The pressure drop across a perforated-pipe distributor for turbulent flow conditions is given using the following correlation: 4 fL V? - 2K P AP = 3D Net pressure drop over the length of the distributor (N/m2) Pipe length (m) Diameter (m) Fanning friction factor (dimensionless) Distributor inlet velocity (m/s) Constant (dimensionless) Density in kg/m3 ere: ДР %3 D %3D f V; K %3D Demonstrate that the two sides of the above equation are dimensionally consistent. IL || || || || ||

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