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2 4 . In an agitated vessel handling a gas - solid - liquid mixture, with a gas holdup of 0 . 0 5 and

24. In an agitated vessel handling a gas-solid-liquid mixture, with a gas holdup of 0.05 and solid holdup of 0.1, calculate the average diameter of gas bubbles and solid particles assuming they have the same size.
25. A packed bed with a cross-sectional area of 0.5 m operates under a liquid superficial velocity of 0.02 m/s and a solid particle size of 3 mm. Find the bed porosity and then estimate the pressure drop per meter of bed height.

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