throbber
ELSEVIER
`
`International Journal of Pharmaceutics 221 (2001) 165- 174
`
`international
`journal of
`pharmaceutics
`
`www.elsevier.com/locatejijpharm
`
`Characterisation of the aggregation behaviour in a
`salmeterol and fluticasone propionate inhalation aerosol
`system
`Yonatan Michael a, Martin J. Snowden a,*, Babur Z. Chowdhry a,
`Ian C. Ashurst b, Craig J. Davies-Cutting h, Trevor Riley b
`a School of Chemical and Life Sciences, University of Greenwich, Wellington Street, Woolwich, London SE18 6PF, UK
`b Inhalation Product Development, GlaxoSmithKline R&D, Park Road, Ware, Hertfordshire SG12 ODP, UK
`
`Received 8 December 2000; received in revised form 23 March 2001; accepted 30 March 2001
`
`Abstract
`
`The nature of the drug-drug aggregation phenomena between salmeterol xinafoate and fluticasone propionate used
`in a metered-dose inhaler system has been examined. Interactions between the drugs in the solvents 1,1 ,2-trichlorotrifl(cid:173)
`oroethane (CFC-113) and 1,1,1,2-tetrafluoroethane (HFA-134a) have been characterised using a focused beam
`reflectance measurement probe by measuring the average floc size of the drug particles individually and in
`combination as a function of stirrer rate. The floc composition in the CFC-113 system, where the drug particles
`cream, was determined by high-performance liquid chromatography analysis. The aggregation behaviour of the
`individual drugs was shown to depend on the physical and chemical properties of both the drug substance and the
`media. Larger floes were observed for salmeterol xinafoate compared with fluticasone propionate, while both drugs
`formed larger aggregates in HF A-134a compared with in CFC-113. The floc composition studies demonstrated that,
`in the combined formulation in CFC-113, sahneterol xinafoate and fluticasone propionate aggregate together to form
`hetero-flocs. The interaction between the two drugs was such that they did not separate on creaming, despite having
`different densities. The average floc size of the combined drug suspension was also found to depend on the dispersion
`medium. © 2001 Elsevier Science B.V. All rights reserved.
`
`Keywords: Salmeterol xinafoate; Fluticasone propionate; HFA-134a; CFC-113; Aggregation; Focused beam reflectance
`
`*Corresponding author. Tel.: + 44-208-3319981; Fax: +
`44-208-3318305.
`E-mail address: m.j.snowden@greenwich.ac.uk (M.J. Snow(cid:173)
`den).
`
`1. Introduction
`
`Metered-dose inhalers (MDis) are the most fre(cid:173)
`quently employed dosage forms for delivering ac(cid:173)
`tive drug substances to the respiratory tract via
`the inhaled route. MDis contain fine micronised
`drugs
`in a suspension of chlorofluorocarbon
`
`0378-5173/01/$ - see front matter © 2001 Elsevier Science B.V. All rights reserved.
`PII: 80378-5173(0 1)00678-0
`
`PLAINTIFFS'
`TRIAL EXHIBIT
`PTX0179
`
`MEDA_APTX03505071
`
`PTX0179-00001
`
`1
`
`CIP2044
`Argentum Pharmaceuticals LLC v. Cipla Ltd.
`IPR2017-00807
`
`

