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Process Equipment and Plant Design

Process Equipment and Plant Design
The distance between the centre of a rivet hole to the nearest edge of the plate is called

None of these
Pitch
Margin
Back pitch

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Process Equipment and Plant Design
Heat transfer co-efficient, hG(Kcal/hr.m² .°C) and mass velocity of air, G (kg/hr.m² ) for air flow parallel to the surface in case of constant drying rate in batch drying is related as hG = 0.0176G0.8. But when the flow of air perpendicular to the surface is encountered, this equation changes to

1.004G0.8
HG = 1.004G0.37
0.0176G1.37
HG = 0.0176G0.37

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

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

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Process Equipment and Plant Design
Ratio of tube length to shell diameter for a shell and tube heat exchanger is

< 4 : 1 for gas-gas exchangers
8 : 1 to 12 : 1 for both liquid-liquid and gas-gas heat exchangers
Both B & C
4 : 1 to 8 : 1 for liquid-liquid exchanger

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Process Equipment and Plant Design
Maximum plate efficiency is achieved in case of __________ flow.

Cascade
Split
Cross
Reverse

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Process Equipment and Plant Design
Lap joints are preferred for plates having thickness __________ mm.

> 5
< 12.5
43961
> 3

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