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WO2000033789A2 - Inhalation powders - Google Patents

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Publication number
WO2000033789A2
WO2000033789A2 PCT/US1999/028608 US9928608W WO0033789A2 WO 2000033789 A2 WO2000033789 A2 WO 2000033789A2 US 9928608 W US9928608 W US 9928608W WO 0033789 A2 WO0033789 A2 WO 0033789A2
Authority
WO
WIPO (PCT)
Prior art keywords
weight
fraction
excipient powder
particle size
excipient
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/US1999/028608
Other languages
French (fr)
Other versions
WO2000033789A3 (en
Inventor
Jonathan Kenneth Embleton
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Catalent Pharma Solutions Inc
Original Assignee
Catalent Pharma Solutions Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Catalent Pharma Solutions Inc filed Critical Catalent Pharma Solutions Inc
Priority to AU20383/00A priority Critical patent/AU2038300A/en
Publication of WO2000033789A2 publication Critical patent/WO2000033789A2/en
Publication of WO2000033789A3 publication Critical patent/WO2000033789A3/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/0012Galenical forms characterised by the site of application
    • A61K9/007Pulmonary tract; Aromatherapy
    • A61K9/0073Sprays or powders for inhalation; Aerolised or nebulised preparations generated by other means than thermal energy
    • A61K9/0075Sprays or powders for inhalation; Aerolised or nebulised preparations generated by other means than thermal energy for inhalation via a dry powder inhaler [DPI], e.g. comprising micronized drug mixed with lactose carrier particles