`

`166
`
`Y. Michael et al. /International Journal of Pharmaceutics 221 (2001) 165-174
`
`(CFC) or hydrofluoroalkane (HFA) propellants,
`which act as both a suspending medium and
`propellant. Current formulations are predomi(cid:173)
`nantly suspensions of single micronised active
`compound in the range 2-5 ~-tm in liquefied
`CFCs or HF As. The physical and chemical
`properties of the single-drug formulations are, in
`principle, easier to study. Combined drug for(cid:173)
`mulations are less well understood and, as a re(cid:173)
`significant amount of fundamental
`sult, a
`scientific research work on the subject is being
`undertaken. Previous work (Michael et al., 2000)
`on the combined inhaler formulations of both
`salmeterol xinafoate and fluticasone propionate
`in propellant CFC-113 indicates that hetero-ag(cid:173)
`gregation of the two drugs would appear to be
`taking place. The hetero-aggregation results in
`reduced drug deposition on to the MDI surfaces
`as compared with that observed with the indi(cid:173)
`vidual drug formulations. This phenomenon
`could be an advantage from a pharmaceutical
`point of view, i.e. the combination formulation
`shows a decrease in the total loss of the drugs
`due to deposition on to the internal surfaces of
`the MDI. Clinical studies have indicated that
`drug formulation of salmeterol xinafoate and
`fluticasone propionate in a single inhaler pro(cid:173)
`vides a treatment as efficacious in achieving
`asthma control and as well tolerated over a 28-
`week period as the two drugs administered indi(cid:173)
`vidually (Chapman et al., 1999). However, a
`clearer understanding of the aggregation be(cid:173)
`haviour of salmeterol xinafoate and fluticasone
`propionate will facilitate the design of combina(cid:173)
`tion aerosol systems.
`A number of methods were considered in an
`attempt
`to characterise
`the aggregation be(cid:173)
`haviour of suspensions in MDis. Microscopy is
`a commonly used technique that allows an opti(cid:173)
`cal inspection of the particles and can be used
`to judge whether a good dispersion has been
`achieved or if any aggregation is present in the
`system (Rawle, 1999). Light-diffraction
`tech(cid:173)
`niques (Sidhu et al., 1993) are also used for the
`study of floes in liquid suspensions, and the par(cid:173)
`ticles in suspension are measured by re-circulat(cid:173)
`ing the sample in front of the laser beam. This
`technique was, however, found to be unsuitable
`
`due to the high optical absorbance of the con(cid:173)
`centrated suspensions, which made scattering
`measurements difficult due to low signals and
`multiple scattering. Rheological methods (Sidhu
`et al., 1993) have also been used to study the
`in
`inhalation systems.
`extent of flocculation
`However, these methods normally make use of
`high solid-phase concentrations of the dispersed
`materials as compared with those normally en(cid:173)
`countered in commercial metered-dose inhalers.
`In addition, small-angle
`light-scattering
`tech(cid:173)
`niques have also been used to study the size and
`structural dynamics of floes (Spicer et al., 1998);
`however, floes in MDis would be too large for
`this techniques.
`The objective of the work reported herein was
`to gain a better understanding of the physical
`and chemical factors involved in the combined
`formulation of salmeterol and fluticasone propi(cid:173)
`onate in a single MDI aerosol system. The ag(cid:173)
`gregation of salmeterol xinafoate and fluticasone
`propionate
`in HFA-134a and CFC-113 was
`studied using a focused beam reflectance mea(cid:173)
`surement (FBRM), which enables floc size to be
`determined as a function of stirrer rate. In addi(cid:173)
`tion, a floc composition study of the CFC-based
`combined drug formulation was performed to
`monitor the migration behaviour of the individ(cid:173)
`ual drugs within the suspension.
`
`2. Materials and methods
`
`2.1. Reagents
`
`The test samples of salmeterol xinafoate and
`fluticasone propionate were donated by GlaxoS(cid:173)
`mithKline Research and Development (Ware,
`UK), and were used as received. The propellants
`1,1,2-trichlorotrifloroethane
`(CFC-113)
`and
`1,1,1,2-tetrafluoroethane (HFA-134a), with a wa(cid:173)
`ter content of less than 10 p.p.m., were obtained
`from ICI Chemicals and Polymers Ltd (Run(cid:173)
`corn, Cheshire, UK). Poly(vinyl chloride) (PVC)(cid:173)
`coated glass aerosol bottles were supplied by
`~-tl metering
`Wheaton Ltd (NJ, USA) and 63
`valves were purchased from Valois S.A. (Le
`Neubourg, France).
`
`MEDA_APTX03505072
`
`PTX0179-00002
`
`2
`
`

