Evaluation of total volume flow rate for multiphase flows is still a great challenge in spite of the numerous efforts documented in the last fifty years. This works presents the results of an experimental characterization of two-phase, water-very viscous oil flows through Venturi and Nozzles flow meters. The fluids under consideration are tap water (density = 998 kg/m^3, dynamic viscosity = 1.026×10-3 Pa∙s at 20°C) and Milpar 220 oil (density = 910 kg/m^3, dynamic viscosity = 0.9 Pa∙s at 20°C) flowing in standard devices with inlet and throat diameters of 40 and 30 mm, respectively. The investigated range of inlet superficial velocities is 0.45 ≤ Jw ≤ 1.33 [m/s] for water, and 0.25 ≤ Jo ≤ 0.72 [m/s] for oil, including the range between annular and dispersed flow patterns. Experiments have shown that the two-phase mixture through the variable area devices behaves like a homogeneous flow, thus enabling the measurement of the total volume flow rate with average deviations lower than 5%. Furthermore, the detection of the pressure gradient upstream of the device can be used with a suitably developed two-fluid model, in order to determine the water and oil volume fractions, and hence the volume flow rates of the single phases.

Investigation on Venturi and nozzle devices as volume flow meters for two-phase, water-very-viscous oil flows

L. P. M. Colombo;M. Guilizzoni;G. Sotgia
2017-01-01

Abstract

Evaluation of total volume flow rate for multiphase flows is still a great challenge in spite of the numerous efforts documented in the last fifty years. This works presents the results of an experimental characterization of two-phase, water-very viscous oil flows through Venturi and Nozzles flow meters. The fluids under consideration are tap water (density = 998 kg/m^3, dynamic viscosity = 1.026×10-3 Pa∙s at 20°C) and Milpar 220 oil (density = 910 kg/m^3, dynamic viscosity = 0.9 Pa∙s at 20°C) flowing in standard devices with inlet and throat diameters of 40 and 30 mm, respectively. The investigated range of inlet superficial velocities is 0.45 ≤ Jw ≤ 1.33 [m/s] for water, and 0.25 ≤ Jo ≤ 0.72 [m/s] for oil, including the range between annular and dispersed flow patterns. Experiments have shown that the two-phase mixture through the variable area devices behaves like a homogeneous flow, thus enabling the measurement of the total volume flow rate with average deviations lower than 5%. Furthermore, the detection of the pressure gradient upstream of the device can be used with a suitably developed two-fluid model, in order to determine the water and oil volume fractions, and hence the volume flow rates of the single phases.
2017
Proceedings of the 14th International Conference on Multiphase Flow in Industrial Plants
9788888198408
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/11311/1042866
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