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Overall, the present study proves the existence of a mass velocity threshold above which identical heat transfer performances are achieved regardless of orientations.
They inferred a mass velocity using mapped erupted mass (Wallace et al. 2013) and measured eruption durations, whereas we used a value based on the analysis of infrasound data.
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The concept of a mass-velocity interaction diagram is proposed for shear damage evaluation of RC beams under impact.
The pressure drop characteristics of steam-water two-phase flow at a low mass velocity in a four-head rifled tube were experimentally studied under an adiabatic condition with pressure ranging from 11.3 to 21.5 MPa, mass velocity ranging from 250 to 1200 kg/m2 s, and steam quality ranging from 0 to 1.
This paper deduced formulas of the sensitivity coefficient of flow and output enthalpy, and made a heat sensitivity analysis for the vertical water wall of a 600 MW supercritical pressure W-shaped flame boiler at a low mass velocity when heat disturbance occurs.
From the infrasound signal, we calculated a peak mass velocity of 315 m s-1 (Fig. 1 b).
It is found that a critical mass velocity (G_cr) exists under supercritical pressure conditions, which is much similar to the cases at subcritical pressure conditions.
Since the heat per unit of mass for the full tube length increases with either an increase in heat flux or a decrease in mass velocity and tube diameter, the transition always occurs at smaller vapor qualities with the increase of the heat per unit of mass during the transition of the three flow patterns.
The results indicate that a drying thermal efficiency of 50% is available at the typical drying temperatures in the mate industry (100 °C) if a value of mass velocity in the order of 0·1 kg m−2 s−1 is set.
The recorded infrasound signals, de-trended and high-pass filtered (0.1 Hz) for removal of very long-period noise/drift (a, c), and calculated mass velocity profiles (b, d) for event 2 (a, b), and event 17 (c, d).
The heat removal rate is re-evaluated as a function of air mass velocity at the inlet of heat transfer tube banks.
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