`

`Y. Michael et al. /International Journal of Pharmaceutics 221 (2001) 165-174
`
`167
`
`2.2. Focused beam reflectance measurement
`
`The aggregation behaviour of the suspensions
`was studied by FBRM, using a Lasentec Labtec
`1000 instrument (Lasentec Inc, Redmond, USA)
`(Allen and Davies, 1998). The apparatus uses a
`focused laser diode beam source that is projected
`on to the sample at a fixed velocity and rapidly
`scans across the particle structures. As the focused
`beam transcribes a particle or floc structure, light
`from the incident beam is reflected back until the
`beam reaches the opposite edge of the particle.
`The back-scattered light is collected by a pair of
`stereoscopic photodiode detectors and converted
`into an electronic signal. The chord length of the
`particle or aggregate can then be determined from
`the product of the pulse duration and the velocity
`of the scanning laser. The chord lengths measured
`over a specific time period are sorted into a
`38-chord distribution that covers the size range
`0.4-250
`J.lm. Because
`the beam does not
`intersect the particle in the same way every time,
`the so-called 'random chord length distribution'
`of the particles is measured (Fig. 1). During one
`measurement cycle, adjusted to 8 s, thousands of
`particles are identified. To produce robust statis(cid:173)
`tics, 2000 or more particles need to be sampled
`per second. An advantage of FBRM over forward
`scattering or transmission sizing techniques is that
`opaque dispersions can be analysed. Hence, ex(cid:173)
`periments can be performed at realistic concentra(cid:173)
`tions, without the need for sample dilution.
`Unlike many other particle sizing techniques,
`pressurised systems can be readily studied using
`the Lasentec Labtec 100 without the need for
`building a complex pressure cell. Instead, samples
`may be presented in cylindrical glass-coated aero(cid:173)
`sol bottles. Nevertheless, an important aspect of
`
`the Lasentec system is that the hydrodynamic
`conditions must be such that a representative
`sample flows past the probe window. This cannot
`always be guaranteed in practice, causing system(cid:173)
`atic errors or noisy signals (Dijkstra et al., 1996).
`Measurement of the floc size of the suspensions
`can be hindered by either gravitational sedimenta(cid:173)
`tion or creaming, if the densities of the solid and
`liquid phase are unequal. To avoid this problem,
`the suspensions were agitated by means of a mag(cid:173)
`netic stirrer. By varying the rotational velocity of
`the magnetic stirrer, it is possible to control the
`shear conditions within the sample. The shear
`stress in the aerosol bottle filled with HFA-134a
`at a stirrer speed of 1000 rev min- 1, was esti(cid:173)
`mated by assuming laminar flow and was found
`to be of the order of 0.025 N m - 2 .
`Data from the experiments were collected by
`analysing the samples at three equidistant posi(cid:173)
`tions on the aerosol bottle. At each position, two
`particle size determinations were performed, with
`each determination being the mean of five mea(cid:173)
`surements, averaged by the instrument software.
`The floc size measurement of one sample was,
`therefore, the average of salmeterol xinafoate and
`fluticasone propionate six particle size determina(cid:173)
`tions from
`three different positions on
`the
`bottle. In this way, errors due to imperfections in
`the plastic-coated aerosol bottles could be min(cid:173)
`imised.
`
`2.3. Floc size analysis
`
`Model suspensions in HFA-134a were prepared
`by pressure filling propellant through a valve at(cid:173)
`tached to a pressure-resistant 15 ml round clear
`PVC-coated glass aerosol bottle, to which known
`
`Scanning Laser Beam
`
`Duration of Reflection
`Measured - Chord
`
`Fig. I. An illustration of the normalised chord length distribution of a particulate species.
`
`MEDA_APTX03505073
`
`PTX0179-00003
`
`3
`
`

