U.S. patent application number 12/687691 was filed with the patent office on 2010-07-22 for novel process.
This patent application is currently assigned to AstraZeneca AB. Invention is credited to Eva Trofast.
Application Number | 20100183729 12/687691 |
Document ID | / |
Family ID | 9892016 |
Filed Date | 2010-07-22 |
United States Patent
Application |
20100183729 |
Kind Code |
A1 |
Trofast; Eva |
July 22, 2010 |
Novel Process
Abstract
The invention relates to a stable pharmaceutical composition
useful in the treatment of respiratory disorders such as asthma,
rhinitis and chronic obstructive pulmonary disease (COPD) and a
novel micronisation process for manufacturing a stable formulation
for formoterol or its enantiomers and a carrier/diluent comprising
a carbohydrate such as lactose.
Inventors: |
Trofast; Eva; (Lund,
SE) |
Correspondence
Address: |
FISH & RICHARDSON P.C.
P.O BOX 1022
MINNEAPOLIS
MN
55440-1022
US
|
Assignee: |
AstraZeneca AB
Sodertalje
SE
|
Family ID: |
9892016 |
Appl. No.: |
12/687691 |
Filed: |
January 14, 2010 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
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11627051 |
Jan 25, 2007 |
7670625 |
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12687691 |
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10276458 |
Nov 18, 2002 |
7179489 |
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PCT/SE01/01117 |
May 17, 2001 |
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11627051 |
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Current U.S.
Class: |
424/489 ;
514/630 |
Current CPC
Class: |
A61P 11/02 20180101;
Y10S 514/952 20130101; A61K 9/0075 20130101; A61K 31/165 20130101;
A61K 9/145 20130101; A61P 11/00 20180101; A61P 11/06 20180101; Y10S
514/951 20130101 |
Class at
Publication: |
424/489 ;
514/630 |
International
Class: |
A61K 9/14 20060101
A61K009/14; A61K 31/167 20060101 A61K031/167; A61P 11/00 20060101
A61P011/00; A61P 11/06 20060101 A61P011/06 |
Foreign Application Data
Date |
Code |
Application Number |
May 19, 2000 |
GB |
0012261.4 |
Claims
1. A process for preparing a pharmaceutical composition comprising,
in admixture, an active ingredient which is micronised formoterol
or an enantiomer thereof, optionally in the form of a salt or
solvate of a salt, and a micronised carrier/diluent, which process
comprises preparing a mixture of micronised active ingredient and
carrier/diluent, followed by addition of further pre-micronised
carrier/diluent which is mixed in at low energy, and either
subjecting the mixture to agglomeration and spheronisation, or
adding coarse carrier/diluent.
2. A process according to claim 1 in which formoterol is in the
form of its fumarate dihydrate salt.
3. A process according to claim 1 or 2 in which the formoterol is
in the form of the single R,R-enantiomer.
4. A process according to any one of claims 1 to 3 in which the
carrier is a coarse carbohydrate.
5. A process according to any of claims 1 to 4 in which the carrier
is lactose.
6. A pharmaceutical composition comprising, in admixture, an active
ingredient which is micronised formoterol optionally in the form of
a salt or solvate or a solvate of a salt, and a micronised
pharmaceutically acceptable carrier/diluent, the composition having
a high storage stability.
7. A pharmaceutical composition according to claim 6 in which
formoterol is in the form of its fumarate dihydrate salt.
8. A pharmaceutical composition according to claims 6 and 7 in
which the formoterol is in the form of the single
R,R-enantiomer.
9. A pharmaceutical composition according to any one of claims 6 to
8 in which the carrier/diluent is lactose.
10. A pharmaceutical composition according to any one of claims 6
to 9 in which the particle size of the formoterol is less than 10
um.
11. A pharmaceutical composition according to any one of claims 6
to 10 for use for the treatment or prophylaxis of a respiratory
disorder.