Definitions

  • This invention relates to inhalable drugs in particulate form and the use thereof. Particularly, it is concerned with excipient powders which are mixed with such drugs to facilitate handling and metering, and maximising the delivery of inspired drug to target sites in the lungs.
  • Inhalable drugs are typically provided in micronised form with average
  • the particulate drug is mixed with an excipient powder
  • Boehringer Ingelheim International GmbH describe an excipient powder for use with an inhalable micronised drug which has coarser and finer fractions.
  • the coarser fraction has an
  • the finer fraction has an average particle size of at least 20 ⁇ m.
  • the finer fraction has an average particle size
  • the amount of drug that reaches the lungs can be controlled, without losing the benefits that are afforded by the use of the larger excipient particles, particularly the flowability of the mixture of excipient and inhalable drug, and the metering of doses therefrom.
  • inhalable pharmaceutical powder compositions can be further enhanced by the careful selection of coarse and fine fractions in the excipient powder, and by the use of a ternary particulate agent in the mixture. Firstly, we have found that some benefits can be achieved by excluding from the excipient mixture particles having an intermediate size, i.e., neither coarse
  • coarse particles of at least 30 ⁇ m, preferably at least 50 ⁇ m
  • particles of no more than lO ⁇ m are effective in enhancing the delivery of drug to
  • the intermediate sized particles between 10 and 30 ⁇ m
  • an excipient powder consisting of two discrete fractions, and excluding particles of intermediate size, can offer considerably improved performance in combination with a particulate, normally micronised, drug. It will, though, be appreciated that it may be impossible to wholly exclude intermediate sized particles from the excipient mixture; the benefits of this aspect of the invention will also be apparent even when the proportion of intermediate sized particles is substantially reduced.
  • a typical excipient powder according to the invention comprises a coarse first
  • powder fractions with the requisite particle size ranges can be accomplished by sieving out the particles to be included or mixing pre-classified powders; i.e., powders in which the particle size range is already accurately defined. Mixing will normally be by high sheer blending.
  • Pre-classified coarse powders are available as staple products, for example a lactose powder of which at least 80% by
  • weight has a particle size of at least 50 ⁇ m is available under the Trade Mark Meggle
  • Effectively pre-classified fine powder fractions can be prepared by micronisation or spray drying.
  • the fine fraction and, where used, the ternary agent will be provided in the smallest possible particle sizes.
  • a ternary agent can also enhance the delivery of particulate drug to target sites in the lungs.
  • a ternary agent would be provided in particulate form as an additional fine fraction, but slightly larger particle sizes are acceptable.
  • Suitable ternary agents include a wide range of water-soluble and physiologically acceptable materials, but will normally be water surface active agents or amino acids, peptides and polypeptides or derivatives thereof.
  • a particularly preferred ternary agent is L-leucine.
  • Typical carrier powders embodying the invention excluding drug or any ternary agent, have the following particle size analysis by weight: Size BanD ( ⁇ m) ⁇ 10 10-30 30-50 10-50 50-100 >100 Total
  • the particle size distribution in powders useful in the practice of the invention can be established using a Malvern Mastersizer, a proprietary product available from
  • flavour-enhancers and anti-oxidants can be included in powders according to the invention. Primarily, such additional components would have the purpose of rendering the powder and drug mixture more palatable, and/or more stable.
  • a typical excipient powder according to the invention for use with an inhalable particulate drug comprises a coarse first fraction of which at least 90% by
  • weight has a particle size of at least lO ⁇ m and/or at least 80%> by weight has a particle
  • the first and second fractions will often consist of the same material, such as sugar, e.g., mono, di, or polysaacharide, typically lactose.
  • the proportions by weight of the first fraction to the second fraction will normally be in the range 50:1 to 2:1, preferably 20:1 to 3:1, and most preferably 10:1 to 4:1.
  • the ratio by weight of the first and second fractions to the third fraction is normally in the range 1000:1 to 10:1, typically 400:1 to 25: 1 and preferably 200:1 to 50:1.
  • the amount of drug included in an inhalable pharmaceutical composition of the kind to which the invention relates is normally relatively small. Typically the ratio by weight of excipient powder to drug is as high as 1000:1.
  • ratio of excipient to drug can be as low as 1 :1.
  • Preferred ratios are in the range 500:1 to 3:1, with the most preferred ratios being in the range 200:1 to 10:1.
  • the carrier formulations were each blended with 2% of a corticosteroid, commonly used for the prophylactic treatment of asthma, in a high-shear blender.
  • Fine lactose >90% by mass below lO ⁇ m in size
  • Fine L-leucine >90% by mass below lO ⁇ m in size
  • Coarse lactose >80% by mass over 50 ⁇ m in size
  • Fine lactose >90% by mass below lO ⁇ m in size
  • the carrier formulations were each blended with 1.5% of a cortico steroid in a high-shear blender. A small sample of each drug blend was then filled into a separate reservoir- type inhaler device and its aerosol performance assessed using the MSLI.
  • the mean RF (from three determinations) using the drug blend containing 2% ternary agent was approximately 67%, compared to a value of only 63% for the formulation with 1%> L-leucine.
  • the respirable fraction (RF) was calculated at a flow rate of 60 litres per minute by dividing the fine particle dose or amount of drug found in the lower stages in the impinger, by the emitted dose or total mass of drug recovered from the impinger as a whole.
  • Example 1 demonstrates the considerable improvement in the respirable fraction achieved by the use of the specified ternary agent.
  • Example 2 shows that this benefit is enhanced by the use of additional amounts of the ternary agent.

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  • Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Medicinal Chemistry (AREA)
  • Pulmonology (AREA)
  • Chemical & Material Sciences (AREA)
  • Otolaryngology (AREA)
  • Pharmacology & Pharmacy (AREA)
  • Epidemiology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Animal Behavior & Ethology (AREA)
  • General Health & Medical Sciences (AREA)
  • Public Health (AREA)
  • Veterinary Medicine (AREA)
  • Medicinal Preparation (AREA)

Abstract

The present invention relates to inhalable drugs in particulate form. More specifically, the present invention is directed to an excipient powder that comprises a coarse first fraction having a particle size of 10νm, a fine second fraction having a particle size of no more than 10νm and a third fraction consisting of ternary agents. The excipient powder has been found to be beneficial in the administration of phamarceuticals to the pulmonary system.

