Title:  Process for the preparation of suspensions of drug particles for inhalation delivery

United States Patent:  6,464,958

Issued:  October 15, 2002

Inventors:  Bernini; Eva (Parma, IT); Malvolti; Chiara (Parma, IT); Garzia; Raffaella (Parma, IT); Brambilla; Gaetano (Parma, IT); Chiesi; Paolo (Parma, IT)

Assignee:  Chiesi Farmaceutici S.p.A. (Parma, IT)

Appl. No.:  830884

Filed:  May 22, 2001

PCT Filed:  October 28, 1999

PCT NO:  PCT/EP99/08176

371 Date:  May 22, 2001

102(e) Date:  May 22, 2001

PCT PUB.NO.:  WO00/25746

PCT PUB. Date:  May 11, 2000

The invention is directed to a process for the preparation of suspensions of drug particles for inhalation delivery, said process providing particles of optimized particle size and distribution homogeneously dispersed in the carrier. The process, which is also suitable for the preparation of sterile suspensions, includes the step of homogenizing and micronizing the formulation in a turboemulsifier provided with a high-potency turbine, optionally followed by a treatment in a high-pressure homogenizer. A further aspect of the invention is directed to a process for preparing micronized sterile beclomethasone dipropionate by gamma-irradiation.

Description of the Invention

The administration of drugs through inhalation has been used for many years and is the mainstay of treatment of diseases which limit airflow, such as asthma and chronic bronchitis.

Furthermore, a number of inhalatory formulations have been marketed for some years, for the administration of steroidal antiinflammatory, decongestant and antiallergic agents for the topical treatment of rhinitis and/or sinusitis.

One of the advantages of the inhalatory route over the systemic one is the possibility of delivering the drug directly at the action site, so avoiding any systemic side-effects. Said way of administration allows to achieve a more rapid clinical response and a higher therapeutic index.

Among the different classes of drugs which are usually administered by inhalation for the treatment of respiratory diseases, glucocorticosteroids such as beclomethasone dipropionate (BDP), dexamethasone, flunisolide, budesonide, fluticasone propionate are of great importance. They can be administered in the form of a finely divided, i.e. micronised, powder, formulated as suspension in an aqueous phase containing any necessary surfactants and/or cosolvents; when intended to be administered in the form of metered doses of aerosol spray, they should also contain a low-boiling propellant.

The effectiveness of the administration form depends on the deposition of an adequate amount of particles at the action site. One of most critical parameters determining the proportion of inhalable drug which will reach the lower respiratory tract of a patient is the size of the particles emerging from the device. In order to ensure an effective penetration into the bronchioli and alveoli and hence ensure a high respirable fraction, the mean aerodynamic diameter (MMAD) of the particles should be lower than 5-6 microns (.mu.m). For nasal administration, particles with higher MMAD are required.

Other important characteristics for a correct administration and therefore for the therapeutic efficacy, are the size distribution and the homogeneous dispersion of the particles in the suspension.

A poor control of said parameters might favour the formation of loose agglomerates (curds) or, if the curds become compacted and fuse, cakes of suspended particles which, in turn, may impair the possibility of re-suspending the product easily and providing uniform dosing either during the filling of the containers and during the use.

The first object of the present invention is to provide a process for the preparation of particles suspensions for use in pharmaceutical formulations for aerosol inhalation, said particles being characterised by optimised particle size and distribution for obtaining compositions with high therapeutic efficacy.

In a first embodiment of the invention, the process is carried out by using a turboemulsifier, optionally followed by a treatment with a high pressure homogeniser.

Accordingly, said process includes a first step wherein an aqueous solution which constitutes the carrier is dispersed in a turboemulsifier apparatus. A typical turboemulsifier suitable for the treatment comprises a containment vessel equipped with magnetic stirring and a high potency turbine system which is used for homogenising the suspension. The apparatus can also be fitted with a heating steam jacket as well as a vacuum system.

The carrier optionally contains wetting agents, surfactants, viscosity-increasing agents, preservatives, stabilising agents, isotonicity agents and/or buffers and can optionally be sterilised. In a second step, one or more micronised active ingredients, obtained after conventional milling, are added to the aqueous phase and dispersed in the same turboemulsifier vessel by applying very high speed (2000-3000 r.p.m., preferably 2500-2600) for 15-20 min. In has been found that said conditions are necessary in order to effectively disperse the micronised particles of the active ingredient in such a way as to prevent agglomeration during storage. Moreover, it has been more surprisingly found that the particles during said treatment are subjected to a further mild milling which reduces the sizes of the crystals of larger diameter so removing the fractions with higher particle size distribution.

