A process has a distillation column, where a crude dichlorobenzene is pumped from a storage tank. Nitrogen is used to blanketing the column and the pressure above the liquid surface is held constant at 0.1 bar gauge pressure. The minimum depth of liquid in the tank is 1 m. The distillation column operates at a pressure of 500 mmHg. The feed point to the column is 16 m above the base of the tank. The tank and column are connected by a 50 mm internal diameter commercial steel pipe, 220 m long. The pipe run from the tank to the column contains the following valves and fittings: 20 standard radius 90° elbows: two gate valves to isolate the pump an orifice plate and a flow-control valve. If the maximum flow-rate required is 20,000 kg/h, calculate the pump motor rating (power) needed. Take the pump efficiency as 70 per cent and allow for a pressure drop of 0.5 bar across the control valve and a loss of 10 velocity heads across the orifice. (Density of the dichlorobenzene 1300 kg/m3, viscosity 1.4 cp).
A process has a distillation column, where a crude dichlorobenzene is pumped from a storage tank. Nitrogen is used to blanketing the column and the pressure above the liquid surface is held constant at 0.1 bar gauge pressure. The minimum depth of liquid in the tank is 1 m. The distillation column operates at a pressure of 500 mmHg. The feed point to the column is 16 m above the base of the tank. The tank and column are connected by a 50 mm internal diameter commercial steel pipe, 220 m long. The pipe run from the tank to the column contains the following valves and fittings: 20 standard radius 90° elbows: two gate valves to isolate the pump an orifice plate and a flow-control valve. If the maximum flow-rate required is 20,000 kg/h, calculate the pump motor rating (power) needed. Take the pump efficiency as 70 per cent and allow for a pressure drop of 0.5 bar across the control valve and a loss of 10 velocity heads across the orifice. (Density of the dichlorobenzene 1300 kg/m3, viscosity 1.4 cp).
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