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Process Equipment and Plant Design

Process Equipment and Plant Design
Baffles may be eliminated for

Large diameter tanks
High viscosity liquids (> 600 poise)
Low viscosity liquids (< 200 poise)
None of these

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Process Equipment and Plant Design
It is not desirable to design a heat exchanger for LMTD correction factor, FT, of less than

0.8
0.99
0.55
0.95

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Process Equipment and Plant Design
The ends of a cylinderical vessel can be closed by a head, which can be one of the four shapes. For the same thickness, choose the one which can withstand the highest pressure.

Flat plate
Ellipsoidal
Torispherical
Hemispherical

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Process Equipment and Plant Design
for couplings and unions would be

Negligible
350
60
200

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Process Equipment and Plant Design
Steam economy is defined as the amount of evaporation per unit amount of steam used, while the capacity is the total evaporation obtained per hour. Use of multiple effect in evaporation

Increases capacity
Increases economy
Both B & C
Does not affect the capacity

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Process Equipment and Plant Design
Removable connection of tubes to tube sheet is called

Nipple
Ferrule
Saddle
Socket

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