Optionally the process can be carried out under vacuum in order to skim off the suspension.

In a more preferred embodiment of the invention, the drug, dispersed in the aqueous phase, is subjected to an additional homogenisation treatment under high-pressure to further reduce the mean size of the suspended particles. A typical apparatus used for this treatment, such as the Microfluidizer.RTM., includes a high pressure pump which can supply pressures up to 1500 bar and one or more interaction chambers. During the process, the sample is introduced as a stream, then forced at the operating pressure through the interaction chambers where the stream is accelerated to extremely high velocities and subjected to three main forces: i) shear (sliding of particles across one another, tearing); ii) impaction (collisions; crushing); iii) cavitation (collapsing of cavities or bubbles of the surrounding liquid phase; an increased change in velocity with a decreased change in pressure).

The degree of reduction of the solid particles size and the resulting distribution particle curve can be optimised by controlling the following variables i) the type and size of the interaction chamber; ii) the operating pressure; iii) the time of processing and the number of cycle the material is going through.

The effect of the process is also dependent on physico-chemical characteristics of the ingredient subjected to the treatment. According to the hardness of its crystalline lattice, different pressure and processing times can be requested to achieve the desired results.

It has now been found that, in case of steroids, it is possible to tighten the distribution particle curve in such a way as that the mean diameter of at least 90% of the particles is lower than or equal to 5 .mu.m by keeping the operating pressures between 500 and 1000 bar. In particular, particles optimised for pulmonary delivery are obtained using an interaction chamber with sharp edges and maintaining the operating pressure between 600 and 800 bar. Overprocessing at higher pressure should be avoided as it may result in particle-size growth and curds formation. Said surprising results were achieved by submitting the suspension to only one cycle of treatment and therefore for a very short period, making the process very convenient and attractive from an industrial point of view.

The process of the invention is efficiently carried out at room temperature which constitutes a considerable advantage in case of potentially thermolabile molecules such as steroids. On the other hand, the temperature does not significantly increase during the treatment. Furthermore, said specific range of pressures turned out to be suitable for reducing the particle size of the suspended active ingredient without requiring a significant increment in the amount of surfactants. It is general knowledge indeed that the total surface area of the active ingredient increases upon micronisation making sometimes necessary to change the formula of the suspension. Therefore, the breaking of the particles has to be controlled to the degree allowed by the chosen composition.

At the end of the treatment of the invention, particles of particle size distribution within well-defined parameters as well as a good dispersion of the suspended particles are obtained. The resulting formulation is physically stable and it can be easily re-suspended after at least one year of storage.

In order to prevent an increment in the viscosity of the suspension and the formation of even loose aggregates during storage which may puzzle the patient before the use, the process can be preferably carried out by operating at 600-700 bar and by employing an additional interaction chamber arranged in series with respect to the former.

The most widely experienced applications of high-pressure homogenisation regard solid-in-liquid dispersion of paint, pigments, ink-jet printing ink and ceramic powders.

WO 96/14925 deals with dispersion of hard, non-compliant particles used in magnetic recording media such as audio tapes, video tapes or computer diskettes.

Examples of applications to pharmaceutical compositions can be yet found in the prior art but none of them envisages treatment of steroids.

EP 768114 claims the use of said apparatus for treating aerosol formulation containing low-boiling components such as hydrofluoro-carbon alkanes (HFA's) at ambient temperatures. Homogenisation is achieved at 550-620 bar but after repeated cycles of treatment. Micronisation of the active ingredients exemplified i.e. ipratropium bromide and salbuterol sulfate is achieved only at very high pressures (about 1400 bar).

Also EP 726088 claims a process, consisting of re-circulation under high-pressure through multiple tiny openings in order to obtain homogeneously dispersed formulation containing liquefied propellants to be used in pressurised aerosol inhalers.

Illig et al. (Pharm Tech October 1996) in a study aiming at describing the advantages of Microfluidizer.RTM. processing over conventional milling treatments, applied such technology to produce suspensions of iodinated radiopaque materials with reduced particle size.

Calvor et al. (Pharm Dev Technol 3, 297-305, 1998) discloses the use of high-pressure homogenisation to produce nanoparticle formulation of polymers (less than 1 .mu.m and preferably 5-7 nm).

The suspensions prepared according to the process of the invention can be partitioned in suitable containers such as multi-dose or, preferably, single-dose systems for nebulisation, preformed or prepared with the "blow, fill and seal" technology, or pumps or systems for the rhinologic administration.

