Matthew Jones

The influence of fine excipient particles on the performance of carrier-based dry powder inhalation formulations.

The inclusion of a small amount of fine particle excipient in a carrier-based dry powder inhalation system is a well researched technique to improve formulation performance and is employed in the pharmaceutical industry. The removal of intrinsic fines from a lactose carrier has been found to decrease formulation performance, whereas adding fines of many different materials into formulations increased performance. Changing the particle size of these fines, the amount added and the technique by which they were prepared also affected formulation behaviour. Despite this body of research, there is disagreement as to the mechanism by which fines improved formulation performance, with two main hypotheses presented in the literature. The first hypothesis suggested that fines prevent the drug from adhering to the strongest binding sites on the carrier, whilst the second proposed that fine particles of drug and excipient form mixed agglomerates that are more easily dispersed and deaggregated during aerosolisation. The evidence in support of each hypothesis is limited and it is clear that future research should aim to produce stronger mechanistic evidence. The investigation of interparticulate interactions using techniques such as atomic force microscopy and inverse gas chromatography may prove useful in achieving this aim.

The Role of Fines in the Modification of the Fluidization and Dispersion Mechanism Within Dry Powder Inhaler Formulations

PurposeTo investigate the role of in situ generated fine excipient particles on the fluidization and aerosolization properties of dry powder inhaler (DPI) formulations.Materials and MethodsCarrier based DPI formulations were prepared under low and high shear blending. Powder rheometery was utilized to measure bulk powder properties in a consolidated and aerated state. Powder fluidization and aerosolization characteristics were related to bulk powder properties using high speed imaging and inertial impaction measurements.ResultsHigh shear blending of formulations resulted in the in situ generation of excipient fines, which corresponded to an increase in aerosolization efficiency. The generation of fines were shown to increase the tensile strength and free volume of the carrier, which resulted in a characteristic change in the fluidization properties, as observed by high speed imaging. The increase in minimum fluidization velocity and aerodynamic drag forces required to aerate the powder may provide the source of energy for the increase in fine particle re-suspension.ConclusionsThe in situ generation of excipient fines affect bulk powder properties of DPI formulations, which directly affects fluidization and aerosolization behaviour of DPI formulations. The study suggests an alternative mode of action by which fines increase DPI formulation performance.

An investigation into the relationship between carrier-based dry powder inhalation performance and formulation cohesive-adhesive force balances.

The inclusion of different carrier materials in a dry powder inhaler (DPI) system can alter formulation performance, which might be attributable to variation in the adhesion between drug and carrier particles. The aim of this study was, therefore, to further examine the relationship between drug-carrier adhesion and performance, by comparing data relating to many different drug-carrier combinations. Four drugs and four carriers were employed, giving a total of 16 combinations. The relative magnitude of the drug-carrier adhesion for each combination was quantified using the cohesion-adhesion balance (CAB) approach to colloidal probe atomic force microscopy. The in vitro inhalation performance of the 16 formulations (1.5% w/w drug) was investigated and found to vary significantly. Plots of fine particle dose against drug-carrier CAB ratio revealed that performance was optimised when the drug-carrier CAB ratio was slightly cohesive. This trend was found to fit with those from similar previous studies, although due to the smaller number of formulations investigated previously, the full extent of this relationship had not been revealed. It was concluded, therefore, that when developing a carrier-based DPI, the selection of a drug-carrier combination with a slightly cohesive CAB ratio might result in optimal performance.

An investigation into the dispersion mechanisms of ternary dry powder inhaler formulations by the quantification of interparticulate forces

PurposeTo investigate the dispersion mechanism(s) of ternary dry powder inhaler (DPI) formulations by comparison of the interparticulate adhesions and in vitro performance of a number of carrier–drug–fines combinations.Materials and MethodsThe relative levels of adhesion and cohesion between a lactose carrier and a number of drugs and fine excipients were quantified using the cohesion–adhesion balance (CAB) approach to atomic force microscopy. The in vitro performance of formulations produced using these materials was quantified and the particle size distribution of the aerosol clouds produced from these formulations determined by laser diffraction.ResultsComparison between CAB ratios and formulation performance suggested that the improvement in performance brought about by the addition of fines to which the drug was more adhesive than cohesive might have been due to the formation of agglomerates of drug and fines particles. This was supported by aerosol cloud particle size data. The mechanism(s) underlying the improved performance of ternary formulations where the drug was more cohesive than adhesive to the fines was unclear.ConclusionsThe performance of ternary DPI formulations might be increased by the preferential formation of drug–fines agglomerates, which might be subject to greater deagglomeration forces during aerosolisation than smaller agglomerates, thus producing better formulation performance.