12. A pharmaceutical composition according to any one of claims 6
to 11 for use for the treatment or prophylaxis of asthma, rhinitis
or COPD.
13. A method of treating a respiratory disorder in a mammal which
comprises administering to a patient a pharmaceutical composition
according to any one of claims 6 to 12.
Description
CROSS-REFERENCE TO RELATED APPLICATIONS
[0001] This application is a continuation (and claims the benefit
of priority under 35 USC 120) of U.S. application Ser. No.
11/627,051, filed Jan. 25, 2007, which is a divisional of U.S.
application Ser. No. 10/276,458 filed on Nov. 18, 2002, which is a
National Stage application under 35 U.S.C. .sctn.371 and claims
benefit under 35 U.S.C. .sctn.119(a) of International Application
No. PCT/SE01/01117 having an International Filing Date of May 17,
2001, which claims the benefit of priority of United Kingdom
0012261.4 having a filing date of May 19, 2000. The disclosure of
the prior application is considered part of (and is incorporated by
reference in) the disclosure of this application.
FIELD OF THE INVENTION
[0002] The present invention relates to a stable pharmaceutical
composition and a novel micronisation process for manufacturing a
stable formulation for formoterol or its enantiomers and a
carrier/diluent comprising a carbohydrate such as lactose.
BACKGROUND OF THE INVENTION
[0003] Stability is one of the most important factors which
determines whether a compound or a mixture of compounds can be
developed into a therapeutically useful pharmaceutical product.
When mixing different ingredients in a pharmaceutical formulation
there exists the possibility of interactions taking place between
the components. In addition, each component may have different
degradation characteristics.
[0004] Formoterol is a highly potent and selective .beta.2-agonist
with a long duration of action when inhaled. Compared to
other-adrenergic compounds it has a unique chemical structure with
a formamido group substituted on the benzene ring. It has two
asymmetric carbon atoms in the molecule making four stereoisomers
possible. Most studies, clinical and preclinical, appear to have
been performed with the fumarate (as dihydrate) of the enantiomeric
mixture designed R; R+S; S. The R; R enantiomer is the most potent
of the four enantiomers.
[0005] The stability profile of the drug formoterol (as fumarate
dihydrate) has been evaluated by investigating the influence of
variables such as storage time, temperature, relative humidity,
light and pH on the content of formoterol and determining the
amount of chromatographic impurities. Formoterol (as fumarate
dihydrate) has been demonstrated to be stable under long-term
storage even at high temperatures and high relative humidities.
[0006] However, the chemical structure of formoterol makes the
molecule prone to chemical degradation when in contact with e.g. a
reactive species like an aldehyde or under stress conditions e.g. a
milling process.
[0007] Potent drugs for administration by inhalation are generally
formulated in association with carriers/diluents such as lactose to
facilitate accurate dosing from an inhaler. These formulations have
generally consisted of coarse particles of a carrier together with
fine particles of the drug (s), optionally together with small
particles of carrier/diluent, which combination is generally known
as an ordered mixture. An alternative to such a formulation is to
agglomerate the small particles of the drug (s) and the
carrier/diluent to agglomerates.
[0008] Formoterol (as fumarate dihydrate) as well as a carbohydrate
e.g. lactose (preferably as the monohydrate) are very stable
compounds individually, but degradation products are formed when
the two compounds are mixed. A mixture of formoterol fumarate
dihydrate and lactose monohydrate can be regarded as a three
component system composed of formoterol fumarate, lactose and
water. By sorption of water a saturated aqueous lactose solution is
formed at the surface of the powder mixture. A certain amount of
formoterol fumarate dissolves in this aqueous solution and is
thereby susceptible to degradation.
[0009] Therefore, the relative humidity, as well as the storage
temperature, will influence the stability of the powder
mixture.
[0010] It would therefore be desirable to develop a formulation
with good stability in spite of the complex mixture of compounds
having reactive chemical groups like an amine (formoterol),
formamide (formoterol) and a carbohydrate (e.g. lactose). The
presence of hydrates (formoterol fumarate dihydrate, lactose
monohydrate) will make it even more complex.
