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Process Equipment and Plant Design

Process Equipment and Plant Design
Steam is preferred to be used as a heating medium in heat exchangers, because of its

High film co-efficient
High latent heat
Non-corrosive condensate
Low cost

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Process Equipment and Plant Design
Any shell opening greater than 5 cms for a storage tank must be reinforced for reason of

Preventing the local overstressing of the shell around the opening
None of these
Reduction of discontinuity in shape at the junction
Making the joint leak proof

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Process Equipment and Plant Design
An underdesigned steam trap will

Waste steam
None of these
Destroy itself of acceleration wear due to rapid recycling
Back up condensate and cause water hammer in steam line

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Process Equipment and Plant Design
The ratio of down take area to cross-sectional area of the tube, for calendria type evaporator ranges from

1.5 to 2
0.5 to 1
1 to 1.5
2 to 2.5

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Process Equipment and Plant Design
Power required for agitation depends upon the

Size of agitator & the tank
Height & properties of the liquid
Agitator type & speed of agitation
All of these

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Process Equipment and Plant Design
In the agitators, the power required will be changed with the increase of diameter of agitator (D) as

D
D²
D⁹
D⁵

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