The effects of upstream velocity profile on the performance of orifice
flowmeters were studied. Non-swirling maldistributed axial velocity p
rofiles were obtained using a concentric pipe flow conditioner. Orific
e flowmeters with beta ratios of 0.43, 0.50, 0.60, 0.70 and 0.75 were
installed downstream of the flow conditioner and operated at a Reynold
s number of 54 700 in a 50.4 cm pipe. Increasing the flow along the ce
ntreline of the pipe decreased the pressure drop across the orifice pl
ate, resulting in increased discharge coefficients. The opposite was o
bserved as the flow along the pipe centreline was decreased. The error
s increased with increasing beta ratio. A swirl generator was installe
d upstream of the beta = 0.43 and 0.50 orifice plates. The swirl produ
ced effects opposite to the axial velocity. The change in discharge co
efficient increased with decreasing beta ratio.