaceutically-active
compound.
[0056] In any embodiment, the effective amount of the at least one
pharmaceutically-active compound is in the form of particles as
described herein. In any embodiment, the particles can be
substantially insoluble in the propellant and/or in a solubilized
low-molecular weight poly(ethylene oxide) polymer and/or in
solubilized polyvinylpyrrolidone or mixtures thereof (i.e.,
mixtures of the propellant and the solubilized low-molecular weight
poly(ethylene oxide) and/or the solubilized polyvinylpyrrolidone).
A person having ordinary skill in the art will appreciate that the
effective amount of the at least one pharmaceutically-active
compound will depend upon certain aspects (e.g., the valve
configuration, the propellant, the actuator, the particle size of
the at least one pharmaceutically-active compound) of the MDI
device that is to be used to deliver the pharmaceutical composition
into a body and the amount of pharmaceutically-active compound
(i.e., the pharmaceutical dose) that is intended to be dispensed in
each metered dose delivered by the MDI device. The selection of the
effective amount of the at least one pharmaceutically-active
compound in the pharmaceutical composition prepared according to
the present disclosure is well within the ambit of a person having
ordinary skill in the art.
[0057] Also prior to the transferring step described below, the
second vessel contains a predetermined quantity of an excipient
mixture, wherein the excipient mixture comprises a liquid-state
second quantity of the hydrofluoroalkane propellant (e.g., HFA-227,
HFA-134A, or mixtures thereof) and a first solubilized excipient
(e.g., a low-molecular weight poly(ethylene oxide) polymer). In any
embodiment, the excipient mixture comprises an optional second
solubilized excipient (e.g., polyvinylpyrrolidone). Thus, in any
embodiment, a method according to the present disclosure comprises
contacting a liquid-state second quantity of the
hydroxyfluoroalkane propellant with a suitable excipient (e.g.,
low-molecular weight poly(ethylene oxide) polymer) in the second
vessel, as shown in step 106 of the method 1000 of FIG. 1
[0058] In any embodiment, the liquid-state second quantity of the
hydroxyfluoroalkane propellant can be heated before and/or after
contacting the propellant with the low-molecular weight
poly(ethylene oxide) polymer. Heating the propellant can facilitate
melting the low-molecular weight poly(ethylene oxide) polymer and,
preferably, formation of a substantially homogeneous excipient
mixture. Heating the propellant can comprise heating the propellant
to a temperature near or above the melting point of the first
solubilized excipient (e.g., a poly(ethylene oxide) polymer) or the
second solubilized excipient (e.g., PVP). In any embodiment,
contacting a liquid-state second quantity of the
hydroxyfluoroalkane propellant with the low-molecular weight
poly(ethylene oxide) polymer in the second vessel optionally
comprises mixing the excipient mixture comprising the second
quantity of the hydroxyfluoroalkane propellant and the
low-molecular weight poly(ethylene oxide) polymer.
[0059] In any embodiment, the quantity of low-molecular weight
poly(ethylene oxide) polymer with which the liquid-state second
quantity of the hydrofluoroalkane propellant is contacted can be
greater than 0 weight percent (e.g., greater than or equal to 0.01
weight percent, greater than or equal to 0.025 weight percent,
greater than or equal to 0.05 weight percent, up to about 1 weight
percent, up to about 3 weight percent, up to about 5 weight
percent, up to about 10 weight percent, up to about 15 weight
percent, up to about 20 weight percent) up to about 25 weight
percent of the resulting excipient mixture comprising the of
low-molecular weight poly(ethylene oxide) polymer and the
liquid-state second quantity of the hydrofluoroalkane propellant.
In any embodiment, the quantity of low-molecular weight
poly(ethylene oxide) polymer with which the liquid-state second
quantity of the hydrofluoroalkane propellant is contacted can be
about 0.05 weight percent to about 15 weight percent of the
resulting excipient mixture comprising the of low-molecular weight
poly(ethylene oxide) polymer and the liquid-state second quantity
of the hydrofluoroalkane propellant. In any embodiment, the
quantity of low-molecular weight poly(ethylene oxide) polymer with
which the liquid-state second quantity of the hydrofluoroalkane
propellant is contacted can be about 0.1 weight percent to about 10
weight percent of the resulting excipient mixture comprising the of
low-molecular weight poly(ethylene oxide) polymer and the
liquid-state second quantity of the hydrofluoroalkane
propellant.