`

`168
`
`Y. Michael et al. /International Journal of Pharmaceutics 221 (2001) 165-174
`
`quantity of the drugs had been added. Individual
`drug suspensions over the concentration range
`0.02-0.50% w/w salmeterol xinafoate and flutica(cid:173)
`sone propionate were prepared. Suspensions con(cid:173)
`taining 0.05% w jw salmeterol xinafoate together
`with 0.07% wjw fluticasone propionate were used
`to study aggregation behaviour in the combina(cid:173)
`tion
`product.
`These
`concentrations
`are
`equivalent to the strengths of salmeterol and fluti(cid:173)
`casone propionate combination products that
`were marketed
`initially
`in
`the United
`Kingdom from July 2000. A glass-coated mag(cid:173)
`netic stirrer bar (13 x 5 mm2) was added to each
`aerosol bottle before a metering valve was
`crimped into place (Pamasol model type 2002).
`The bottles were filled with approximately 18 g
`HFA-134a via a pressure burette, which was pres(cid:173)
`surised at about 5 bar with HFA-134a at room
`temperature. Each of the formulations was pre(cid:173)
`pared in triplicate. The aerosol bottles were soni(cid:173)
`cated (Decon FS300 ultra-sonic bath) for 10 min
`to remove any entrapped air from the suspension
`and to promote dispersion. After equilibration,
`the suspensions were re-weighed to ensure that
`significant amounts of propellant had not been
`lost due to evaporation. Drug suspensions in
`CFC-113 were prepared in the same way, except
`that the CFC was filled directly into the aerosol
`bottles prior to being sealed with the metering
`valve.
`The median chord length of the individual drug
`suspensions in the two propellants was measured
`as a function of drug concentration using the
`FBRM system at a constant stirrer rate of 300 rev
`min- 1. The robustness of the floes was investi(cid:173)
`gated by measuring the average floc size of the
`drug suspension as a function of increasing stirrer
`speed up to a maximum of 1500 rev min- 1. The
`suspension was allowed to equilibrate for 5 min at
`each speed setting before measurements were
`made.
`The reproducibility of the Lasentec FBRM re(cid:173)
`sponse was checked by performing repeat mea(cid:173)
`surements of an external standard of aqueous
`graphite dispersion at a constant stirrer rate of
`250 rev min - 1 and interspersed with the samples
`throughout the measurements. The median chord
`length distribution of the graphite standard was
`
`repeatedly found to be 6.00 ± 0.33 11m. Further(cid:173)
`more, the particle size of the graphite standard
`was found to be independent of stirrer speed.
`
`2.4. Electrophoretic mobility studies
`
`The electrophoretic mobility of the suspended
`drug particles was determined using a Malvern
`Zetasizer 3000 (Malvern Instruments, UK) in con(cid:173)
`junction with a non-aqueous dip cell that has a
`narrow electrode gap of 2 mm. Individual disper(cid:173)
`sions of 0.0025% wjw salmeterol xinafoate and
`0.0035% wjw fluticasone propionate were pre(cid:173)
`pared in CFC-113 to give a suspension of suitable
`conductance. The dispersions were ultrasonicated
`for 10 min prior to analysis to ensure that the
`drug was fully dispersed.
`
`2.5. Floc composition studies
`
`Floc composition studies were performed on
`suspensions of the two drugs to examine the
`settling behaviour of the drug particles in the
`absence of shear. Individual and combined disper(cid:173)
`sion concentrations of 0.05% wjw salmeterol xi(cid:173)
`nafoate and 0.07% wjw fluticasone propionate
`were studied in CFC-113 solvent only, as the high
`vapour pressure of HFA-134a propellant makes
`sampling difficult. Suspensions were prepared as
`described in Section 2.3 except that the aerosol
`bottles were sealed with a rubber septum. Using a
`glass syringe, 1 ml suspension was slowly removed
`from a position approximately one-quarter of the
`way from the bottom of the aerosol bottle with(cid:173)
`out re-dispersing the sample. The dispersions were
`sampled at time intervals of 0, 1.5, 5 and 10 min
`and the 1 ml aliquots transferred to 50 ml volu(cid:173)
`metric flasks. Fig. 2 shows photographs taken to
`illustrate the separation behaviour of concen(cid:173)
`trated drug dispersion after a time interval of 10
`min. The collected samples were left open to the
`atmosphere to allow evaporation of the CFC
`solvent, and the drug then dissolved in 70/30 (v /v)
`methanol/water and assayed by high-performance
`liquid chromatography (HPLC) with UV detec(cid:173)
`tion at 228 nm. The details of the HPLC analyti(cid:173)
`cal method have previously been described by
`Michael et al. (2000).
`
`MEDA_APTX0350507 4
`
`PTX0179-00004
`
`4
`
`