Description

INHALATION POWDERS
This invention relates to inhalable drugs in particulate form and the use thereof. Particularly, it is concerned with excipient powders which are mixed with such drugs to facilitate handling and metering, and maximising the delivery of inspired drug to target sites in the lungs.
Inhalable drugs are typically provided in micronised form with average
particle sizes of up to 10 μm. The particulate drug is mixed with an excipient powder
of larger average particle size, and the drug particles become attached to the excipient or carrier particles to create a generally homogeneous mixture. The larger particle size of the excipient results in the powder mixture being flowable, and the homogeneity of the mixture enables it to be metered into accurately measurable doses. This is of particular importance when only very small quantities of the drug are required in a dose. Dilution of the drug in the excipient does, of course, facilitate accurate metering. Excipient powders of this kind and pharmaceutical powder compositions for inhalation utilising such excipients are described in British Patent Specification No. 1,242,211.
When an inhalation powder of the kind referred to above is inspired, the drug particles detach themselves from the larger carrier particles which, by virtue of their own momentum, are effectively separated from the inflowing air. The smaller drug particles remain in train, and are carried to the lungs. Effective particle sizes for the excipient or carrier powder has been the subject of considerable research. In his Thesis No. DX 187842 published at the University of London Library in August 1991, Nuha M. Kassem examines the effect of using different sized excipients on the extent to which a drug carried thereby penetrates the lungs, and thereby reaches the target sites. He conducted experiments using a multistage impinger to simulate the inhalation process, with different sizes of carrier
particles, ranging from below lOμm to over 180μm. He also included an experiment
using an excipient powder in which the particle size was not predetermined, but rather
broad and comprised of particles below lOμm and up to and over 80μm, reaching the
conclusion that the performance of this unclassified powder combines the performance of different ranges of particle sizes inherent in such a powder.
In their European Patent Specification No. 0,663,815 Boehringer Ingelheim International GmbH describe an excipient powder for use with an inhalable micronised drug which has coarser and finer fractions. The coarser fraction has an
average particle size of at least 20μm. The finer fraction has an average particle size
of no more than lOμm. By specifically including a finer fraction in the excipient
powder, it is stated that the amount of drug that reaches the lungs can be controlled, without losing the benefits that are afforded by the use of the larger excipient particles, particularly the flowability of the mixture of excipient and inhalable drug, and the metering of doses therefrom.
We have found that the performance of inhalable pharmaceutical powder compositions can be further enhanced by the careful selection of coarse and fine fractions in the excipient powder, and by the use of a ternary particulate agent in the mixture. Firstly, we have found that some benefits can be achieved by excluding from the excipient mixture particles having an intermediate size, i.e., neither coarse
nor fme. For example, coarse particles of at least 30μm, preferably at least 50μm,
have a clearly beneficial effect on handleability of the powder mixture, and fine
particles of no more than lOμm are effective in enhancing the delivery of drug to
target sites in the lungs. The intermediate sized particles, between 10 and 30μm
(preferably lOμm to 50μm), tend to have an adverse affect on handleability without
imparting any benefit to the drug delivery characteristics. Thus, an excipient powder consisting of two discrete fractions, and excluding particles of intermediate size, can offer considerably improved performance in combination with a particulate, normally micronised, drug. It will, though, be appreciated that it may be impossible to wholly exclude intermediate sized particles from the excipient mixture; the benefits of this aspect of the invention will also be apparent even when the proportion of intermediate sized particles is substantially reduced.
A typical excipient powder according to the invention comprises a coarse first
fraction of which at least 80% by weight has a particle size of at least lOμm; a fine
second fraction of which at least 90% by weight has a particle size of nor more than
lOμm; and a third fraction consisting of a ternary agent. Preferably, no more than
15%, and most preferably no more than 10% by weight of the coarse fraction has a
particle size of less than lOμm. The preparation of powder fractions with the requisite particle size ranges can be accomplished by sieving out the particles to be included or mixing pre-classified powders; i.e., powders in which the particle size range is already accurately defined. Mixing will normally be by high sheer blending. Pre-classified coarse powders are available as staple products, for example a lactose powder of which at least 80% by
weight has a particle size of at least 50μm is available under the Trade Mark Meggle
Spherolac 100.