[0060] A "low-molecular weight poly(ethylene oxide) polymer", as
used herein, refers to a poly(ethylene oxide) polymer composition
having a weight average molecular weight of about 200 Daltons to
about 3000 Daltons. In any embodiment, the low-molecular weight
poly(ethylene oxide) polymer can have a weight average molecular
weight of about 800 Daltons to about 2000 Daltons. In any
embodiment, the low-molecular weight poly(ethylene oxide) polymer
can have a weight average molecular weight of about 1000
Daltons.
[0061] The second quantity of hydrofluoroalkane propellant is a
portion (e.g., <1%, about 1%, about 3%, about 5%, about 10%,
about 15%, about 20%, about 25%, about 30%, about 35%, about 40%,
about 45%, about 50%, about 55%, about 60%, about 65%, about 70%,
about 85%, about 80%, about 85%, about 90%, about 95%, >95%) of
the total mass of the hydrofluoroalkane propellant used in the
pharmaceutical composition made using the method of the present
disclosure.
[0062] Optionally, in any embodiment, the second quantity of
hydrofluoroalkane propellant can be heated (e.g., in the second
vessel) to facilitate dissolution of the solid-state low-molecular
weight poly(ethylene oxide) polymer. In any embodiment, the second
quantity of propellant can be heated before contacting the
low-molecular weight poly(ethylene oxide) polymer with the second
quantity of propellant (not shown in FIG. 1) and/or after the
low-molecular weight poly(ethylene oxide) polymer is contacted with
the second quantity of propellant (as shown in step 108 of the
method 1000 of FIG. 1).
[0063] In any embodiment, the method comprises transferring the
predetermined quantity of the excipient mixture from the second
vessel to the first vessel. In any embodiment, internal pressure
can be monitored in both the first and second vessels during the
transfer. In addition, in any embodiment, the internal pressure can
be regulated in at least one of the first and second vessels (as
shown in step 110 of the method 1000 of FIG. 1) to ensure the
internal pressure of the first vessel is at a pressure that is not
more than about 210 kPa, not more than 140 kPa, not more than about
105 kPa, not more than about 70 kPa, or not more than about 35 kPa
below the internal pressure of the second vessel. In any
embodiment, the pressure in the first and second vessels can be
approximately equalized before the transfer. Advantageously,
keeping the vessels within a predetermined pressure differential
prevents sudden excessive vaporization of propellant from the
excipient mixture as it is transferred into the first vessel.
Excessive vaporization of liquid-state propellant as it enters the
first vessel can result in a rapid temperature drop (e.g., to a
temperature where the solubility limit of one or more solubilized
excipient is below the concentration of the solubilized excipient
in the second quantity of the propellant) that can cause
precipitation of at least a portion of the low-molecular weight PEG
polymer or other solubilized excipient from the excipient mixture,
which could result in a decreased ability to suspend the at least
one pharmaceutically-active compound in the pharmaceutical
composition.
[0064] In any embodiment, the temperature of the first vessel and
second vessel can be same immediately prior to transferring the
excipient mixture. Alternatively, the temperature of the first
vessel and second vessel may be different immediately prior to
transferring the excipient mixture. In any embodiment, the
temperature of the second vessel immediately prior to transferring
the excipient mixture may be higher than the first vessel.
[0065] In order to transfer the predetermined quantity of the
excipient mixture from the second vessel to the first vessel, the
first vessel and second vessel are placed into fluid communication
with each other, as shown in step 112 of the method 1000 of FIG. 1.
This can be done, for example, by opening at least one valve that
is disposed between the first and second vessels, as shown in FIG.
2.
[0066] In any embodiment, prior to transferring the excipient
mixture from the second vessel to the first vessel, the first
vessel and second vessel are substantially free of an alcoholic
co-solvent (e.g., ethanol). "Substantially free of an alcoholic
co-solvent", as used herein means that the mass of alcoholic
co-solvent in either or both of the first and second vessels is
less than 1%, less than 0.5%, less than 0.1%, or 0% of the total
mass of the pharmaceutical composition produced by the method of
the present disclosure.
[0067] In any embodiment, prior to transferring the excipient
mixture from the second vessel to the first vessel, the first
vessel and second vessel are substantially free of a polar
co-solvent (e.g., ethanol, isopropanol). "Substantially free of a
polar co-solvent", as used herein means that the mass of polar
co-solvent in either or both of the first and second vessels is
less than 1%, less than 0.5%, less than 0.1%, or 0% of the total
mass of the pharmaceutical composition produced by the method of
the present disclosure.
