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Process Equipment and Plant Design

Process Equipment and Plant Design
__________ head is the most economical for cylindrical vessels designed for operating at high pressure (> 15 atm.).

Ellipsoidal
Hemispherical
Conical
Dished

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Process Equipment and Plant Design
In which of the following evaporators, steam is fed inside the tube while the liquor is outside the tube?

Short tube vertical evaporator
Long tube vertical evaporator
Horizontal tube evaporator
None of these

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

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

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Process Equipment and Plant Design
Hold up of material in a operating rotary drier is in the range of

0.8 to 0.9
0.5 to 0.8
0.05 to 0.15
0.25 to 0.50

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Process Equipment and Plant Design
Vertical vessels are not supported by

Brackets
Saddles
Columns
Skirts

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Process Equipment and Plant Design
Hoop (circumferential) stress induced in a thin walled 'Horton Sphere' used for the storage of liquid ammonia under pressure is

pD/6t
pD/3t
pD/4t
pD/2t

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