Ionizable cationic lipids
US-2024383841-A1 · Nov 21, 2024 · US
US2016324792A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016324792-A1 |
| Application number | US-201615152835-A |
| Country | US |
| Kind code | A1 |
| Filing date | May 12, 2016 |
| Priority date | Oct 11, 2011 |
| Publication date | Nov 10, 2016 |
| Grant date | — |
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Crystalline microparticles consisting of a phenylalkylamino beta 2 -adrenergic agonist coated with a C12-C20 fatty acid are useful for the preparation of pharmaceutical aerosol formulations in form of suspension in a liquefied propellant gas or powder formulations.
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1 - 11 . (canceled) 12 . A process for preparing chemically stable crystalline microparticles, comprising a beta 2 -adrenergic agonist selected from the group consisting of formoterol, a pharmaceutically acceptable salt of formoterol, indacaterol, and a pharmaceutically acceptable salt of indacaterol, coated with at least one C12-C20 fatty acid in an amount of 0.5 to 2.0% by weight based on a total weight of the crystalline microparticles, the process comprising: (a) preparing a solution of the C12-C20 fatty acid in a fluorinated model propellant in which the beta 2 -agonist is substantially insoluble, selected from the group consisting of perfluoropentane, 2H,3H-perfluoropentane (HPFP), perfluorohexane, and 1H-perfluorohexane; (b) adding the beta 2 -agonist as a micronized powder to said solution of the fatty acid, to obtain a mixture; (c) mixing the mixture to obtain a homogeneous suspension; and (d) subjecting the suspension to spray-drying, to obtain the coated microparticles; wherein the fatty acid forms a continuous film on a surface of the microparticles. 13 . The process according to claim 12 , wherein the fluorinated model propellant is 2H,3H-perfluoropentane (HPFP). 14 - 16 . (canceled) 17 . The process according to claim 12 , wherein the beta 2 -adrenergic agonist is formoterol. 18 . The process according to claim 17 , wherein the fluorinated model propellant is 2H,3H-perfluoropentane (HPFP). 19 . The process according to claim 17 , wherein: the C14-C20 saturated fatty acid is myristic acid; and the myristic acid is present in an amount of 1.0 to 2.0% by weight based on the total weight of the crystalline microparticles. 20 . The process according to claim 17 , further comprising: preparing a pharmaceutical aerosol formulation comprising the coated microparticles in suspension in a liquefied propellant gas; and filling the pharmaceutical aerosol formulation into a pressurized metered dose inhaler. 21 . The process according to claim 20 , wherein the liquefied propellant gas is 1,1,1,2,3,3,3-heptafluoro-n-propane (HFA227) or 1,1,1,2-tetrafluoroethane (HFA 134a), or a mixture thereof. 22 . The process according to claim 20 , wherein the formulation, upon storage, meets the requirements of EMEA Guideline CPMP/QWP/122/02. 23 . The process according to claim 17 , further comprising preparing a dry powder pharmaceutical formulation comprising the coated microparticles. 24 . The process according to claim 12 , wherein the beta2-adrenergic agonist is a fumarate dihydrate salt of formoterol. 25 . The process according to claim 24 , wherein the fluorinated model propellant is 2H,3H-perfluoropentane (HPFP). 26 . The process according to claim 24 , wherein: the C14-C20 saturated fatty acid is myristic acid; and the myristic acid is present in an amount of 1.0 to 2.0% by weight based on the total weight of the crystalline microparticles. 27 . The process according to claim 24 , further comprising: preparing a pharmaceutical aerosol formulation comprising the coated microparticles in suspension in a liquefied propellant gas; and filling the pharmaceutical aerosol formulation into a pressurized metered dose inhaler. 28 . The process according to claim 27 , wherein the liquefied propellant gas is 1,1,1,2,3,3,3-heptafluoro-n-propane (HFA227) or 1,1,1,2-tetrafluoroethane (HFA 134a), or a mixture thereof. 29 . The process according to claim 27 , wherein the formulation, upon storage, meets the requirements of EMEA Guideline CPMP/QWP/122/02. 30 . The process according to claim 24 , further comprising preparing a dry powder pharmaceutical formulation comprising the coated microparticles. 31 . The process according to claim 12 , wherein the beta 2 -adrenergic agonist is indacaterol. 32 . The process according to claim 31 , wherein the fluorinated model propellant is 2H,3H-perfluoropentane (HPFP). 33 . The process according to claim 31 , wherein: the C14-C20 saturated fatty acid is myristic acid; and the myristic acid is present in an amount of 1.0 to 2.0% by weight based on the total weight of the crystalline microparticles. 34 . The process according to claim 31 , further comprising: preparing a pharmaceutical aerosol formulation comprising the coated microparticles in suspension in a liquefied propellant gas; and filling the pharmaceutical aerosol formulation into a pressurized metered dose inhaler. 35 . The process according to claim 34 , wherein the liquefied propellant gas is 1,1,1,2,3,3,3-heptafluoro-n-propane (HFA227) or 1,1,1,2-tetrafluoroethane (HFA 134a), or a mixture thereof. 36 . The process according to claim 34 , wherein the formulation, upon storage, meets the requirements of EMEA Guideline CPMP/QWP/122/02. 37 . The process according to claim 31 , further comprising preparing a dry powder pharmaceutical formulation comprising the coated microparticles. 38 . The process according to claim 12 , wherein the beta 2 -adrenergic agonist is a maleate salt of indacaterol. 39 . The process according to claim 38 , wherein the fluorinated model propellant is 2H,3H-perfluoropentane (HPFP). 40 . The process according to claim 38 , wherein: the C14-C20 saturated fatty acid is myristic acid; and the myristic acid is present in an amount of 1.0 to 2.0% by weight based on the total weight of the crystalline microparticles. 41 . The process according to claim 38 , further comprising: preparing a pharmaceutical aerosol formulation comprising the coated microparticles in suspension in a liquefied propellant gas; and filling the pharmaceutical aerosol formulation into a pressurized metered dose inhaler. 42 . The process according to claim 41 , wherein the liquefied propellant gas is 1,1,1,2,3,3,3-heptafluoro-n-propane (HFA227) or 1,1,1,2-tetrafluoroethane (HFA 134a), or a mixture thereof. 43 . The process according to claim 41 , wherein the formulation, upon storage, meets the requirements of EMEA Guideline CPMP/QWP/122/02. 44 . The process according to claim 38 , further comprising preparing a dry powder pharmaceutical formulation comprising the coated microparticles.
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