[0068] The method further comprises contacting the at least one
pharmaceutically-active compound with the excipient mixture under
conditions that facilitate forming an intermixture comprising the
propellant, the polymer, and the pharmaceutically-active compound,
as shown in step 114 of the method 1000 of FIG. 1. Such conditions
are known to a person having ordinary skill in the art and may
include, for example, heating and/or stirring. In any embodiment,
the intermixture can be stirred (e.g., in the first vessel) at a
sufficient speed and for a sufficient period of time to obtain a
substantially homogeneous mixture of the liquid propellant, the
low-molecular weight PEG, and the particles of the at least one
pharmaceutically-active compound.
[0069] In any embodiment, forming an intermixture comprising the
propellant, the polymer, and the pharmaceutically-active compound
may comprise forming a pharmaceutical composition. Accordingly, in
these embodiments, the intermixture comprises at least one
pharmaceutically-active compound, at least one solubilized
excipient, and a propellant; each at a first concentration that is
pharmacologically suitable for delivery to a patient from a
metered-dose inhaler.
[0070] Optionally, in any embodiment, the method further comprises
mixing a liquid-state third quantity of the hydrofluoroalkane
propellant with the intermixture to form a pharmaceutical
composition. In these embodiments, the at least one
pharmaceutically-active compound and the at least one solubilized
excipient of the intermixture are diluted with the liquid-state
third quantity of the hydrofluoroalkane propellant to form a
pharmaceutical composition wherein the at least one
pharmaceutically-active compound, the at least one solubilized
excipient, and the propellant each is at a concentration that is
pharmacologically suitable for delivery to a patient from a
metered-dose inhaler. In these embodiments of the method, the
intermixture may or may not be a pharmaceutical composition
according to the present disclosure. In the embodiments wherein the
intermixture is a first pharmaceutical composition (e.g., a
"high-dose" first pharmaceutical composition), the diluted
intermixture diluted with addition hydrofluoroalkane propellant is
a second pharmaceutical composition (e.g., a "low dose" second
pharmaceutical composition).
[0071] In any embodiment, the liquid-state third quantity of the
hydrofluoroalkane propellant may be added to the intermixture in
any suitable vessel (e.g., a relatively large vessel for the
preparation of bulk quantities of the pharmaceutical composition
(e.g., the second pharmaceutical composition) or a relatively small
vessel (e.g., a canister to be used in a metered dose
inhaler)).
[0072] In any embodiment, a method of the present disclosure
further comprises transferring a predefined mass of the
pharmaceutical composition to a vessel that is configured to be
used in a metered-dose inhaler.
[0073] Dispensers comprising an aerosol vial equipped with
conventional dispensing valves, preferably metered dose valves, can
be used to deliver formulations of the invention. Conventional
dispensers and aerosol vials can be used to contain a formulation
of the invention. However it has been found that certain vials
enhance the chemical stability of certain formulations of the
invention. Therefore it is preferred to contain a formulation of
the invention within a glass aerosol vial or a metal, in particular
aluminum, vial having an interior surface coated with a non-metal
coating. A suitable non-metal coating can include a plasma
deposited coating such as a diamond like glass coating. Another
suitable non metal coating can include a polymer coating, in
particular a fluorocarbon polymer coating. Such coatings are known
in the art and are described, for example in U.S. Pat. Nos.
8,430,097; 8,414,956; 8,616,201; 8,104,469; and U.S. Patent
Application Publication Nos. 2013/0019863, 2013/0025592, and
2011/0103330; which are all incorporated herein by reference in
their entirety. Advantageously other internal surfaces, in
particular such surfaces of components of the valve, or all of the
internal surfaces of the dispenser may be also coated with a
polymer, in particular a fluorocarbon polymer. Suitable
fluorocarbon polymers include fluorocarbon polymers, which are made
of multiples of one or more of the following monomeric units:
tetrafluoroethylene (PTFE), fluorinated ethylene propylene (FEP),
perfluoroalkoxyalkane (PFA), ethylene tetrafluoroethylene (ETFE),
vinylidenefluoride (PVDF), and chlorinated ethylene
tetrafluoroethylene. Polymers, which have a relatively high ratio
of fluorine to carbon, such as perfluorocarbon polymers e.g. PTFE,
PFA, and FEP, are preferred; FEP is particularly preferred.