Both steps, involving respectively the turboemulsifier and the high-pressure homogeniser, can be carried out without any contact with atmosphere and are therefore compatible with working in sterile environment.

All the steps of the process can be carried out on an industrial scale.

The types of dispersion which can preferably benefit of such treatment are: i) sterile suspensions obtained as from a micronised sterile active ingredient; ii) suspensions obtained as from a micronised non-sterile active ingredient.

The process of the invention could also be advantageously utilised for: iii) suspensions obtained from a non-sterile ingredient in the form of non-micronised powder; iv) sterile formulations as a result of wet steam treatment of the bulk suspensions.

In fact, it has been more surprisingly found that particles of the desired particle size distribution can also be obtained by submitting the suspension containing the non-micronised active ingredient to the high-pressure homogenisation treatment. In particular, by applying operating pressures lower than those previously claimed, particles suitable for nasal delivery could be obtained. Said treatment might also be effective in restoring the desired particle size distribution after that unfavourable changes in their profile have occurred as a result of heat-sterilising processes. The latter methods may indeed lead to the formation of aggregates which will hardly de-aggregate into fine particles upon administration.

Drugs which can advantageously be used for preparing the suspensions according to the process of the invention include those steroids which are usually administered by inhalation for the treatment of respiratory diseases, such as beclometasone dipropionate, flunisolide, momethasone furoate, triamcinolone acetonide, dexamethasone, fluticasone propionate, budesonide and its epimers. The corresponding formulations can be prepared by dispersing the active ingredient(s) in an aqueous solution or in high-boiling organic solvents, such as alcohols. According to the particle size and particle distribution obtained, they can be used either for pulmonary or nasal delivery.

Moreover, the particles obtained with the process of the invention, suitably dried, can optionally be conditioned in pressurised dosed areosol inhalers. Suspensions in organic solvents can be directly distributed in containers for pressurised aerosols.

As reported above, the process of the invention is compatible with working under sterile conditions. Since sterility is a requirement more and more demanded for pharmaceutical formulations intended for nebulisation, it would be highly advantageous to provide aqueous suspensions of steroids to be delivered as sterile single-dose preparations. Said formulations allow to avoid the use of antimicrobials or preservatives which are extensively reported to be responsible of allergies and irritations of airways which, in turn, manifest by cough or bronchospasm.

It is therefore a second object of the invention to provide a process for the preparation of particles to be used as aqueous suspensions intended for aerosol inhalation, said particles being constituted of a sterile micronised active ingredient and characterised by an optimal size distribution for obtaining high therapeutic efficacy starting from.

Said process comprises the following steps: i) to prepare an aqueous solution, which constitutes the carrier and optionally containing wetting agents, surfactants, viscosity-increasing agents, stabilising agents, isotonicity agents and/or buffers, in a suitable turboemulsifier vessel; ii) to sterilise the aqueous base inside the same container; iii) to add, in a sterile environment, one or more active sterile micronised ingredients; iv) to disperse all the ingredients by using the same turboemulsifier.

The resulting suspension can be directly partitioned under sterile conditions, in plastic single-dose containers, pre-formed and sterilised by suitable treatments or produced in sterile by employing the "blow, fill and seal" technology.

Before packaging, the suspension can optionally be submitted to a further high-pressure homogenisation treatment, still carried out under sterile conditions.

A third object of the invention is a process for making therapeutically acceptable micronised BDP sterile as a result of gamma-ray irradiation.

The use of gamma irradiation for sterilising steroids has been already reported in the literature. However, data always refer to drugs in the form of powders, solutions, suspensions, creams or ointments; furthermore, even in the most favourable cases, a decrease of the content is often observed which do not conform with the current ICH (International Conference Harmonisation) requirements for pharmaceutical formulations or products intended for.

Hayes R et al. in J Pharm Pharmacol 32 (Suppl), 48P, 1980 compare the stability of powder BDP with respect to that of its solution in methanol or propylene glycol, solvents currently used for the preparation of creams. Cobalt (⁶⁰ Co), at doses of 1 to 4 Mrad is used as gamma-irradiating source. The conclusions are that BDP in the form of powder is stable immediately after irradiation while its solutions undergo quick degradation.

Bussey DM et al. in J Parent Sci Technol 37, 51-54, 1983 and Kane MP et al. in J Pharm Sci 72, 30-35, 1983 report data on the degradation of powder corticosteroids sterilised by using ⁶⁰ Co as irradiating source. The percentage of degradation varies from a minimum of 0.2%/Mrad for prednisone to a maximum of 1.4%/Mrad for hydrocortisone sodium succinate, The degradation following irradiation causes the loss of the C17 side chain and the oxidation of the alcohol group at the C11 position. Sterilisation of micronised steroids was reported in Illum L et al. in Arch Pharm Chemi Sci Ed. 2, 167-74, 1974. The active ingredients submitted to two different radiation doses (4.5 and 15 Mrad) showed different degradation degrees, namely below 1% for hydrocortisone acetate and prednisone and about 2.4% for hydrocortisone, prednisolone and prednisolone hydrate.