`

`Y. Michael et al. /International Journal of Pharmaceutics 221 (2001) 165-174
`
`169
`
`Fig. 3 illustrates that the average floc size of the
`salmeterol xinafoate aggregates is larger than that
`of the fluticasone propionate aggregates, in both
`CFC and HF A media. This may be partially due
`to salmeterol xinafoate having a lower density
`(1.2 g em- 1 as determined by helium pycnometry)
`compared with that of fluticasone propionate (1.3
`g em- 1), and therefore occupying a larger phase
`volume at the same w/w concentration. However,
`the nature of the drug may also influence the
`aggregation behaviour in the suspensions. The
`electrophoretic mobilities of salmeterol xinafoate
`and fluticasone propionate in CFC-113 were
`found to be 3 X 10- 9 and 1 X 1Q- 9 m2 s- 1 y- 1 ,
`respectively, at l5°C. This reflects the fact that a
`higher charge is present on the surface of salme(cid:173)
`terol xinafoate compared with that of fluticasone
`propionate, which is believed to increase the po(cid:173)
`larity of salmeterol xinafoate relative to flutica(cid:173)
`sone propionate. It would be expected that the
`hydrophobic
`fluticasone propionate particles
`would be wetted more readily in the non-polar
`CFC-113 environment than the salmeterol xi(cid:173)
`nafoate particles. This could explain why flutica(cid:173)
`sone propionate forms more compact aggregates
`than salmeterol xinafoate.
`The results presented in Fig. 3 also illustrate
`that the suspending medium has a considerable
`effect on the floc size of the drug suspension. The
`average floc size of both salmeterol xinafoate and
`fluticasone propionate was larger in HFA-134a as
`compared with in CFC-113. For diffusion-limited
`aggregation, the aggregation kinetics of the sus(cid:173)
`pension will be dependent on the viscosity of the
`medium. Einstein's law of diffusion, states that
`the diffusion coefficient of spherical particles is
`given by (Shaw, 1992): D = (kT)/(6n1Ja), where k
`is Boltzmann's constant, Tis the absolute temper(cid:173)
`ature, 1J
`is the viscosity and a is the particle
`radius.
`Comparing the liquid viscosity of HFA-134a
`(0.20 mPa s) with that ofCFC-113 (0.66 mPa s) at
`25°C (Solvay, 1992), it can be seen that the diffu(cid:173)
`sion coefficient of drug particles in HFA-134a is
`approximately three times faster than in CFC-
`113. Hence, under equivalent shear conditions,
`the faster rate of coagulation would be expected
`to result in the observed floc size increase.
`
`X
`=~===
`
`(a)
`
`(b)
`
`Fig. 2. Photographs illustrating the settling behaviour of con(cid:173)
`centrated drug dispersion at (a) 0 min and (b) 10 min intervals.
`Samples for floc composition studies were taken from position
`x using a syringe.
`
`3. Results and discussions
`
`Characterisation of the MDI formulations ini(cid:173)
`tially concentrated on understanding the dis(cid:173)
`persibility of the individual drug suspensions in
`CFC-113 and HFA-134a aerosol propellants, and
`was then extended to examine the combined drug
`system at different drug concentrations and molar
`ratios of drugs.
`Suspension concentration is an important fac(cid:173)
`tor in determining the behaviour of suspensions of
`drugs in liquid suspensions. In the absence of
`shear, the drug particles tend to flocculate, which
`leads to a separation of the solid phase due to the
`relative density difference between the drug and
`the liquid continuous phase. When the suspension
`is subjected to stirring, random collisions of drug
`particles with the walls of the container and with
`each other can result in breakdown of the floc
`structure. Plots of the average aggregate size as a
`function of the suspension concentration of sal(cid:173)
`meterol xinafoate and fluticasone propionate in
`HFA-134a and CFC-113, at a constant stirrer
`speed of 300 rev min- 1, are shown in Fig. 3. In
`all cases, the floc size of the suspensions increased
`with increasing drug concentration. Bower et al.
`(1996) have reported that in a system of constant
`shear stress the disruptive force is unchanged and
`therefore increasing the drug concentration results
`in the equilibrium being shifted towards aggregate
`formation.
`
`MEDA_APTX03505075
`
`PTX0179-00005
`
`5
`
`

`

`170
`
`Y. Michael et al. /International Journal of Pharmaceutics 221 (2001) 165-174
`
`In addition, the dipole moment of HF A is
`known to be greater than that of CFC (Blondino
`and Byron 1998). The greater polarity of HFA
`combined with the presence of hydrogen sub(cid:173)
`stituents allows for considerable charge separation
`in this propellant molecule, owing to the elec(cid:173)
`tronegativity of the fluorine atoms (Blondino and
`Byron 1998). The presence of a layer of oriented
`dipolar molecules at the surface may make a
`significant contribution to the nature of the elec(cid:173)
`trical double layer (Shaw, 1992). This polarisation
`effect induces a temporary dipole on the drug
`molecule without changing the net surface charge
`of the drug. This may lead to an increase in the
`van der Waals force of attraction between drug
`particles and therefore an increased tendency to
`form larger floes in the HF A medium compared
`with in CFC (Fig. 3).
`Fig. 4 shows how the average floc size of the
`drugs varies with increasing stirrer speed in HFA-
`134a and CFC-113. In all cases, the average floc
`
`size of the suspensions initially decreased sharply
`as the stirrer rate was increased, before becoming
`less shear dependent at higher stirrer speeds. For
`example, the floc size of the combined drug dis(cid:173)
`persion of 0.05% wfw salmeterol xinafoate and
`0.07% w/w fluticasone propionate decreased from
`101.2 to 39.5 J.lm in HFA-134a and from 19.8 to
`8.2 J.lm in CFC-113, i.e. an approximately 60%
`reduction of the original size of the floc over the
`range 200-1000 rev min- 1• The shape of these
`profiles is attributed to the structural breakdown
`of floc structure as they are subjected to higher
`shear forces. However, it is noticeable that the
`floes persisted even at the highest shear rate stud(cid:173)
`ied, suggesting that the aggregates are not broken
`down to the size of the input drugs (2-5 J.lm). The
`average floc size of the combined formulation of
`0.05% wfw salmeterol xinafoate and 0.07% w/w
`fluticasone propionate in CFC-113 was greater
`than that of the individual drugs. This was ex(cid:173)
`pected on the basis of the higher drug concentra-
`
`i
`-.5
`1.»
`.~
`(I)
`to>
`
`..s
`
`~
`
`140
`
`120
`
`100
`
`80
`
`(j()
`
`40
`
`2() ~ ~
`
`8
`
`)<
`
`0+-----~----r----,----~-----r----.-----~----.-----r---~
`0.5
`
`()
`
`0.1
`
`0.2
`
`0.3
`
`0.4
`
`Suspension concentration (% w /w)
`
`Fig. 3. Effect of increasing suspension concentration on average floc size of salmeterol xinafoate aggregates in ( ()) HF A-134a and
`(0) CFC-113, and fluticasone propionate aggregates in {D) HFA-134a and ( x) CFC-113. All measurements were made at a stirrer
`rate of 300 rev min- 1•
`
`MEDA_APTX03505076
`
`PTX0179-00006
`
`6
`
`

