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Process Equipment and Plant Design

Process Equipment and Plant Design
Le/D for fully open globe value may be around

10
25
75
300

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Process Equipment and Plant Design
Fouling factor must be included in the calculation of over all design heat transfer coefficient, when the liquid

Is highly viscous
Is of high specific gravity
Containing suspended solids flows at low velocity
Containing suspended solids flows at high velocity

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Process Equipment and Plant Design
for couplings and unions would be

350
Negligible
60
200

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Process Equipment and Plant Design
The distance between the top of the slots and the liquid surface when the static liquid is just ready to flow over the overflow weir is called

Skirt clearance
None of these
Downcomer liquid seal
Static submergence

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Process Equipment and Plant Design
In a shell and tube heat exchanger, the 'tube pitch' is defined as the

O.D. of the tube for square pitch
Shortest centre to centre distance between adjacent tubes
Shortest distance between two adj acent tube holes
None of these

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Process Equipment and Plant Design
In a __________ rivetted joint, the number of rivets decreases from the innermost row to the outermost row.

None of these
Diamond
Chain
Zig-zag

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