Problem statement: Based on Case problem I, present the results in terms of:
1) Total pressure drop vs. gas mass flow rate (discriminate: liquid mass flow rate); [Chart edition options will be exposed here]2) Total pressure drop vs. liquid mass flow rate (discriminate: liquid composition)
3) Total pressure drop vs. gas superficial velocity (discriminate: pressure) for liquid mass flow rate of 10 +/- 1% kg/m2s (9.9-10.1 kg/m2s)
4) For glass beads of 1.3 mm nominal diameter, establish an approximate total pressure drop value for nitrogen-water downflow at 10 bars for gas mass flow rate approaching 1 kg/m2s.
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