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Fig. 7.8 The clear liquid height, and volumetric liquid hold-up on a tray, as a function of the superficial vapor velocity for: a) 5.7 m diameter column; b) 2.8 m diameter column. The calculations have been carried out for two weir heights hw = 80 and 140 mm. The large black circles denote the chosen design conditions

Superficial gas velocity / [m/s]

Superficial gas velocity / [m/s]

Fig. 7.8 The clear liquid height, and volumetric liquid hold-up on a tray, as a function of the superficial vapor velocity for: a) 5.7 m diameter column; b) 2.8 m diameter column. The calculations have been carried out for two weir heights hw = 80 and 140 mm. The large black circles denote the chosen design conditions

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