Experimental observations of dry powder inhaler dose fluidisation

Dry powder inhalers (DPIs) are widely used to deliver respiratory medication as a fine powder. This study investigates the physical mechanism of DPI operation, assessing the effects of geometry, inhalation and powder type on dose fluidisation. Patient inhalation through an idealised DPI was simulated as a linearly increasing pressure drop across three powder dose reservoir geometries permitting an analysis of shear and normal forces on dose evacuation. Pressure drop gradients of 3.3, 10 and 30 kPa s(-1)were applied to four powder types (glass, aluminium, and lactose 6 and 16% fines) and high speed video of each powder dose fluidisation was recorded and quantitatively analysed. Two distinct mechanisms are identified, labelled fracture and erosion. Fracture mode occurs when the initial evacuation occurs in several large agglomerates whilst erosion mode occurs gradually, with successive layers being evacuated by the high speed gas flow at the bed/gas interface. The mechanism depends on the powder type, and is independent of the reservoir geometries or pressure drop gradients tested. Both lactose powders exhibit fracture characteristics, while aluminium and glass powders fluidise as an erosion. Further analysis of the four powder types by an annular shear cell showed that the fluidisation mechanism cannot be predicted using bulk powder properties.

The use of inverse gas chromatography for the study of lactose and pharmaceutical materials used in dry powder inhalers

Inverse gas chromatography (IGC) is a sensitive technique for the measurement of powder surface properties, especially surface energetics. Given the importance of these characteristics to the performance of dry powder inhaler formulations (DPIs), it is unsurprising that IGC has been applied to the study of these systems. Monitoring batch-to-batch variation and the effects of processing steps are established uses of IGC in this field and the relevant studies are discussed. A less established use of IGC is for the prediction of DPI performance. Although some groups have found a negative relationship between the dispersive surface energy of one formulation component and fine particle delivery, such studies often have a number of limitations. More complex approaches have failed to produce consistent results. Further, more carefully designed, studies are required in this area. In the final section of this article, some areas for on-going research are discussed, including the need to critically assess the best method for the calculation of the specific free energy of adsorption with pharmaceutical materials.

Characterisation and aerosolisation of mannitol particles produced via confined liquid impinging jets.

Mannitol particles, produced by spray drying (SD), have been used commercially (Aridol) in bronchial provocation test. In this study, we propose an alternative method to produce inhalable mannitol powders. The elongated mannitol particles (number median length 4.0microm, and axial ratio of 3.5) were prepared using a confined liquid impinging jets (CLIJs) followed by jet milling (JM). Spray dried and jet milled raw mannitol particles were compared in an attempt to assess the performance of the particles produced by the new method. Aerosol performance of the three different powders (CLIJ, SD, and JM) was relatively poor (fine particle fraction or FPF(loaded) below 15%) when dispersed by the Rotahaler. Dispersion through the Aeroliser led to better aerosol performance of the CLIJ mannitol (FPF(loaded) 20.3%), which is worse than the JM (FPF(loaded) 30.3%) and SD mannitol particles (FPF(loaded) 45.7%) at 60 L/min, but comparable (FPF(loaded) 40.0%) with those of the JM (FPF(loaded) 40.7%) and SD (FPF(loaded) 45.5%) powders at 100L/min. Hence, the optimum use of these elongated mannitol particles can be achieved at increased air flow with a more efficient inhaler. In addition to crystallinity, morphology, and particle size distribution, the surface energies of these powders were measured to explain the differences in aerosol performance. A major advantage of using the CLIJ method is that it can be scaled up with a good yield as the precipitate can be largely collected and recovered on a filter, compared with spray drying which has a low collection efficiency for fine particles below 2microm.

