This study utilised a combination of computational fluid dynamics (CFD) and standardised entrainment tubes to investigate the influence of impaction on the break-up and aerosol performance of a model inhalation formulation. A series of entrainment tubes, with different impaction plate angles were designed in silico and the flow characteristics, and particle tracks, were simulated using CFD. The apparatuses were constructed using threedimensional printing. The deposition and aerosol performance of a model agglomerate system (496.3-789.2 :m agglomerates containing 3.91 :m median diameter mannitol particles) were evaluated by chemical analysis and laser diffraction, respectively. Analysis of the mannitol recovery from the assembly and CFD simulations indicated that mass deposition on the plate was dependent on the impactor angle (45 β’ -90 β’ ) but independent of the airflow rate (60-140 Lβ’min -1 ). In comparison, wall losses, perpendicular to the impactor plate were dependent on both the impactor angle and flow rate. Analysis of the particle size distribution exiting the impactor assembly suggested mannitol aerosolisation to be independent of impactor angle but dependent on the air velocity directly above the impactor plate. It is proposed that particle-wall impaction results in initial agglomerate fragmentation followed by reentrainment in the airstream above the impaction plate. Such observations have significant implications in the design of dry powder inhaler devices.