[0074] The valve may be any suitable metering valve with an outlet
made from, for example, stainless steel, acetal, nylon or
polybutylene terephthalate and with seals made from nitrile or EPDM
elastomer.
[0075] A pharmaceutical composition prepared according to any
process of the present disclosure can be administered to the
respiratory tract by oral or nasal inhalation. Oral inhalation is
preferred, and conventional actuators for oral inhalation can be
used in connection with a pharmaceutical composition made according
to a process of the present disclosure. It has been found that good
respirable doses are achieved with an orifice diameter within the
range of 0.2 to 0.6 mm, preferably in the range 0.30 to 0.50 mm,
most preferably 0.35 to 0.45 mm.
[0076] FIG. 2 shows one embodiment of a system 2000 that can be
used to practice an embodiment of a method according to the present
disclosure. The system 2000 comprises a first vessel 20 and a
second vessel 25 in selective fluidic communication with the first
vessel via two valves (valves 51 and 52, respectively). Also in
selective fluidic communication with the first vessel 20 is a vapor
addition vessel 45, which supplies vapor-state propellant (e.g.,
HFA-227, HFA-134A, or mixtures thereof) to the first vessel 20. The
vapor addition vessel 45 is selectively isolated from the first
vessel 20 via a plurality of valves (valves 58, and 61,
respectively).
[0077] The second vessel 25 and vapor addition vessel 45 can be
supplied with propellant from a propellant reservoir 30. The
propellant reservoir 30 is selectively isolated from the vapor
addition vessel 45 via a plurality of valves (valves 53 and 61,
respectively) and is selectively isolated from the second vessel 25
via a plurality of valves (valves 53 and 54, respectively).
[0078] The first vessel 20 is in selective fluid communication with
a filler 40, which is configured to deliver the resulting
substantially homogeneous pharmaceutical composition (not shown)
from the first vessel 20 into a canister (not shown) to be used in
a drug-delivery device (e.g., a metered-dose inhaler device). The
pharmaceutical composition is transferred from the first vessel 20
to the filler 40 (e.g., by a pump 50). During use, the propellant
reservoir 30 is used to deliver liquid-state propellant to the
second vessel 25 (to which the first excipient (i.e., the
low-molecular weight PEG polymer) is added) and to deliver
liquid-state and/or vapor-state propellant to the vapor addition
vessel 45. The vapor addition vessel 45 is used to add vapor-state
propellant to first vessel 20. After the excipient mixture is
prepared in the second vessel 25 according to the present
disclosure, the excipient mixture is transferred to the first
vessel 20, where it is mixed with at least one
pharmaceutically-active compound to make suspension (e.g., a
homogeneous suspension) of the pharmaceutical composition.
Optionally, additional liquid phase propellant can be added to
first vessel 20 through valve 58 after some or all of the excipient
mixture has been added to first vessel 20 in order to achieve the
proper final concentrations of the pharmaceutically-active agent
and the solubilized excipient(s) in the pharmaceutical composition.
After the suspension of the pharmaceutical composition is prepared
in the first vessel 20, at least a portion of the pharmaceutical
composition is transferred (e.g., pumped) to the filling unit 40
where the suspension is used to fill canisters for drug-delivery
devices (e.g., metered-dose inhalers).
[0079] In any embodiment, the contents of the first vessel 20 can
be transferred to a larger vessel (not shown) into which additional
liquid-state propellant can be added to achieve the final
concentration of suspended pharmaceutically-active compound for use
in a metered dose inhaler.
[0080] Certain embodiments of the methods of the present disclosure
are set forth in the following list of embodiments.
EMBODIMENTS
[0081] Embodiment A is method, the method comprising:
[0082] transferring a predetermined quantity of an excipient
mixture from a second vessel to a first vessel; [0083] wherein the
excipient mixture transferred from the second vessel comprises a
liquid-state second quantity of a hydrofluoroalkane propellant and
a first solubilized excipient; [0084] wherein the first solubilized
excipient comprises a low-molecular weight poly(ethylene oxide)
polymer; [0085] wherein, before transferring the excipient mixture,
the first vessel contains a vapor-phase first quantity of the
hydrofluoroalkane propellant and an effective amount of at least
one pharmaceutically-active compound; and
[0086] contacting the compound with the excipient mixture under
conditions that facilitate forming an intermixture comprising the
propellant, the first solubilized excipient, and the at least one
pharmaceutically-active compound.