DESCRIPTION OF THE INVENTION
[0011] In accordance with the present invention, there is provided
a process for preparing a pharmaceutical composition comprising, in
admixture, an active ingredient which is micronised formoterol or
an enantiomer thereof and a micronised carrier/diluent, which
process comprises:
1. preparing a mixture of micronised active ingredient and
carrier/diluent, 2. followed by addition of further pre-micronised
carrier/diluent which is mixed in at low energy, and 3. either
subjecting the mixture to agglomeration and spheronisation, or
adding coarse carrier/diluent.
[0012] The first active ingredient and carrier/diluent can be
prepared according to step 1 by micronising the two components
together or each can be micronised individually and then combined
to give a micronised mixture. Preferably the first active
ingredient and carrier/diluent are mixed together and then
micronised.
[0013] Preferably step 3 involves subjecting the mixture to
agglomeration and spheronisation.
[0014] Optionally the mixture/ingredients can be conditioned at any
suitable stage of the process, such as between steps 1 and 2,
and/or the further pre-micronised carrier/diluent can be
conditioned at step 2, and/or the mixture can be conditioned
between the agglomeration and spheronisation in step 3. Preferably
the mixture/ingredients is conditioned between steps 1 and 2, and
the further pre-micronised carrier/diluent is conditioned at step
2.
[0015] Conditioning can be carried out according to the procedures
described in WO 95/05805 or by selecting the process parameters
such as relative humidity in such a way that the final product when
submitted to water vapour gives off heat of less than 1.2 joules
per gram for the particles having a mean particle size of less than
10 um as described and measured in U.S. Pat. No. 5,874,063.
[0016] By "low energy" is meant mixing at low pressure, preferably
below 2 bar, more preferably below 1 bar. Preferably the
micronisation as well as the mixing step are carried out in a
spiral jet mill.
[0017] By "micronised" is meant milling to give a desired particle
size or obtaining a desired particle size by any other means for
producing small particles such as direct precipitation.
[0018] The process of the invention produces compositions having
high storage stability in that the decomposition of formoterol in
the formulation will be less than 10% when stored in open dishes at
40.degree. C. and 75% relative humidity for 6 months when the
content of formoterol is less than about 1.0% (w/w), preferably
less than about 0.8% (w/w) and most preferably less than about 0.6%
(w/w) in the formulation or, when stored in a dry powder device, a
decomposition of less than about 2.5% under the same
conditions.
[0019] The formoterol can be in the form of a mixture of
enantiomers. Preferably the formoterol is in the form of a single
enantiomer, preferably the R; R enantiomer. The formoterol can be
in the form of the free base, salt or solvate, or a solvate of a
salt, preferably the formoterol is in the form of its fumarate
dihydrate salt. Other suitable physiologically salts include
chloride, bromide, sulphate, phosphate, maleate, tartrate, citrate,
benzoate, 4-methoxybenzoate, 2- or 4-hydroxybenzoate,
4-chlorobenzoate, p-toluenesulphonate, benzenesulphonate,
ascorbate, acetate, succinate, lactate, glutarate, gluconate,
tricaballate, hydroxynapaphthalenecarboxylate or oleate.
[0020] Preferably the carrier/diluent is a carbohydrate, more
preferably a reducing carbohydrate such as lactose, glucose,
galactose, mannose, xylose, maltose, cellobiose, mellibiose,
maltotriose (e.g. as monohydrates). More preferably the carrier is
lactose, most preferably lactose monohydrate.
[0021] As used herein the term micronised carrier/diluent refers to
carrier/diluent having a mean particle size of less than about 25
.mu.m, preferably less than about 10 .mu.m, more preferable less
than about 5 .mu.m. The term coarse carrier/diluent refers to
carrier/diluent having a mean particle size of greater than about
25 .mu.m.