Effectively pre-classified fine powder fractions can be prepared by micronisation or spray drying. In all embodiments of the invention the fine fraction and, where used, the ternary agent, will be provided in the smallest possible particle sizes.
In a second aspect, we have found that the use of a ternary agent can also enhance the delivery of particulate drug to target sites in the lungs. Such a ternary agent would be provided in particulate form as an additional fine fraction, but slightly larger particle sizes are acceptable. Suitable ternary agents include a wide range of water-soluble and physiologically acceptable materials, but will normally be water surface active agents or amino acids, peptides and polypeptides or derivatives thereof. A particularly preferred ternary agent is L-leucine.
Typical carrier powders embodying the invention, excluding drug or any ternary agent, have the following particle size analysis by weight: Size BanD (μm) <10 10-30 30-50 10-50 50-100 >100 Total
I 18.62 3.25 3.31 6.55 27.14 47.69 100
II 27.58 2.95 2.94 5.39 24.09 42.44 100
III 36.55 2.65 2.56 5.21 21.04 37.2 100
The particle size distribution in powders useful in the practice of the invention can be established using a Malvern Mastersizer, a proprietary product available from
Malvern Instruments Limited, Malvern, U.K.
Additional components, such as flavour-enhancers and anti-oxidants, can be included in powders according to the invention. Primarily, such additional components would have the purpose of rendering the powder and drug mixture more palatable, and/or more stable.
A typical excipient powder according to the invention for use with an inhalable particulate drug comprises a coarse first fraction of which at least 90% by
weight has a particle size of at least lOμm and/or at least 80%> by weight has a particle
size of at least 50μm; a fine second fraction of which at least 90%0 by weight has a
particle size of no more than lOμm; and a third fraction consisting of a ternary agent
of which typically at least 90% by weight has a particle size of no more than 20μm.
The first and second fractions will often consist of the same material, such as sugar, e.g., mono, di, or polysaacharide, typically lactose. The proportions by weight of the first fraction to the second fraction will normally be in the range 50:1 to 2:1, preferably 20:1 to 3:1, and most preferably 10:1 to 4:1. The ratio by weight of the first and second fractions to the third fraction is normally in the range 1000:1 to 10:1, typically 400:1 to 25: 1 and preferably 200:1 to 50:1. The amount of drug included in an inhalable pharmaceutical composition of the kind to which the invention relates is normally relatively small. Typically the ratio by weight of excipient powder to drug is as high as 1000:1. However, certain drugs can be used in much larger quantities in excipients according to the invention, and the ratio of excipient to drug can be as low as 1 :1. Preferred ratios are in the range 500:1 to 3:1, with the most preferred ratios being in the range 200:1 to 10:1.
We have conducted some preliminary tests of formulations embodying the invention using an Astra Draco Multi-Stage Liquid Impinger (MSLI). The coarse lactose fraction in each case is Meggle SpheroLac 100. The fine fractions and L- leucine are prepared by micronisation. The results thereof are set out below.
Example 1
Two carrier formulations were prepared as follows:
Formulation A:
Coarse lactose (>80%> by mass over 50μm in size) = 89.0%
Fine lactose (>90% by mass below lOμm in size) = 10.0%>
Fine L-leucine (>90%> by mass below lOμm in size) = 1.0% Formulation B:
Coarse lactose (>80% by mass over 50μm in size) = 90.0%
Fine lactose (>90%o by mass below lOμm in size) = 10.0% The carrier formulations were each blended with 2% of a corticosteroid, commonly used for the prophylactic treatment of asthma, in a high-shear blender.
A small sample of each drug blend was then filled into a separate reservoir- type inhaler device and its aerosol performance assessed using the MSLI. The mean RF (Respirable Fraction) from three determinations using the drug blend containing ternary agent was approximately 60%, compared to a value of only approximately 40% for the formulation without L-leucine.
Example 2 Two carrier formulations were prepared as follows:
Formulation A:
Coarse lactose (>80% by mass over 50μm in size) = 78.0%
Fine lactose (>90% by mass below lOμm in size) = 20.0% Fine L-leucine (>90% by mass below lOμm in size) = 2.0%>
Formulation B :
Coarse lactose (>80% by mass over 50μm in size) = 79.0% Fine lactose (>90% by mass below lOμm in size) = 20.0%>
Fine L-leucine (>90% by mass below lOμm in size) = 1.0%
The carrier formulations were each blended with 1.5% of a cortico steroid in a high-shear blender. A small sample of each drug blend was then filled into a separate reservoir- type inhaler device and its aerosol performance assessed using the MSLI.
The mean RF (from three determinations) using the drug blend containing 2% ternary agent was approximately 67%, compared to a value of only 63% for the formulation with 1%> L-leucine. The respirable fraction (RF) was calculated at a flow rate of 60 litres per minute by dividing the fine particle dose or amount of drug found in the lower stages in the impinger, by the emitted dose or total mass of drug recovered from the impinger as a whole. Example 1 demonstrates the considerable improvement in the respirable fraction achieved by the use of the specified ternary agent. Example 2 shows that this benefit is enhanced by the use of additional amounts of the ternary agent.