WO 99/25359 claims a process for sterilisation of a powdered form of a glucocorticosteroid, preferably budesonide, by employing temperatures (from 100 to 130^oC.) significantly lower than those considered necessary for the heat sterilisation of other substances.

PT-A-69652 disclosed cold sterilisation of micronized glucocorticosteroids using mixture of ethylene oxide and carbon dioxide. Specific examples are prednacinolone, dexamethasone, prednisolone and salts, esters and fluoro derivatives thereof. Sterile BDP is not reported. Furthermore, the technique requires the elimination of residual ethylene oxide which is time consuming and difficult. In the light of the present strict regulatory requirement the method would be not suitable for producing therapeutically acceptable glucocorticosteroids.

In summary, methods of sterilisation, in particular gamma-ray irradiation, has never been previously applied to micronised beclomethasone dipropionate (BDP). Moreover, the stability upon storage of the corresponding suspensions of the micronised irradiated product has never been verified. Degradation processes may indeed start after a significant lag-time due to the energy stored up by the drug after irradiation.

It has now surprisingly been found that BDP micronised substance when subjected to gamma-irradiation at 2 to 9 KGy under particular conditions, remains chemically stable. Contrary to what has been reported in WO 99/25359 for budesonide, no significant chemical degradation was observed with respect to the non-irradiated product. Sterile BDP micronised substance according to the process of the invention experiences any change neither in its crystalline characteristics, as demonstrated by DSC (Differential Scanning Calorimetry), TGA (Thermal Gravimetric Analysis), XRD (X-ray diffractometry), IR (infrared spectrum), nor in its particle size as proved by Malvern analysis. Also the corresponding suspensions turned out to be physically and chemically stable after long-term and accelerated storage conditions.

The process is carried out on the product packed in containers made of suitable materials, preferably polythene, after having replaced air by nitrogen, or optionally under vacuum; the containers are, in turn, sealed in bags made of oxygen-proof materials such as Polikem.RTM. or Co-pack.RTM..

It has indeed been found that the presence of oxygen during irradiation dramatically affects the stability of the product as the latter becomes more sensitive to oxidative processes. The ratio between the volume of the container and the amount of micronised powder should also be kept as low as possible and necessarily equal or less than 7:1 w/v.

The present process was validated according to the International Standard Organization Procedure ISO-11137-2B in order to ensure a Sterility Assurance Level (SAL) of at least 10^-6 (preferably 10^-7) and it yields a material sterile according the criteria of the European Pharmacopoeia (Ph.Eur).

The method of the invention allows to solve the technical problem of preparing micronised BDP sterile suspensions to be used for nebulisation. Sterilisation methods of the prior art carried out directly on the final formulation are indeed not suitable; aseptic filtration cannot be utilised due to non-filterability of suspended particles, while wet steam (autoclaving) involves a degree of heat which can be only tolerated by thermostable steroids. For instance, BDP suspensions subjected to a wet steam process under conditions similar to those reported in U.S. Pat. No. 3,962,430 (121^oC. for 15 minutes) undergo a remarkable decrease in the content in active ingredient (about 8-9%), with a corresponding significant increase in degradation products (about 10-11%).

The BDP starting material for the process has a bioburden of less than 100 CFU (colony forming units) per gram, preferably less tan 10 CFU per gram and is used in the form of micronised powder, particularly in the form of particles having a MMAD of less than 10 .mu.m, more preferably less than 5 .mu.m.

The corresponding formulation for inhalation can be advantageously used in the treatment of any allergic condition and/or inflammatory condition of the nose or lungs, such as asthma as well as of bronchopulmonary dysplasia either in hospital and domicilary setting.

Claim 1 of 20 Claims

What is claimed is:

1. A process for the preparation of an aerosol inhalable suspension of particles, comprising:

a) preparing a suspension of a steroid active ingredient, in a turboemulsifier provided with a turbine adapted for homogenising the suspension;

b) optionally subjecting the resulting suspension to a further treatment in a high pressure homogeniser,

thereby forming said aerosol inhalable suspension.

 

____________________________________________
If you want to learn more about this patent, please go directly to the U.S. Patent and Trademark Office Web site to access the full patent.