[0087] Embodiment B is the method of Embodiment A, wherein forming
the intermixture comprises forming a pharmaceutical
composition.
[0088] Embodiment C is the method of Embodiment A or Embodiment B,
wherein the method further comprises mixing a liquid-state third
quantity of the hydrofluoroalkane propellant with the intermixture
to form a pharmaceutical composition.
[0089] Embodiment D is the method of any one of the preceding
Embodiments wherein, before transferring the excipient mixture, the
first vessel is substantially free of liquid-state propellant in
fluid contact with the at least one pharmaceutically-active
compound.
[0090] Embodiment E is the method of any one of the preceding
Embodiments, wherein the hydrofluoroalkane propellant is selected
from a group consisting of HFA-227, HFA-134A, and mixtures
thereof.
[0091] Embodiment F is the method of any one of the preceding
Embodiments, wherein the low-molecular weight poly(ethylene oxide)
polymer has a weight average molecular weight of about 200 Daltons
to about 3000 Daltons.
[0092] Embodiment G is the method of Embodiment F, wherein the
low-molecular weight poly(ethylene oxide) polymer has a weight
average molecular weight of about 800 Daltons to about 2000
Daltons.
[0093] Embodiment H is the method of Embodiment F, wherein the
low-molecular weight poly(ethylene oxide) polymer has a weight
average molecular weight of about 1000 Daltons.
[0094] Embodiment I is the method of any one of the preceding
Embodiments, wherein the excipient mixture comprises about 0.01
weight percent to about 25 weight percent of the poly(ethylene
oxide) polymer.
[0095] Embodiment J is the method of Embodiment I, wherein the
excipient mixture comprises about 0.05 weight percent to about 15
weight percent of the poly(ethylene oxide) polymer.
[0096] Embodiment K is the method of Embodiment I, wherein the
excipient mixture comprises about 0.1 weight percent to about 10
weight percent of the poly(ethylene oxide) polymer.
[0097] Embodiment L is the method of any one of the preceding
Embodiments, wherein the pharmaceutical composition comprises about
0.01 weight percent to about 3.0 weight percent poly(ethylene
oxide) polymer.
[0098] Embodiment M is the method of Embodiment L, wherein the
pharmaceutical composition comprises about 0.05 weight percent to
about 0.5 weight percent poly(ethylene oxide) polymer.
[0099] Embodiment N is the method of Embodiment L, wherein the
pharmaceutical composition comprises about 0.3 weight percent
poly(ethylene oxide) polymer.
[0100] Embodiment O is the method of any one of the preceding
Embodiments, wherein the excipient mixture further comprises a
second solubilized excipient.
[0101] Embodiment P is the method of Embodiment O, wherein the
second solubilized excipient comprises a polyvinylpyrrolidone
polymer.
[0102] Embodiment Q is the method of Embodiment P, wherein the
polyvinylpyrrolidone polymer has a K-Value of about 15 to 150
according to the K-Value test described in the European
Pharmacopoeia, 5th edition.
[0103] Embodiment R is the method of Embodiment P, wherein the
polyvinylpyrrolidone polymer has a K-Value of about 15 to 80
according to the K-Value test described in the European
Pharmacopoeia, 5th edition.
[0104] Embodiment S is the method of Embodiment P, wherein the
polyvinylpyrrolidone polymer has a K-Value of about 20 to about 40
according to the K-Value test described in the European
Pharmacopoeia, 5th edition.
[0105] Embodiment T is the method of Embodiment P, wherein the
polyvinylpyrrolidone polymer has a K-Value of about 25 according to
the K-Value test described in the European Pharmacopoeia, 5th
edition.
[0106] Embodiment U is the method of any one of Embodiments P
through T, wherein the pharmaceutical composition comprises about
0.0001 weight percent to about 0.05 weight percent of the
polyvinylpyrrolidone polymer.
[0107] Embodiment V is the method of any one of Embodiments P
through U, wherein the pharmaceutical composition comprises about
0.0001 weight percent to about 0.0015 weight percent of the
polyvinylpyrrolidone polymer.
[0108] Embodiment W is the method of any one of Embodiments P
through U, wherein the pharmaceutical composition comprises about
0.0003 weight percent of the polyvinylpyrrolidone polymer.