Claims

CLAIMS:
1. An excipient powder for inhalable drugs comprising a coarse first
fraction of which at least 80% by weight has a particle size of at least lOμm; a fine
second fraction of which at least 90% by weight has a particle size of no more than
lOμm; and a third fraction consisting of a ternary agent.
2. An excipient powder according to Claim 1 wherein at least 90% by
weight of the ternary agent has a particle size of no more than 20μm.
3. An excipient powder according to Claim 1 or Claim 2 wherein at least
80% by weight of the coarse fraction has a particle size of at least 50μm.
4. An excipient powder according to any preceding claim wherein the first and second fractions consist of the same material.
5. An excipient powder according to claim 4 wherein the material is lactose.
6. An excipient powder according to any preceding claim wherein the ratio by weight of the first fraction to the second fraction is in the range 50:1 to 2:1, preferably 20:1 to 3:1; and most preferably 10:1 to 4:1.
7. An excipient powder according to any preceding claim wherein the ratio by weight of the first and second fractions to the third fraction is in the range 1000:1 to 10:1; preferably 400: 1 to 25:1; and most preferably 200:1 to 50:1.
8. An excipient powder according to any preceding claim wherein the ternary agent is a water-soluble surface active agent.
9. An excipient powder according to Claim 6 wherein the ternary agent is selected from Amino acids, peptides and polypeptides and derivatives thereof.
10. An excipient powder according to Claim 7 wherein the ternary agent is L-leucine.
11. An excipient powder according to any preceding claim wherein
particles in the size range lOμm to 30μm represent no more than 10% by weight of
the total excipient powder.
12. An excipient powder according to any preceding claim wherein
particles in the size range lOμm to 50μm represent no more than 10% by weight of
the total excipient powder.
13. An excipient powder for inhalable drugs comprising a coarse first
fraction of which at least 90%> by weight has a particle size of at least 30μm and a fine
second fraction of which at least 90% by weight has a particle size of no more than
lOμm, and particles in the size range lOμm to 30μm represent no more than 10%o by
weight of the total excipient powder.
14. An excipient powder for inhalable drugs comprising a coarse first
fraction of which at least 80% by weight has a particle size of at least 50μm and a fine
second fraction of which at least 90% by weight has a particle size of no more than
lOμm, and particles in the size range lOμm to 50μm represent no more than 20% by
weight of the total excipient powder.
15. An excipient powder according to Claim 14 wherein particles in the
size range lOμm to 50μm represent no more than 10%) by weight of the total excipient
powder.
16. An excipient powder according to any preceding claim wherein at least
30% by weight of the coarse first fraction has a particle size of at least lOOμm.
17. A powder composition for inhalation comprising an excipient according to any preceding claim and a particulate pharmaceutically active substance.
18. A composition according to Claim 16 wherein 90%o by weight of the
active substance has a particle size of no more than lOμm.
PCT/US1999/028608 1998-12-04 1999-12-03 Inhalation powders Ceased WO2000033789A2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU20383/00A AU2038300A (en) 1998-12-04 1999-12-03 Inhalation powders