The Influence of Crystal Habit on the Prediction of Dry Powder Inhalation Formulation Performance Using the Cohesive-Adhesive Force Balance Approach

The aim of this investigation was to study the influence of crystalline habit of active pharmaceutical ingredients on the cohesive–adhesive force balance within model dry powder inhaler (DPI) formulations and the corresponding affect on DPI formulation performance. The cohesive–adhesive balance (CAB) approach to colloid probe atomic force microscopy (AFM) was employed to determine the cohesive and adhesive interactions of micronized budesonide particles against the {102} and {002} faces of budesonide single crystals and crystalline substrates of different sugars (cyclodextrin, lactose, trehalose, raffinose, and xylitol), respectively. These data were used to measure the relative level of cohesion and adhesion via CAB and the possible influence on in vitro performance of a carrier-based DPI formulation. Varying the crystal habit of the drug had a significant effect on the cohesive measurement of micronized budesonide probes, with the cohesive values on the {102} faces being approximately twice that on the {002} crystal faces. However, although different CAB values were measured with the sugars with respect to the crystal faces chosen for the cohesive-based measurement, the overall influence on the rank order of the CAB values was not directly influenced. For these data sets, the CAB gradient indicated that a decrease in the dominance of the adhesive forces led to a concomitant increase in fine particle delivery, reaching a plateau as the cohesive forces became dominant. The study suggested that crystal habit of the primary drug crystals influences the cohesive interactions and the resulting force balance measurements of colloid probe CAB analysis.

The relationship between drug concentration, mixing time, blending order and ternary dry powder inhalation performance

Some studies have shown that the mixing order of drug, fines and coarse carrier in a ternary dry powder inhaler (DPI) formulation affects fine particle delivery; others have seen no difference. This was investigated by examining the influence of salbutamol sulphate concentration (0.5-4.5%(w)/(w)), mixing time and blending order (drug and lactose carrier first, then lactose fines; versus fines and carrier first, then drug) on formulation in vitro fine particle delivery. With 15 min of mixing, there was no effect of drug concentration or blending order on fine particle fraction (FPF). With 30 min of mixing, lower drug concentrations produced larger FPFs with the fines and carrier first blending order. Higher drug concentrations resulted in equal performance between the blending orders. With 60 min of mixing, the drug and carrier first blending order resulted in larger a FPF at 0.5%(w)/(w) salbutamol sulphate. The previous conflicting studies used a mixing time of 30 min; these results suggest that their conflicting results may have been due to the use of different drug concentrations. The complexity in the whole dataset suggests that blending order studies are of limited use for the investigation of the mechanism behind the effects of fines.

Following mechanical activation of salbutamol sulphate during ball-milling with isothermal calorimetry.

Formulation of actives for pulmonary delivery with dry powder inhaler devices frequently requires a particle size reduction step. The high-energy forces imparted to a material during milling, as well as reducing particle size, can cause a significant change in physicochemical properties, in particular mechanical activation of the surface (manifested as generation of amorphous regions) which can affect formulated product performance. It is not clear whether particle size reduction occurs prior to, or concomitantly with, generation of amorphous content. In this study the formation of amorphous content with time in crystalline salbutamol sulphate was quantified with isothermal gas perfusion calorimetry as the sample was ball-milled. The data showed that the most particle size reduction occurred initially (d(0.5) dropping from 12.83+/-0.4 to 4.2+/-0.4 within 5 min). During this time period, no detectable amorphous content was observed. Between 5 and 15 min milling time the particle size distribution remained relatively constant but the amorphous content increased non-linearly with time. After 20 min milling time the particle size increased slightly. The data suggest that particle size reduction occurs initially upon application of a force to the crystal. Once maximum particle size reduction has occurred the crystal absorbs the force being applied and the crystal lattice becomes disordered. After extended milling the conditions in the ball mill (heat and/or humidity) may cause crystallisation of some of the amorphous material resulting in particle-particle fusion. It would appear that the ball-milling process could be optimised to achieve the desired particle size distribution but without any loss of crystalline structure.