`

`Y. Michael et al. /International Journal of Pharmaceutics 221 (2001) 165-174
`
`171
`
`140
`
`a
`
`120
`
`100
`
`80
`
`i

`u
`.~
`fl)
`~ 60
`.s
`~
`
`40
`
`20
`
`0
`
`0
`
`25
`
`b
`
`20
`
`5
`
`200
`
`400
`
`600
`
`800
`
`1000
`
`1200
`
`1400
`
`1600
`
`Stirrer rate (rev min"1)
`
`0
`
`200
`
`400
`
`600
`1000
`800
`Stirrer rate (rev min"1)
`
`1200
`
`1400
`
`1600
`
`Fig. 4. Effect of increasing stirrer rate on the average floc size of ( ()) 0.05% wjw salmeterol xinafoate, (D) 0.07% wjw fiuticasone
`propionate, and (0) 0.05% wjw salmeterol xinafoate/0.07% wjw fiuticasone propionate aggregates in (a) HFA-134a and (b)
`CFC-113.
`
`MEDA_APTX03505077
`
`PTX0179-00007
`
`7
`
`

`

`172
`
`Y. Michael et al. /International Journal of Pharmaceutics 221 (2001) 165-174
`
`(a)
`
`120
`
`100
`
`80
`
`60
`
`40
`
`20 (b)~
`..........
`--~ •..... .• i!J ..........
`
`......
`!
`
`u
`.!:I
`Cll
`u .s
`
`~
`
`•
`
`•
`
`0
`
`0
`
`200
`
`400
`
`800
`1000
`600
`Stirrer rate (rev min"1)
`
`1200
`
`1400
`
`1600
`
`Fig. 5. Average floc size measurement of the combined drug formulation of 0.05% w jw salmeterol xinafoate and 0.07% w/w
`fluticasone propionate as a function of increasing and decreasing stirrer rate in (a) HFA-134a and (b) CFC-113: <>, increasing rate;
`D, decreasing rate.
`
`tion of the combined formulation. In contrast, the
`floc size of the combined formulation in HFA-
`134a appeared to be an average of that of the
`individual drugs, over the entire stirrer speed
`range. Hence, it would appear that the interaction
`between salmeterol xinafoate and fluticasone pro(cid:173)
`pionate in the combined formulation is dependent
`on the physical properties of the solvent. This in
`turn leads to differences in the aggregation be(cid:173)
`haviour of the two drugs. Wang (1992) studied
`the hetero-flocculation of particles of different
`sizes in an apatite-hematite-phlogopite disper(cid:173)
`sion system. The studies showed that particles in
`mixed suspensions were affected by each other's
`stability in a way that the size growth of the less
`stable particles increased the hetero-flocculation
`rate constant and caused the loss of flocculation
`selectivity, especially between the middle and large
`size particles. This indicates that a difference in
`floc size has an effect on the mutual interaction
`between the particles in the dispersion, which can
`
`to
`
`in preference
`
`promote hetero-flocculation
`homo-flocculation.
`In order to determine whether the breakdown
`and re-formulation of the hetero-floc structures is
`a reversible process, the effect of increasing and
`decreasing the stirrer speed on the average floc
`size was investigated. Fig. 5 shows that the aver(cid:173)
`age floc size of the combined drug formulation of
`0.05% wjw salmeterol xinafoate and 0.07% wjw
`fluticasone propionate in CFC-113 was the same
`in both increasing and decreasing shear experi(cid:173)
`ments. In the case of the combined formulation in
`HFA-134a, there was a slight hysteresis effect, but
`most of the floc structure recovered. The interpar(cid:173)
`ticulate binding between salmeterol xinafoate and
`fluticasone propionate is a reversible process.
`However, it is apparent that the drug particles
`had not completely returned to their original state
`after an equilibration period of 5 min. Further
`work performing additional measurements after
`different equilibration
`times could
`therefore
`
`MEDA_APTX03505078
`
`PTX0179-00008
`
`8
`
`