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB9826783.4 1998-12-04
GBGB9826783.4A GB9826783D0 (en) 1998-12-04 1998-12-04 Inhalation powders

Publications (2)

Publication Number Publication Date
WO2000033789A2 true WO2000033789A2 (en) 2000-06-15
WO2000033789A3 WO2000033789A3 (en) 2000-09-14

Family

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Country Status (3)

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AU (1) AU2038300A (en)
GB (1) GB9826783D0 (en)
WO (1) WO2000033789A2 (en)

Cited By (22)

* Cited by examiner, † Cited by third party
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WO2001095885A1 (en) * 2000-06-16 2001-12-20 Glaxo Group Limited Dry-powder pharmaceutical formulation for inhalation comprising alpha4-intergrin antagonist
WO2002000197A1 (en) * 2000-06-27 2002-01-03 Vectura Limited Method of making particles for use in a pharmaceutical composition
GB2363987A (en) * 2000-04-17 2002-01-16 Vectura Ltd Formulations for dry powder inhalers comprising fractions of fine and coarse particle size
JP2004501183A (en) * 2000-06-27 2004-01-15 ヴェクトゥラ リミテッド Method for producing particles for use in pharmaceutical compositions
US7399528B2 (en) 1999-07-16 2008-07-15 Chiesi Farmaceutici S.P.A. Powder particles with smooth surface for use in inhalation therapy
US7541022B2 (en) 2000-04-17 2009-06-02 Vectura Limited Pharmaceutical formulations for dry powder inhalers
US8726874B2 (en) 2012-05-01 2014-05-20 Ford Global Technologies, Llc Cylinder bore with selective surface treatment and method of making the same
US20150202148A1 (en) * 2012-07-05 2015-07-23 Arven llac Sanayi Ve Ticaret Anonim Sirketi Dry powder inhalers comprising a carrier other than lactose
WO2016055544A1 (en) * 2014-10-08 2016-04-14 Eratech S.R.L. Composition comprising at least one dry powder obtained by spray drying to increase the stability of the formulation
WO2016055546A1 (en) * 2014-10-08 2016-04-14 Zambon S.P.A. Pharmaceutical composition containing budesonide and formoterol.
US9365905B2 (en) 2005-02-10 2016-06-14 Dmv-Fonterra Excipients Technology Gmbh Processes for making lactose utilizing pre-classification techniques and pharmaceutical formulations formed therefrom
CN106692116A (en) * 2015-11-15 2017-05-24 复旦大学 Capsule-type inhalation aerosol powder containing isoforskolin
US20170143625A1 (en) * 2014-07-09 2017-05-25 Arven Ilac Sanayi Ve Ticaret Anonim Sirketi Novel process for the preparation of dry powder formulations
US20170348290A1 (en) * 2013-07-03 2017-12-07 Luxena Pharmaceuticals, Inc. Novel aerosol formulations of granisetron and uses thereof
US9931304B2 (en) 2000-11-30 2018-04-03 Vectura Limited Method of making particles for use in a pharmaceutical composition
US10105316B2 (en) 2012-07-05 2018-10-23 Arven llac Sanayi Ve Ticaret A.S. Inhalation compositions comprising muscarinic receptor antagonist
US10238601B2 (en) 2000-11-30 2019-03-26 Vectura Limited Particles for use in a pharmaceutical composition
US10314784B2 (en) 2006-06-30 2019-06-11 Novartis Ag Compositions of glycopyrronium salt for inhalation
WO2021058454A1 (en) 2019-09-24 2021-04-01 Chiesi Farmaceutici S.P.A. Novel carrier particles for dry powder formulations for inhalation
KR20220078315A (en) * 2020-12-03 2022-06-10 충북대학교 산학협력단 Dry powder inhalation formulation containing selexipag and manufacturing method thereof
US20220387313A1 (en) * 2013-07-03 2022-12-08 Luxena Pharmaceuticals, Inc. Novel aerosol formulations of ondansetron and uses thereof
EP4316473A2 (en) 2013-03-28 2024-02-07 Vectura Limited Use of stearate in an inhalable formulation

