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Local mass transfer coefficient increased with the inlet liquid flow rate.
It is found that the inlet liquid flow rate is the dominating factor influencing the liquid distribution.
In the experiment, the range of inlet gas superficial velocities was 0.01 16.668 m/s, and the inlet liquid superficial velocity was 0.01 6.945 m/s.
The velocity and mixture gas density distributions in channels are discussed and plotted at various locations for an inlet liquid flow rate of 0.3 cc min−1.
Reducing inlet liquid temperature can improve the filling performance in normal gravity, but cannot significantly reduce the maximum pressure in microgravity.
Three different designs of liquid distributor were used to examine the effect of inlet liquid distribution on holdup distribution inside the column.
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The user specifies the air inlet and liquid inlet conditions.
The effective parameters considered for optimization were air inlet velocity, liquid inlet velocity, bubble diameter, and viscosity.
At the inlet the liquid contains species A dissolved in it.
The effects of heat transfer fluid (HTF) flow rate, HTF inlet temperature, liquid PCM volume fraction, complete discharging time, discharging capacity of the tank, and temperature distribution in direct contact TES tank are investigated.
At ambient conditions, a change in the volumetric inlet gas-liquid ratio from 0 to 580 m3 NTP m−3 was necessary to achieve a similar reduction in liquid hold-up.
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