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Process Equipment and Plant Design

Process Equipment and Plant Design
Friction factor for turbulent flow in a new pipe is given by

f = 16/NRe
f = 0.22 NRe0.05
f = 0.04/NRe0.16
f = 25/NRe

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Process Equipment and Plant Design
Needle valves are generally not used for

Smaller sizes of pipe
Very accurate flow control
High pressure throttling service
Very large diameter pipes

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Process Equipment and Plant Design
In a shell and tube heat exchanger, the overall heat transfer co-efficient is proportional to the tube side (volumetric flow rate)0.8. This is valid, only when the ratio of the tube side film resistance to the total resistance is almost equal to

2
1
∞
20.8

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Process Equipment and Plant Design
Welded joint efficiency in the design of chemical process equipment is taken as

0.75
0.85
0.95
0.55

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Process Equipment and Plant Design
In a shell and tube heat exchanger, the shortest centre to centre distance between the adjacent tubes is

Always less than the diameter of the tube
None of these
Called tube clearance
Called tube pitch

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Process Equipment and Plant Design
The stress developed in a material without any permanent set is called the

Breaking stress
Yield stress
Ultimate stress
Elastic limit

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