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Title: Mometasone furoate suspensions for nebulization United States Patent: 6,187,765 Inventors: Harris; David (New Providence, NJ); Sequeira; Joel A. (Edison, NJ); Chaudry; Imtiaz A. (North Caldwell, NJ)Assignee: Schering Corporation (Kenilworth, NJ) Appl. No.: 167512Filed: October 6, 1998 An aqueous nebulizer suspension contains water, mometasone furoate monohydrate, a nonionic surfactant, a soluble salt and optionally a pH buffer. The suspension may be prepared by ultrasonication or jet milling techniques. DETAILED DESCRIPTION OF THE INVENTION Percentages expressed herein are meant to indicate percent
by weight, unless the context clearly dictates otherwise. Polysorbate Acid Moles EtO
20 Lauric 20
21 Lauric 4
40 Palmitic 20
60 Stearic 20
61 Stearic 4
65* Stearic 20
80 Oleic 20
81 Oleic 5
85* Oleic 20
In general, Polysorbate surfactants will be present in a formulation at about 50 to 500 .mu.g/mL. When the surfactant concentration is below about 20 .mu.g/mL, the particles tend to form cakes which are not easily redispersed. Useful surfactants also include the "Poloxamers," which are block polymers of polyoxyethylene and polyoxypropylene, generally corresponding to the following formula: HO(CH2 CH2 O)x [CH(CH3)CH2 O]y (CH2 CH2 O)z H Representative commercially available poloxamer surfactants are listed in the following table, wherein the CTFA designation (Poloxamer number) and average values of x, y and z are given. Poloxamer x y z
101 2 16 2
105 11 16 11
108 46 16 46
122 5 21 5
123 7 21 7
124 11 21 11
181 3 30 3
182 8 30 8
183 10 30 10
184 13 30 13
185 19 30 19
188 75 30 75
212 8 35 8
215 24 35 24
217 52 35 52
231 6 39 6
234 22 39 22
235 27 39 27
237 62 39 62
238 97 39 97
282 10 47 10
284 21 47 21
288 122 47 122
331 7 54 7
333 20 54 20
334 31 54 31
335 38 54 38
338 128 54 128
401 6 67 6
402 13 67 13
403 21 67 21
407 98 67 98
Poloxamer surfactants are used at concentrations similar to those for the Polysorbates, although certain members are useful at concentrations up to about 1 mg/mL. In general, the chosen surfactant should not materially increase the viscosity of the suspension formulation, since the efficiency of the nebulization process is particularly sensitive to viscosity. Many nonionic surfactants are useful for preparing inhalation and/or injectable drug formulations, and any of these should be suitable for use in the present invention. The formulations further include a soluble salt. This salt performs at least two functions: it minimizes the effects of the inhaled formulation on the normal cell fluid balance of airway cells and also stabilizes the suspension of medicament. For the first function, it is preferred to use sufficient salt concentrations to render the formulation isotonic; sodium chloride and potassium chloride are preferred for this purpose. It has been found that adequate suspension stability is produced by isotonic concentrations (i.e., about 0.9 weight percent) of sodium chloride, although concentrations about 0.2 to about 2 weight percent are useful. Any physiologically compatible alkali metal or alkaline earth metal soluble salt can be used in the present invention. Optionally, the formulations will contain a pH buffer, to maintain the formulation pH between about 3 and about 7. It has been found that stability of the drug (as measured by the absence of degradation reaction products) in suspension is improved by maintaining pH conditions below about 6. For reasons of tissue compatibility, excessively acidic products are not desired, so the pH should not be made to be below about 3. Some experimentation may be needed to qualify specific buffers for use in the invention: phosphate buffers in concentrations of 1 to 50 millimolar do not appear to adequately prevent caking of the particulates in the suspension when there is no added soluble salt. A citrate-citric acid buffer, maintaining pH between about 4 and about 5, has been used with particularly good effect for both maintaining pH during storage and preventing any particulate caking in the absence of soluble salts. The citrate-citric acid buffer may be present in suspension formulations at concentrations at least about 2 and up to about 50 millimolar. While the literature has some reports of cough being induced by such buffer systems, this seems to occur primarily at the 150-200 millimolar level, although one report attributed cough to only a 35 millimolar concentration. Sterility or adequate antimicrobial preservation of the final packaged formulation is needed for patient protection. The use of antimicrobial preservatives is less desirable, since certain of these have been associated with adverse clinical effects, such as bronchospasm. Alternative processes which may be considered for achieving sterility usually will not include sterilization steps for the micronized drug substance or formulation, since it has been found that the drug undergoes degradation under the influence of gamma-ray irradiation and sterilizing heat conditions. Sterilization by filtration ordinarily will not be feasible, due to the suspension nature of the formulation. Thus, it is preferred to produce the mometasone furoate monohydrate under sterile conditions, conduct the drug micronization in a sterile environment, and perform a sterile packaging operation. Methods are known for reducing particle sizes into the micrometer range, including mechanical milling, application of ultrasonic energy and other techniques. Mechanical milling frequently generates high surface temperatures on the particles, and this is undesirable for mometasone furoate monohydrate which tends to lose some part of its hydration under the influence of high temperatures. Ultrasonic techniques are quite slow in their action, generally requiring very long processing times, but are capable of producing acceptable suspensions. Suspensions of drug particles can rapidly undergo particulate size reduction when subjected to "jet milling" (high pressure particle in liquid milling) techniques. A presently preferred jet milling procedure for producing the formulations of the invention involves the use of the "Microfluidizer" system sold by Microfluidics International Corporation of Newton, Mass., U.S.A. This device divides a fluid stream, flowing under high pressures (up to about 40,000 pounds per square inch, or 2.76 x 108 newton/meter2), between two separate microchannel paths and then recombines them from generally perpendicular directions to create very high shear, impact and cavitation forces. By continuously recirculating suspensions through the system for a predetermined time period, it is possible to reproducibly create desired distributions of micron- and submicron-sized particles. Since the particles are always completely surrounded by liquid, their surfaces will not develop high temperatures under the influence of the size reduction forces, and the hydration water in the drug crystals will remain intact. Other useful equipment which utilizes related technology is available from Avestin Inc., Ottawa, Ontario, Canada. Claim 1 of 21 Claims What is claimed is:
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