[0022] As used herein the term micronised active ingredient means
active ingredient having a mean particle size of less than about 10
.mu.m, preferably less than about 5 .mu.m.
[0023] The pharmaceutical compositions according to the invention
can be used for the treatment or prophylaxis of a respiratory
disorder, in particular the treatment or prophylaxis of asthma,
rhinitis or COPD.
[0024] In a further aspect the invention provides a method of
treating a respiratory disorder, in particular asthma, rhinitis or
COPD, in a mammal which comprises administering to a patient a
pharmaceutical composition as herein defined.
[0025] The compositions of the invention can be inhaled from a
nebulizer, from a pressurized metered dose inhaler or as a dry
powder from a dry powder inhaler e.g. multidose reservoir systems
from AstraZeneca (Turbuhaler) or Schering-Plough or from a dry
powder inhaler utilizing gelatine, plastic or other capsules,
cartridges or blister packs. Doses will be dependent on the
severity of the disease and the type of patient.
[0026] The process of the invention is shown schematically in FIG.
2.
BRIEF DESCRIPTION OF DRAWINGS
[0027] FIG. 1 is a graph illustrating the results of the
experiments described in Examples 1 and 2.
[0028] FIG. 2 is a diagram showing the steps of a process according
to one embodiment of the invention.
EXPERIMENTAL SECTION
[0029] The invention is illustrated by the following examples which
are not intended to limit the scope of the application. In the
examples micronisation is carried out such that the particle size
range for each of the active components is suitable for
administration by inhalation.
[0030] The determination of the formoterol degradation products was
performed by reversed phase liquid chromatography, on a two column
system using LiChrospher 60 RP-select B.
[0031] 5 .mu.m particles with octylsilane as stationary phase.
UV-detector at 214 nm. Evaluation was done as area-% since the
degradation products were not fully known.
Example 1
[0032] The following example is a reference example in which the
formulation is prepared in a conventional manner.
[0033] Formoterol fumarate dihydrate (26.5 g) and lactose
monohydrate (4.97 kg) are mixed for one or two hours in a tumbling
mixer. This mixture was micronised in a spiral jet mill in order to
attain a particle size suitable for inhalation. Micronisation of
substances into the low micron range (1-5 .mu.m) may induce
disturbances in the crystallinity of the substance.
[0034] Amorphous areas are introduced, especially at the surfaces
of the micronised substance.
[0035] This morphological change of the substances will increase
the sensitivity to humidity and thereby being an potential
implement to stability problems. The crystal structure of the
substance mixture was restored in a controlled way according to
U.S. Pat. No. 5,874,063 or U.S. Pat. No. 5,709,884.
[0036] To improve the flowability of the cohesive powder it was
spheronised to agglomerates at room temperature at a controlled
relative humidity of less than 50%.
[0037] The micronised and spheronised formoterol fumarate
dihydrate/lactose monohydrate formulation according to example 1
was filled in the powder device Turbuhaler (AstraZeneca) and stored
for 6 months at 40.degree. C. and 75% relative humidity. Results
are shown in FIG. 1 (A).
Example 2
[0038] Formoterol fumarate dihydrate (0.575 kg) and lactose
monohydrate (4.425 kg) were mixed for two to four hours in a
tumbling mixer. The mixture was micronised in a spiral jet mill in
order to attain a particle size suitable for inhalation. The
crystal structure was restored in a controlled way according to
U.S. Pat. No. 5,874,063 or U.S. Pat. No. 5,709,884. To part of this
mixture (223 g) was added further micronised and conditioned
lactose monohydrate (4.77 kg) and the mixture was blended using
very low energy in a modified spiral jet mill followed by a
spheronisation step to provide agglomerates.
[0039] The micronised and spheronised formoterol fumarate
dihydrate/lactose monohydrate formulation was filled into the dry
powder device Turbuhaler.RTM. (AstraZeneca) and stored for 6 months
at 40.degree. C. and 75% relative humidity. Results are shown in
FIG. 1 (B).
* * * * *