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

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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 thermal stress in a metallic bar does not depend upon the

Cross-sectional area
Changes in temperature
Neither A nor B
Both A & B

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

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

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Process Equipment and Plant Design
Generally, no corrosion allowance in wall thickness of a part is required, if the thickness is more than __________ mm.

10
5
30
20

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Process Equipment and Plant Design
The normal range of velocity of water in pipes is __________ m/sec.

10-50
15-30
0.1-0.5
1-2

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