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Phase distributions, pressure and velocity profiles together with flow rates for all phases are presented and analysed.
This experimental study examines the detailed Nusselt number (Nu) distributions, pressure drop coefficients (f) and thermal performance factors (TPF) for a square spiral channel with two opposite endwalls roughened by in-line 45° ribs.
In a previous article [1] theoretical predictions of velocity distributions, pressure drops and mean Nusselt-numbers are given for non-isothermal pipe flow of power-law fluids having a temperature dependent consistency-index.
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Simulated temperature distribution, pressure distribution and outlet gas concentrations were validated by the experimental data in 30%O2/70%% CO2 atmosphere.
Velocity distribution, pressure contours, output torque within the flow domain were also characterized.
Numerical simulation is employed to investigate the coolant flow distribution, pressure drop and thermal behavior of different designs.
The relative velocity distribution, pressure distribution and static pressure rise at the design point are obtained for the regular impeller with only long blades and three complex impellers with long, mid or short blades.
Their relative merits with respect to factors like cost, flow distribution, pressure drop and scale-up are discussed.
Holdup distribution, pressure drop, separation efficiencies and droplet separation characteristics of six different wire mesh pads were investigated experimentally.
For both steady and oscillating flows, the bulk and local wall temperature distribution, pressure drop, inlet and outlet temperatures and frequency were measured.
A special study of flow in particular central region of TATSE was carried out by the analysis of the velocity distribution, pressure distribution and partial residence time distribution (RTD).
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