[0109] Embodiment X is the method of any one of Embodiments P
through U, wherein the pharmaceutical composition comprises about
0.0005 weight percent of the polyvinylpyrrolidone polymer.
[0110] Embodiment Y is the method of any one of Embodiments P
through U, wherein the pharmaceutical composition comprises about
0.0007 weight percent of the polyvinylpyrrolidone polymer.
[0111] Embodiment Z is the method of any one of Embodiments P
through U, wherein the pharmaceutical composition comprises about
0.001 weight percent of the polyvinylpyrrolidone polymer.
[0112] Embodiment AA is the method of any one of the preceding
Embodiments, wherein the at least one pharmaceutically-active
compound is selected from a group consisting of formoterol fumarate
and hydrates thereof, budesonide, fluticasone propionate,
fluticasone furoate, salmeterol xinafoate, mometasone furoate,
albuterol sulfate, beclomethasone, ipratropium bromide, tiotropium
bromide, ciclesonide, indacaterol, vilanterol, glycopyrrolate,
generally long acting beta agonist, steroids, long acting
muscarinic agonists, and a combination of any of the foregoing
pharmaceutically-active compounds.
[0113] Embodiment AB is the method of Embodiment AA, wherein the at
least one pharmaceutically-active compound comprises formoterol
fumarate dihydrate and budesonide.
[0114] Embodiment AC is the method of Embodiment AA, wherein the at
least one pharmaceutically-active compound comprises albuterol
sulfate.
[0115] Embodiment AD is the method of any one of the preceding
Embodiments, wherein the at least one pharmaceutically-active
compound comprises particles, wherein the particles have an average
particle diameter of less than or equal to 10 microns.
[0116] Embodiment AE is the method of any one of the preceding
claims:
[0117] wherein transferring a predetermined quantity of an
excipient mixture from a second vessel to a first vessel comprises
placing the first and second vessels in fluid communication;
[0118] wherein, while the first and second vessels are in fluid
communication, the first vessel has a first internal pressure and
the second vessel has a second internal pressure;
[0119] wherein the first internal pressure is not more than about
210 kPa below the second internal pressure.
[0120] Embodiment AF is the method of Embodiment AE, wherein the
first internal pressure is not more than about 105 kPa below the
second internal pressure.
[0121] Embodiment AG is the method of Embodiment AE, wherein the
first internal pressure is not more than about 70 kPa below the
second internal pressure.
[0122] Embodiment AH is the method of Embodiment AE, wherein the
first internal pressure is not more than about 35 kPa below the
second internal pressure.
[0123] Embodiment AI is the method of any one of the preceding
Embodiments, further comprising forming the excipient mixture,
wherein forming the excipient mixture comprises:
[0124] contacting the poly(ethylene oxide) polymer with the second
quantity of the propellant, wherein at least a portion of the
poly(ethylene oxide) polymer contacted with the second quantity is
solid state poly(ethylene oxide) polymer; and
[0125] heating the propellant.
[0126] Embodiment AJ is the method of Embodiment AI, wherein
heating the propellant comprises heating the propellant before it
is contacted with the poly(ethylene oxide) polymer.
[0127] Embodiment AK is the method of Embodiment AI or Embodiment
AJ, wherein heating the propellant comprises heating the propellant
after it is contacted with the poly(ethylene oxide) polymer.
[0128] Embodiment AL is the method of any one of Embodiments A
through AH, further comprising forming the excipient mixture,
wherein forming the excipient mixture comprises:
[0129] heating the poly(ethylene oxide) polymer; and
[0130] after heating the poly(ethylene oxide) polymer, contacting
the poly(ethylene oxide) polymer with the second quantity of the
propellant.
[0131] Embodiment AM is the method of any one of the preceding
Embodiments, further comprising transferring a predefined mass of
the intermixture to a vessel that is configured to be used in a
metered-dose inhaler.
[0132] Embodiment AN is method of any one of the preceding
Embodiments, further comprising transferring a predefined mass of
the pharmaceutical composition to a vessel that is configured to be
used in a metered-dose inhaler.
[0133] Embodiment AO is the method of any one of the preceding
Embodiments wherein, prior to transferring a predetermined quantity
of an excipient mixture from a second vessel to a first vessel, the
first vessel and the second vessel are substantially free of an
alcoholic solvent.