`

`Y. Michael et al. /International Journal of Pharmaceutics 221 (2001) 165-174
`
`173
`
`provide an insight into the flocculation kinetics of
`these systems.
`The composition of the floc structures of single
`and combined formulations of 0.05% wfw salme(cid:173)
`terol xinafoate and 0.07% wfw fluticasone propi(cid:173)
`onate in CFC-113 was determined as a function
`of time (see Fig. 6). Initially, post agitation, the
`suspensions are well dispersed. This is followed by
`macroscopic flocculation, which in turn leads to
`phase separation between the drug particles and
`the dispersion medium. The drug particles migrate
`to the air/liquid surface of the sample (creaming
`phenomena) and, as a result, the drug concentra(cid:173)
`tion at the bottom of the sample decreases over a
`period of time. Although all the plots in Fig. 6
`show a similar characteristic decrease in drug
`concentration with time, the data demonstrate
`that there are significant differences between the
`individual and combined suspension formula(cid:173)
`tions. The densities of salmeterol xinafoate and
`
`fluticasone propionate are approximately 1.2 and
`1.3 g em- 3, respectively. Hence, both the drugs
`cream in CFC-113, which has a density of 1.57 g
`em- 3 at 25°C. Since fluticasone propionate is
`denser than salmeterol xinafoate, it creams less
`rapidly as shown in Fig. 6. It is also interesting to
`note that, in the combined formulation, salme(cid:173)
`terol xinafoate
`and
`fluticasone propionate
`creamed at approximately the same rate. If there
`were no interparticulate interactions between the
`two drugs, then they would be expected to sepa(cid:173)
`rate on creaming as a consequence of their differ(cid:173)
`ent densities. Hence,
`this data suggests
`that
`salmeterol xinafoate and fluticasone propionate
`must be inextricably bound in a hetero-flocculated
`state. The hetero-flocs cream faster than either of
`the individual drugs. This may be attributed to
`the higher solids concentration of the combined
`formulation, giving rise to a larger floc s1ze, as
`shown in Fig. 4.
`
`12 -~ 10
`
`........
`Ill
`~
`"::!?. e.... 8
`li
`-~
`~
`
`l 4.1 l 4.1
`
`~
`4.1
`~
`
`6
`
`4
`
`2
`
`...
`. . ·· .... (b)
`... ···![ .• ...
`
`..... ...
`
`. ..
`
`...... ... . ..
`... ... .. .. .._ .. ... ... ... .. , ...
`
`...
`.• "3:
`
`. ..
`
`. •.• ·:I:
`
`0+-----~--~----~----~--~~--~----,-----~--~~--~--
`4
`6
`8
`10
`0
`2
`Time (min)
`
`Fig. 6. Percentage drug weight measurement from a flocculated suspension at different time intervals for single and combined drug
`formulations in CFC-113: (a) 0.07% w/w fluticasone propionate, (b) 0.05% w/w salmeterol xinafoate, (c) fluticasone propionate from
`a combined formulation of 0.05% w/w salmeterol xinafoate and 0.07% w/w fluticasone propionate, and (d) salmeterol xinafoate from
`a combined formulation of 0.05% w/w salmeterol xinafoate and 0.07% w/w fluticasone propionate. wE/w0 , Percentage ratio of
`experimental weight relative to the original weight of the drug.
`
`MEDA_APTX03505079
`
`PTX0179-00009
`
`9
`
`

