(12) Patent Application Publication (10) Pub. No.: US 2016/0000709 A1 MORTON (43) Pub

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(12) Patent Application Publication (10) Pub. No.: US 2016/0000709 A1 MORTON (43) Pub US 2016.000.0709A1 (19) United States (12) Patent Application Publication (10) Pub. No.: US 2016/0000709 A1 MORTON (43) Pub. Date: Jan. 7, 2016 (54) DRY POWDER INHALER FORMULATIONS A613 L/55 (2006.01) COMPRISING SURFACE-MODIFIED A6M I5/00 (2006.01) KS WITH ANT-ADHERENT A613 L/473 (2006.01) A613 L/35 (2006.01) (71) Applicant: VECTURA LIMITED, CHIPPENHAM A647/26 (2006.01) (GB) A647/12 (2006.01) 469/14 (2006.01) 72) Inventor: DAVID MORTON CHIPPENHAM (72) Inventor (GB) s A613 L/522 (2006.01) (52) U.S. Cl. (21) Appl. No.: 14/823,484 CPC ............... A61K 9/0075 (2013.01); A6IK 9/145 (2013.01); A61 K3I/58 (2013.01); A61 K3I/55 (22) Filed: Aug. 11, 2015 (2013.01); A61 K3I/522 (2013.01); A61 K Related U.S. Application Data 31/473 (2013.01); A61K 31/135 (2013.01); (63) Continuation of application No. 13/085,200, filed on A61K4726 (2013.01); A61K 47/12 (2013.01); Apr. 12, 2011, which is a continuation of application A61M 15/0028 (2013.01); A61M 2202/064 No. 1 1/791,385, filed on Jul. 5, 2007, now abandoned, (2013.01) filed as application No. PCT/GB05/50211 on Nov. 23, 2005. (57) ABSTRACT (30) Foreign Application Priority Data The present invention is concerned with a refinement of the processing of particles that are to form a dry powder formu Nov. 23, 2004 (GB) ................................... O425758.0 lation which is to be administered to the lung using a dry powder inhaler (DPI) device. In particular, the present inven Publication Classification tion provides the processing of particles of active material and (51) Int. Cl. particles of carrier material in the presence of additive mate A6 IK9/00 (2006.01) rial to provide a powder composition which exhibits excellent A6 IK3I/58 (2006.01) powder properties and which is economical to produce. Patent Application Publication Jan. 7, 2016 Sheet 1 of 7 US 2016/0000709 A1 Microporosity of lactose 100 80 s -- SOrbolaC 3.9. 60 -A-MF SOrbolac 40 ... Sorb/MgSt 98/2 -- Sorb/MgSt 95/5 20 O O 20 40 60 80 100 pore diameter (nm) Fig. 1 Patent Application Publication Jan. 7, 2016 Sheet 2 of 7 US 2016/0000709 A1 Patent Application Publication Jan. 7, 2016 Sheet 3 of 7 US 2016/0000709 A1 Patent Application Publication Jan. 7, 2016 Sheet 4 of 7 US 2016/0000709 A1 9 L # eº|| Patent Application Publication Jan. 7, 2016 Sheet 5 of 7 US 2016/0000709 A1 Patent Application Publication Jan. 7, 2016 Sheet 6 of 7 US 2016/0000709 A1 pasniq +900AS :66)3SõJN Patent Application Publication Jan. 7, 2016 Sheet 7 of 7 US 2016/0000709 A1 =Alpeg ·~~~~);0:02 A 2 US 2016/0000709 A1 Jan. 7, 2016 DRY POWDER INHALER FORMULATIONS 0008 FIG. 3, also noted as Table 2, shows the Hosokawa COMPRISING SURFACE-MODIFIED Powder Tester Results for Extra Fine Lactose. PARTICLES WITH ANT-ADHERENT 0009 FIG. 4, also noted as Table 3, shows the Hosokawa ADDITIVES Powder Tester Results for Sorbolac 400 (Cyclomixed). 0010 FIG. 5, also noted as Table 4, shows the Hosokawa RELATED APPLICATIONS Powder Tester Results for Micronised Lactose (Model Drug). 0001. This application is a continuation of U.S. applica 0011 FIG. 6, also noted as Table 5, shows the Hosokawa tion Ser. No. 13/085,200 filed Apr. 12, 2011, which is a Powder Tester Results for SU003 (Conventional “Large” Car continuation of U.S. application Ser. No. 1 1/791,385 filed Jul. rier). 5, 2007, now abandoned which is a United States national 0012 FIG. 7 shows the Zeta potential of Lactose. Lactose/ stage of International Application No. PCT/GB2005/0502.11, Magnesium Stearate that has been Turbula-blended and Lac filed Nov. 23, 2005, which was published as International tose/Magnesium Stearate that has been mechanofused. Publication No. WO 2006/056812, and which claims benefit of United Kingdom Application No. 0425758.0 filed, Nov. DETAILED DESCRIPTION OF THE INVENTION 23, 2004, the entire contents of which are hereby expressly 0013 The drug particles or particles of pharmaceutically incorporated herein by reference thereto. active material (also referred to herein as “active' particles) in the resuspended powder must aerosolise into an ultra-fine FIELD OF THE INVENTION aerosol so that they can be transported to the appropriate target area within the lung. Typically, for lung deposition, the 0002 The present invention is concerned with a refine active particles have a diameter of less than 10 Jums, fre ment of the processing of particles that are to form a dry quently 0.1 to 7 um, 0.1 to 5um, or 0.5 to 5 um. powder formulation which is to be administered to the lung, 0014 For formulations to reach the deep lung or the blood for example using a dry powder