[0134] Embodiment AP is the method of Embodiment AO wherein, prior
to transferring a predetermined quantity of an excipient mixture
from a second vessel to a first vessel, the first vessel and the
second vessel are substantially free of ethanol.
[0135] Embodiment AQ is the method of any one of the preceding
Embodiments wherein, prior to transferring a predetermined quantity
of an excipient mixture from a second vessel to a first vessel, the
first vessel and the second vessel are substantially free of a
polar co-solvent.
[0136] Objects and advantages of this invention are further
illustrated by the following examples, but the particular materials
and amounts thereof recited in these examples, as well as other
conditions and details, should not be construed to unduly limit
this invention.
Examples
[0137] The following compositions were prepared using standard
methods well known to those skilled in the art. After the
compositions were made according to the present disclosure, the
compositions were filled into aluminum aerosol canisters having a
fluoropolymer coating comprising either an
ethylene-tetrafluoroethylene co-polymer (ETFE) or a blend of
perfluorinated ethylene propylene co-polymer (FEP) and
polyethersulphone (PES). Aerosol canisters were fitted with
metering valves obtained from Aptar Pharma (Congers, N.Y.). As
observed visually in glass bottles, compositions prepared according
to the present invention were in the form of suspensions which were
readily dispersed by hand shaking. The suspension stability of each
composition was suitable for use with a metered dose inhaler.
TABLE-US-00001 TABLE 1 List of Materials Name Chemical name Source
Budesonide 16,17-(butylidenebis(oxy))-11,21- dihydroxy-,
(11-.beta.,16-.alpha.)-pregna-1,4- diene-3,20-dione Formoterol
rac-(R,R)-N-[2-hydroxy-5-[1-hydroxy-2-[1- fumarate
(4-methoxyphenyl) propan-2-ylamino]ethyl] phenyl]formamide,
fumarate salt, dihydrate PEG 1000 Polyethylene glycol PVP K25
Polyvinylpyrrolidone HFA-227 1,1,1,2,3,3,3-heptafluoropropane
Examples 1-2. Preparation of a Pharmacologic Composition Comprising
Budesonide and Formoterol Fumarate
TABLE-US-00002 [0138] TABLE 2 Composition of the MDI formulation
made using the process of Examples 1 and 2. Component Example 1
Example 2 Budesonide, micronized 7.28 g 7.28 g Formoterol fumarate,
0.204 g 0.21 g micronized PEG 1000 9.0 g 9.0 g PVP K25 0 g 0.03 g
HFA-227 2983.59 g 2983.56 g
[0139] The micronized Budesonide and Formoterol fumarate were added
to a one-gallon (3.785 liters) first vessel (see first vessel 20,
FIG. 2), taking care not to introduce any of the powder into an
exit port in the vessel. The first vessel was connected to a vapor
addition vessel (see vapor addition vessel 45, FIG. 2) and a second
vessel (see second vessel 25, FIG. 2). At least one valve between
the first vessel and the vapor addition vessel was closed and at
least one valve between the first vessel and the second vessel was
closed. The vapor addition vessel contained HFA 227.
[0140] Solid-state PEG 1000 and PVP K25 were added to the second
vessel. About 300 g of HFA 227 was added to the second vessel and
the second vessel was sealed. The second vessel was heated to about
30-40.degree. C. until the PEG and PVP were dissolved
(approximately 15-30 minutes) to form the excipient mixture, after
which the heat source was removed.
[0141] A valve was opened to place the first vessel in vapor
communication with the vapor addition vessel and the first vessel
was slowly pressurized with HFA 227 vapor from the vapor addition
vessel, being careful not to disturb the powdered
pharmaceutically-active agents. Heat was applied to the vapor
addition vessel as needed to maintain a pressure differential
between the first vessel and the vapor addition vessel of no
greater than about 35 kPa. The first vessel was filled with HFA 227
vapor to a pressure of about 350 kPa, after which all valves
between the first vessel and the vapor addition vessel were
closed.
[0142] Valves were opened to place the second vessel in fluid
communication with the first vessel and the liquid in the second
vessel was transferred into the first vessel until the entire
contents (i.e., the excipient mixture) of the second vessel were
transferred. During the entire transfer process, the pressure
differential between the second vessel and the first vessel was
maintained at less than or equal to about 138 kPa.