`

`174
`
`Y. Michael et al. /International Journal of Pharmaceutics 221 (2001) 165-174
`
`4. Conclusions
`
`The focus of this paper has been to gain an
`understanding of the interaction between salme(cid:173)
`terol xinafoate and fluticasone propionate in sin(cid:173)
`gle and combined formulations. The study
`demonstrates that the formulation behaviour of
`the individual drugs is dependent on the physical
`and chemical properties of both the media and the
`drug substance itself. In CFC-113, the two drugs
`hetero-flocculate in the combination product and
`consequently do not separate under the influence
`of gravity. Furthermore, the interaction between
`the two drugs leads flocculation behaviour that
`differs from that of the individual drugs. This
`interaction again appears to depend on the physi(cid:173)
`cal properties of the medium.
`
`Acknowledgements
`
`The authors would like to thank Dr Mike
`Kaszuba, Malvern Instrumentals Ltd., for his as(cid:173)
`sistance with the experimental determinations of
`the electrophoretic mobilities of the drugs and Dr
`John F. Miller, Inhalation Product Development,
`GlaxoSmithKline, USA, for helpful discussions.
`
`References
`
`Allen, T., Davies, R., 1998. An evaluation of the Lab-Tee 100
`particle size analyser. Proceedings of the Particle Size
`
`Analysis Conference, London, P.J. Lloyd (Ltd), Wiley, pp.
`33-44.
`Blondino, F.E., Byron, P.R., 1998. Surfactant dissolution and
`water solubilization in chlorine-free liquefied gas propel(cid:173)
`lants. Drug Dev. Ind. Pharm. 24, 935 - 945.
`Bower, C., Washington, C., Purewal, T.S., 1996. The effect of
`surfactant and solid phase concentration on drug aggre(cid:173)
`gates in model aerosol propellant suspensions. J. Pharm.
`Pharmacol. 48, 342- 346.
`Chapman, K .R., Ringdal, N ., Backer, V., Palmqvist, M.,
`Saarelainen, S., Briggs, M., 1999. Salmeterol and flutica(cid:173)
`sone propionate (50/250 llg) administered via combination
`Diskus inhaler: as effective as when given via separate
`Diskus inhalers. Can. Respir. J. 6, 45- 51.
`Dijkstra, J.J.F .M ., deNie, L.H., Pot, A., 1996. In-line mea(cid:173)
`surement of crystal size -
`campaign experience with the
`Lasentec M200 system. Int. Sugar J. 98 (1174), 521 - 523 .
`Michael, Y., Chowdhry, B.Z., Ashurst, I.C., Snowden, M.J.,
`Davies-Cutting, C., Gray, S., 2000. The physico-chemical
`properties of salmeterol and fluticasone propionate in dif(cid:173)
`ferent solvent environments. Int. J. Pharm. 200, 279-288.
`Rawle, A., 1999. The Importance of Particle Size Analysis in
`the Pharmaceutical Industry, Company Report. Malvern
`Instruments, Malvern, Worchestershire, UK, pp. 1-44.
`Shaw, D.J., 1992. Introduction to Colloid and Surface Chem(cid:173)
`istry, 4th ed. Butterworths, London.
`Sidhu, B.K., Washington, C., Davis, S.S., Purewal, T.S., 1993.
`Rheology of model aerosol suspensions. J. Pharm. Phar(cid:173)
`macol. 45, 597-600.
`Solvay, 1992. Technical Service Thermodynamic properties of
`Kaltron 113 and Solkane 134a. Solvay Fluor Und Derivate
`GmbH, Hannover.
`Spicer, P.T., Pratsinis, S.E., Raper, J., Amal, R., Bushell, G.,
`Meesters, G., 1998. Effect of shear schedule on particle
`size, density and structure during flocculation in stirring
`tanks. Powder Techno!. 97, 26-34.
`Wang, Q., 1992. Studies on aggregation and heteroaggregation
`in particle separation systems. Acta Polytech. Scand.(cid:173)
`Chem. Techno!. Ser. 203, 1-48.
`
`MEDA_APTX03505080
`
`PTX01

This document is available on Docket Alarm but you must sign up to view it.


Or .

Accessing this document will incur an additional charge of $.

After purchase, you can access this document again without charge.

Accept $ Charge
throbber

Still Working On It

This document is taking longer than usual to download. This can happen if we need to contact the court directly to obtain the document and their servers are running slowly.

Give it another minute or two to complete, and then try the refresh button.

throbber

A few More Minutes ... Still Working

It can take up to 5 minutes for us to download a document if the court servers are running slowly.

Thank you for your continued patience.

This document could not be displayed.

We could not find this document within its docket. Please go back to the docket page and check the link. If that does not work, go back to the docket and refresh it to pull the newest information.

Your account does not support viewing this document.

You need a Paid Account to view this document. Click here to change your account type.

Your account does not support viewing this document.

Set your membership status to view this document.

With a Docket Alarm membership, you'll get a whole lot more, including:

  • Up-to-date information for this case.
  • Email alerts whenever there is an update.
  • Full text search for other cases.
  • Get email alerts whenever a new case matches your search.

Become a Member

One Moment Please

The filing “” is large (MB) and is being downloaded.

Please refresh this page in a few minutes to see if the filing has been downloaded. The filing will also be emailed to you when the download completes.

Your document is on its way!

If you do not receive the document in five minutes, contact support at support@docketalarm.com.

Sealed Document

We are unable to display this document, it may be under a court ordered seal.

If you have proper credentials to access the file, you may proceed directly to the court's system using your government issued username and password.


Access Government Site

We are redirecting you
to a mobile optimized page.





Document Unreadable or Corrupt

Refresh this Document
Go to the Docket

We are unable to display this document.

Refresh this Document
Go to the Docket