inhaler (DPI) device. In stream via inhalation, the active agent in the formulation must particular, the present invention provides the processing of be in the form of very fine particles, for example, having a particles of active material and particles of carrier material in mass median aerodynamic diameter (MMAD) of less than 10 the presence of additive material to provide a powder com um. It is well established that particles having an MMAD of position which exhibits excellent powder properties and greater than 10 um are likely to impact on the walls of the which is economical to produce. throat and generally do not reach the lung. Particles having an MMAD in the region of 5 to 2 um will generally be deposited BACKGROUND OF THE INVENTION in the respiratory bronchioles whereas particles having an 0003. Inhalation represents a very attractive, rapid and MMAD in the range of 3 to 0.05um are likely to be deposited patient-friendly route for the delivery of systemically acting in the alveoli and to be absorbed into the bloodstream. drugs, as well as for drugs that are designed to act locally on (0015 Preferably, for delivery to the lower respiratory tract the lungs themselves. It is particularly desirable and advan or deep lung, the MMAD of the active particles is not more tageous to develop technologies for delivering drugs to the than 10 um, and preferably not more than more preferably not lungs in a predictable and reproducible manner. more than 3 Jum, and may be less than 2 Jum, less than 1.5um 0004. The key features which make inhalation an exciting or less than 1 Jum. Especially for deep lung or systemic deliv drug delivery route are: rapid speed of onset; improved ery, the active particles may have a size of 0.1 to 3 um or 0.1 patient acceptance and compliance for a non-invasive sys to 2 Jum. temic route; reduction of side effects; product life cycle 0016. Ideally, at least 90% by weight of the active particles extension; improved consistency of delivery; access to new in a dry powder formulation should have an aerodynamic forms of therapy, including higher doses, greater efficiency diameter of not more than 10 um, preferably not more than 5 and accuracy of targeting; and direct targeting of the site of um, more preferably not more than 3 um, not more than 2.5 action for locally administered drugs, such as those used to um, not more than 2.0 um, not more than 1.5um, or even not treat lung diseases such as asthma, COPD, CF or lung infec more than 1.0 um. tions. 0017. When dry powders are produced using conventional 0005. However, the powder technology behind successful processes, the active particles will vary in size, and often this dry powders and DPI products remains a significant technical variation can be considerable. This can make it difficult to hurdle to those wishing to succeed with this route of admin ensure that a high enough proportion of the active particles istration and to exploit the significant product opportunities. are of the appropriate size for administration to the correct Any formulation must have suitable flow properties, not only site. It is therefore desirable to have a dry powderformulation to assist in the manufacture and metering of the powders, but wherein the size distribution of the active particles is as nar also to provide reliable and predictable resuspension and row as possible. For example, the geometric standard devia fluidisation, and to avoid excessive retention of the powder tion of the active particle aerodynamic or Volumetric size within the dispensing device. distribution (Og), is preferably not more than 2, more prefer ably not more than 1.8, not more than 1.6, not more than 1.5, not more than 1.4, or even not more than 1.2. This will BRIEF DESCRIPTION OF THE DRAWINGS improve dose efficiency and reproducibility. 0006 FIG. 1 shows the microporosity of various types of 0018 Fine particles, that is, those with an MMAD of less lactose particles as measured using the Cooker SA 3100 BET than 101. Lum and Smaller, tend to be increasingly thermody system as defined by pore diameter (nm) versus cumulative namically unstable as their surface area to Volume ratio percentage. increases, which provides an increasing Surface free energy 0007 FIG. 2, also noted as Table 1, shows the Hosokawa with this decreasing particle size, and consequently increases Powder Tester Results for Sorbolac 400 (Mechanofused). the tendency of particles to agglomerate and the strength of US 2016/0000709 A1 Jan. 7, 2016 the agglomerate. In the inhaler, agglomeration of fine par collisions it employs. Such variations can lead to increased ticles and adherence of such particles to the walls of the Surface energy and increased cohesiveness and adhesiveness.
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