[0143] The valves were closed and additional HFA 227 was added to
the second vessel to rinse/dilute any residue of the excipient
mixture that wasn't transferred. The valves were re-opened and the
rinse liquid (HFA 227) from the second vessel was transferred into
the first vessel. During the entire transfer process, the pressure
differential between the second vessel and the first vessel was
maintained at less than or equal to about 138 kPa. The rinse
process was repeated several times until the first vessel contained
the total amount of HFA 227 shown in Table 2, after which all
valves were closed. The contents of the first vessel were mixed at
about 7500 rpm for about 5 minutes.
[0144] After mixing, the substantially-homogeneous pharmaceutical
composition in the first vessel was aliquoted into MDI canisters.
MDI canisters were pressure-filled with the composition.
Example 3. Preparation of a Pharmacologic Composition Comprising
Albuterol Sulfate
TABLE-US-00003 [0145] TABLE 3 Composition of the MDI formulation.
Component Example 3 Albuterol sulfate, micronized 3.60 g PEG 1000
9.0 g PVP K25 0.03 g HFA-134a 2987.37 g
[0146] The composition of Example 3 was prepared using the process
described for Examples 1-2.
[0147] The uniformity of the suspensions of the compositions made
according to Examples 1-4 was assessed visually and appeared
satisfactory for use in a metered dose inhaler.
[0148] Effect of Process on the Efficiency of Suspending the
Pharmaceutically-Active Particles.
Example 4. Preparation of a Pharmacologic Composition Comprising
Budesonide and Formoterol Fumarate
[0149] The composition of Example 4 was prepared using the
components listed in Table 4 according to the process described for
Examples 1 and 2. After mixing the contents of Vessel 1 to form the
intermixture comprising the propellant, the first solubilized
excipient, and the pharmaceutically-active compounds, Vessel 1 was
drained. 500 milliliters of 100% ethanol was added to vessel 1 and,
using a disposable pipette, the walls and mixer shaft were rinsed
with the ethanol to dissolve any residue within vessel. An aliquot
of the ethanol was tested to quantify budesonide and formoterol
fumarate using High Performance Liquid Chromatography. The results
are shown in Table 5.
Comparative Example 1. Preparation of a Pharmacologic Composition
Comprising Budesonide and Formoterol Fumarate
[0150] The quantities of budesonide, formoterol fumarate, PEG 1000,
and PVP K25 shown in Table 4 were placed into a vessel and the
quantity of liquid-state HFA-227 was added to the vessel. The
vessel was stirred at an elevated temperature (about 40.degree. C.
for approximately 93 minutes) to allow the excipients to dissolve.
After the mixing step, the vessel was drained and the residue was
analyzed to quantify budesonide and formoterol fumarate as
described in Example 4. The results are shown in Table 5.
TABLE-US-00004 TABLE 4 Composition of MDI formulations made in
Example 4 and Comparative Example 1. Component Example 4
Comparative Example 1 Budesonide, micronized 3.60 g 3.60 g
Formoterol fumarate, 0.21 g 0.21 g micronized PEG 1000 9.0 g 9.0 g
PVP K25 0.03 g 0.03 g HFA-227 2987.16 g 2987.16 g
TABLE-US-00005 TABLE 5 Residual budesonide and formoterol fumarate
in vessels. The results are reported in micrograms per milliliter
ethanol. Residual formoterol fumarate dihydrate Residual budesonide
(.mu.g/mL) (.mu.g/mL) Example 4 2.93 78.25 Comparative Example 1
4.69 126.07
[0151] The results show that the active ingredients are suspended
more efficiently while using the inventive process than while using
a conventional process for preparing a pharmacologic composition.
Thus, the method of the present disclosure results in less
deposition (i.e., loss) of the active ingredients onto the surface
of the mixing vessel than conventional processes.
[0152] The complete disclosure of all patents, patent applications,
and publications, and electronically available material cited
herein are incorporated by reference. In the event that any
inconsistency exists between the disclosure of the present
application and the disclosure(s) of any document incorporated
herein by reference, the disclosure of the present application
shall govern. The foregoing detailed description and examples have
been given for clarity of understanding only. No unnecessary
limitations are to be understood therefrom. The invention is not
limited to the exact details shown and described, for variations
obvious to one skilled in the art will be included within the
invention defined by the claims.
[0153] All headings are for the convenience of the reader and
should not be used to limit the meaning of the text that follows
the heading, unless so specified.
[0154] Various modifications may be made without departing from the
spirit and scope of the invention. These and other embodiments are
within the scope of the following claims.
* * * * *