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US5747445A (en) * 1993-06-24 1998-05-05 Astra Aktiebolag Therapeutic preparation for inhalation

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US7399528B2 (en) 1999-07-16 2008-07-15 Chiesi Farmaceutici S.P.A. Powder particles with smooth surface for use in inhalation therapy
US6884794B2 (en) 2000-04-17 2005-04-26 Chiesi Farmaceutici S.P.A. Pharmaceutical formulations for dry powder inhalers in the form of hard-pellets
US7541022B2 (en) 2000-04-17 2009-06-02 Vectura Limited Pharmaceutical formulations for dry powder inhalers
WO2001078695A3 (en) * 2000-04-17 2002-03-14 Vectura Ltd Pharmaceutical formulations for dry powder inhalers
US9566239B2 (en) 2000-04-17 2017-02-14 Vectura Limited Pharmaceutical formulations for dry powder inhalers
US8871274B2 (en) 2000-04-17 2014-10-28 Vectura Limited Pharmaceutical formulations for dry powder inhalers
EP1719505A2 (en) 2000-04-17 2006-11-08 CHIESI FARMACEUTICI S.p.A. Pharmaceutical formulations for dry powder inhalers in the form of hard pellets
US7223748B2 (en) 2000-04-17 2007-05-29 Chiesi Farmaceutici S.P.A. Pharmaceutical formulations for dry powder inhalers in the form of hard-pellets
EP1829533A3 (en) * 2000-04-17 2007-10-31 Vectura Limited Pharmaceutical formulations for dry powder inhalers
GB2363987A (en) * 2000-04-17 2002-01-16 Vectura Ltd Formulations for dry powder inhalers comprising fractions of fine and coarse particle size
EP2272508A3 (en) * 2000-04-17 2012-01-18 Vectura Limited Pharmaceutical Formulations for Dry Powder Inhalers
EP2272508A2 (en) 2000-04-17 2011-01-12 Vectura Limited Pharmaceutical Formulations for Dry Powder Inhalers
WO2001095885A1 (en) * 2000-06-16 2001-12-20 Glaxo Group Limited Dry-powder pharmaceutical formulation for inhalation comprising alpha4-intergrin antagonist
US7744855B2 (en) 2000-06-27 2010-06-29 Vectura Limited Method of making particles for use in a pharmaceutical composition
JP2004501183A (en) * 2000-06-27 2004-01-15 ヴェクトゥラ リミテッド Method for producing particles for use in pharmaceutical compositions
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US10561613B2 (en) 2000-06-27 2020-02-18 Vectura Limited Method of making particles for use in a pharmaceutical composition
US9351928B2 (en) 2000-06-27 2016-05-31 Vectura Limited Method of making particles for use in a pharmaceutical composition
WO2002000197A1 (en) * 2000-06-27 2002-01-03 Vectura Limited Method of making particles for use in a pharmaceutical composition
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