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The vapor from a chlorine vaporizer will contain some liquid droplets. The vaporizer consists of a vertical, cylindrical vessel with a submerged bundle for heating. A vapor rate of 2500 kg/h is required and the vaporizer will operate at 6 bara. Size the vessel to restrict the carryover of liquid droplets. The liquid hold-up time need not be considered, as the liquid level will be a function of the thermal design.
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Equal rates of mass transfer for the production of the fine chemical are required. This is often required for certain types of organic synthesis.
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Prepare the design and evaluation of a new chemical manufacturing process.
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Draw T-S diagram of the cycle.
The potential energy between two atoms A and B are constants and r the interatomic separation distance.
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The atmospheric pressure of 100k Pa acts on the other side of the piston. The gas is heated until the volume is doubled and the final pressure is 500 kPa. Calculate the work done by the gas.
Evaluate particle diameter at different terminal gas velocities
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