An experimental study of the flow of highly viscous fluids through small diameter orifices was conducted. Pressure drops were measured over a wide range of flow rates for each of nine different orifices, including orifices of 0.5, 1 and 3 mm nominal diameter, with three thicknesses (nominally 1, 2 and 3 mm) tested for each diameter. The data were nondimensionalized to obtain Euler numbers and Reynolds numbers for the aspect ratio range 0.32 < l/d < 5.72, and orifice-to-pipe diameter range 0.023 < p < 0.137. It was found that in the laminar region, increases in aspect ratio resulted in an increase in Euler number at the same Reynolds number, while increases in diameter ratio resulted in an increase in Euler number for a similar aspect ratio. In the transition region, the Reynolds number was less significant in determining Euler number, tending toward a constant value dictated by the diameter ratio and aspect ratio as the flow became progressively turbulent. . The data were correlated using different expressions for the laminar and turbulent regions, which were then combined to yield one continuous function for the Euler number as a function of Reynolds number and the geometric parameters for the entire range of data. The model predicted 84.4% of the data to within ± 25% and is valid for the following range of conditions: 0.32 < l/d < 5.72, 0.023 < p < 0.137, 8