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Pharm/Biotech Resources
Title: Formulation for inhalation
United States Patent: 6,926,908
Issued: August 9, 2005
Inventors: Robinson; Stuart (Nether Broughton, GB); Smith;
Susan Stewart (Loughborough, GB)
Assignee: Quadrant Drug Delivery Limited (Nottingham, GB)
Appl. No.: 218448
Filed: August 12, 2002
Abstract
Microparticles, obtainable by spray-drying a substantially pure solution
of a therapeutic agent, consist essentially of the agent having its
therapeutic activity when administered to the lung. In a preferred
embodiment the agent is insulin.
SUMMARY OF THE INVENTION
The present invention is based on the surprising discovery that it is
possible to spray-dry a therapeutic agent at higher (and therefore
commercially useful) concentrations than have been used previously, without
the concomitant production of an undesirable high concentration of salt or
other excipients. Such formulations show no substantial loss of activity
after the drying process and have extended stability, by comparison with
pre-spray-dried preparations. This discovery is of value for au therapeutic
agents, in particular proteins and peptides to be administered via the lung.
According to the present invention, microparticles, obtainable by
spray-drying a substantially pure solution of a therapeutic agent, consist
essentially only of the agent. In a preferred embodiment, the microparticles
consist essentially only of insulin and NaCl salt. Such microparticles may
be held in a container at greater than 10% RH, and thus essentially at
ambient humidity. The insulin microparticles are obtainable by dissolving
Zn-insulin in acid, adding alkali to give an insulin solution, e.g. to a pH
above 7, and spray-drying the insulin solution (which also contains a salt
formed as a result of The dissolution process, or a buffer).
Preferably, the microparticles are non-crystalline amorphous
DESCRIPTION OF THE INVENTION
As indicated above, microparticles of the invention "consist essentially"
of the therapeutic agent. This term is used herein to indicate that they are
substantially free of polysaccharide, or buffer salt, e.g. citrate, since
none is necessary. In general, there will be no polysaccharide present at
all, although an amount of up to, say 10% by weight may be tolerated. The
absence of polysaccharide has the advantage that a given unit dosage, e.g. a
particle, contains essentially only the intended active component. This is
an important consideration, for a drug that may be required in large
amounts. Another advantage is the avoidance of delivering unnecessary
material to a subject. A further advantage is that consistent dosing of the
therapeutic agent is facilitated; this is especially important where there
is a narrow therapeutic window.
The absence of buffer salt is desirable as it allows a more concentrated
feedstock solution of the active agent to be spray-dried resulting in
significant cost savings and providing a more commercial-scale process to be
adopted.
The term "substantially pure" is used herein to indicate that the feed stock
solution to be spray-dried comprises primarily only therapeutic agent and
solvent. Again, as described above, there may be a minor amount of solids
other than the active agent, but this has no significant effect on the
eventual stability of the product.
Insulin microparticles of the invention may include components that are
produced during the successive addition of acid and alkali, in preparation
of the feedstock, e.g. a salt. For example, NaCl is formed if the acid and
alkali are respectively HCl and NaOH. It has been found that the presence of
NaCl apparently has no stabilising effect. Indeed, stability may be greater
with reduced amounts of salt, again allowing a more concentrated feedstock
to be used.
Typically, the solution for spray-drying may contain less than 4% by weight
of salt, by weight of total solids. The salt content is based on theoretical
considerations, by titration to pH 7. More particularly, this value is
calculated by consideration of the molar quantities of the ions added during
dissolution. The solution may contain any desired amount of the therapeutic
agent, e.g. more than 20, 30 or 50 mg/ml, often up to 100 or 200 mg/ml.
As indicated above, successive addition of acid and alkali apparently
destroys the crystalline form of Zn insulin. Zn may dissociate from the
hexameric complex but need not be removed. Accordingly, Zn may be present in
the microparticles. If desired, this or any other component, other than the
therapeutic agent, may be removed, using any suitable technique known to
those of skill in the art. In a preferred embodiment for insulin, the Zn is
removed from solution prior to spray-drying. This may be achieved by
diafiltering the solution according to methods known in the art. The Zn-free
insulin may have greater stability than the Zn-containing product. Moisture
may also be present
As disclosed in more detail in WO-A-9218164, WO-A-9408627 and other Andaris
publications, the conditions of spray-drying can be controlled so that
microparticles having a defined size range, e.g. 0 1 to 50 μm, can be
obtained. The mass median particle size is preferably 1 to 10 μm, when the
product is intended for administration by inhalation.
The microparticles (microcapsules) obtained by spray-drying may be solid or
hollow Further, the surface may be smooth or "dimpled"; a dimpled surface
may be beneficial for inhalation.
The microparticles have good stability and may be maintained as such, i.e.
as a dry powder, in a container. During storage or in formulation, they may
be mixed with any suitable pharmaceutical agents, carriers, bulking agents
etc, and they may be processed by any technique desired to give a product
having the properties intended for the ultimate therapeutic use. In
particular, the formulation of particles for formulations that can be
delivered to the lung, e.g. using a metered dose or dry powder inhaler, are
known to those skilled in the art.
The nature of the container is not critical. For example, it may be a glass
jar or plastics box. It merely defines a storage environment within which,
unlike the prior art and as evidenced below, there is no need to remove
moisture or otherwise to control the conditions.
