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Process Equipment and Plant Design

Process Equipment and Plant Design
The raio, (properller agitator dia/tank dia) is normally taken as

0.15-030
0.5-0.65
0.75-0.85
0.60-0.90

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Process Equipment and Plant Design
Optimum economic pipe diameter for fluid flow is determined by the

Viscosity of the fluid
Density of the fluid
None of these
Total cost considerations (pumping cost plus fixed cost of the pipe)

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Process Equipment and Plant Design
Skirt support is the most suitable for supporting __________ vessels.

Small horizontal
Tall vertical
Large horizontal
Thick walled

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Process Equipment and Plant Design
Safety valves are provided in chemical equipments to guard against excessive

Temperature
Turbulence
Pressure/pressure fluctuation
Noise

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Process Equipment and Plant Design
For turbine agitator, the impeller diameter is about

0.95 d
0.65 to 0.85 d
0.1 to 0.2 d
0.3 to 0.5 d

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Process Equipment and Plant Design
Slope of countercurrent flow rotary drier is in the range of __________ meter/metre.

0 to 1.5
0 to 0.08
0 to 0.8
0 to 2.2

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