The therapeutic agent may be any protein or peptide having a desired
therapeutic effect. Included within the definition of proteins and peptides
are functional derivatives, such as glycoproteins. Typical examples of
proteins that may be used include enzymes, hormones and blood plasma
products. DNase and tryspin are specific examples Others include growth
hormone, calcitonins, interferons, interleukin-1 receptor and low molecular
weight heparin.
The therapeutic agent may in particular be any of those described in
WO-A-9632149. Insulin that is used in the invention may be of any suitable
form It may be, for example, bovine or human insulin. Results that have been
obtained, regarding the stability of bovine insulin, apparently apply also
to human insulin
The following Examples illustrate the invention.
EXAMPLE 1
A solution of bovine or human insulin for spray-drying is typically prepared
in the following way. 5 g insulin is dissolved in 70 ml 0.05 m HCl, after
which the solution is back-titrated with sufficient IM NaOH to reform a
solution from the isoelectric point precipitate. According to the final
concentration required, water is added to make to volume. Approximately 4.8
ml 1M NaOH is required, in this Example. The solution is then spray-dried
using a Mini spray drier with an outlet temperature of approximately 87° C.
and a solution feed rate of approximately 0.75 g/min
Reverse Phase High Performance Liquid Chromatography (RP-HPLC) was used to
assess the stability of insulin, under the following conditions.
| Column: |
Vydac C-18, 5 μm, 30 nm |
| Mobile Phase: |
A- 0.1% TFA in water |
| |
B- 0.1% TFA in acetonitrile (95%) and water (5%) |
| |
Gradient Elution |
| Flow Rate: |
1.5 mL/min |
| Detection: |
UV at 220 nm |
| Injection Volume: |
100 μL |
Under these conditions, bovine insulin has a retention time of
approximately 7.4 minutes.
A peak attributable to deamidated insulin is located at the failing edge of
the main peak. The extent of deamidation is used to indicate stability and
is calculated by expressing The area of the deamidation peak as a percentage
of the total peak area. Total degradation is expressed as the area of all
degrading peaks as a percentage of the total peak area.
| TABLE 1 |
| Percentage Total Degradation and Deamidation of Non-Spray Dried |
| Bovine Crystalline insulin |
| |
2° C./Ambient RH |
30° C./60% RH |
| |
% |
% |
% |
% |
| Time |
Deamidation |
Degradation |
Deamidation |
Degradation |
| Initial |
3.2 |
3.6 |
3.2 |
3.6 |
| 1 month |
3.5 |
3.9 |
4.2 |
5.3 |
| 3 months |
4.4 |
5.6 |
5.8 |
11.0 |
| 6 months |
3.4 |
4.5 |
6.7 |
13.7 |
| TABLE 2 |
| Percentage Total Degradation and Deamidation of Insulin |
| Microparticles |
| |
2° C./Ambient RH |
30° C./60% RH |
| % |
% |
% |
% |
| Deamidation |
Degradation |
Deamidation |
Degradation |
| Initial |
2.4 |
3.1 |
2.4 |
3.1 |
| 1 month |
2.8 |
3.9 |
3.1 |
4.6 |
| 3 months |
2.0 |
2.7 |
2.6 |
4.1 |
| 6 months |
1.9 |
3.0 |
2.8 |
5.0 |
The results indicate that the extent of both deamidation and total
degradation is increased with time, for all the batches evaluated.
Additionally, the data suggest that spray drying appears to confer
additional stability to the protein, in that the bovine crystalline insulin
control suffers increased degradation in comparison to the microparticle
formulations at comparable timepoints after storage at 30° C./60% RH.
To investigate whether this was also seen with human insulin, human insulin
microparticles were prepared (by the same general procedure as that
described above) and placed on accelerated stability at 40° C./75% RH. All
samples were analysed by RP-HPLC at the initial time point, and also after 1
week, 2 weeks and 5 weeks.
| TABLE 3 |
| Effect of Storage at 40° C./75% RH on the Deamidation and Total |
| Degradation Levels of Human Insulin Recombinant From E. Coli |
| Storage Time at |
|
|
| 40° C./75% RH |
% Deamidation |
% Total Degradation |
| 0 |
0.59 |
0.75 |
| 1 |
1.57 |
4.27 |
| 2 |
1.62 |
5.15 |
| 5 |
2.37 |
8.40 |
| TABLE 4 |
| Effect of Storage at 40° C./75% RH on the Deamidation and Total |
| Degradation Levels of Human Insulin Microparticles |
| Storage Time at |
|
|
| 40° C./75% RH |
% Deamidation |
% Total Degradation |
| 0 |
0.95 |
1.65 |
| 1 |
1.08 |
2.20 |
| 2 |
1.03 |
3.10 |
| 5 |
1.21 |
3.32 |
Comparing Tables 3 and 4, the microparticle formulation of human insulin
is less prone to degradation, showing only 3.32% total degradation for the 5
weeks at 40° C./75% RH compared to 8.40% total degradation for the material
stored as received under the same conditions.
Pikal and Rigsbee (1997), supra, although working on a lyophilised form of
insulin, might be understood to substantiate the findings reported herein.
Claim 1 of 53 Claims
1. Microparticles, obtainable by spray-drying a substantially pure
solution of a therapeutic agent, wherein the microparticles consist
essentially only of the therapeutic agent having its therapeutic activity
when administered to the lung, and further wherein the therapeutic agent is
a protein or peptide.
____________________________________________
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