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Process Equipment and Plant Design

Process Equipment and Plant Design
Typical static submergence for bubble cap plate column operating at atmospheric pressure may be around

2.5"
50% of the plate spacing
0.5"
5"

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Process Equipment and Plant Design
Steam side heat transfer co-efficient for design consideration under ordinary condition can be assumed to be about __________ kcal/hr.m².°C.

1250
15000
2500
7500

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Process Equipment and Plant Design
The ratio of tube length to shell diameter in case of liquid shell and tube heat exchanger ranges from

6 to 12
3 to 5
2 to 3
4 to 8

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Process Equipment and Plant Design
__________ strain is measured using a 'strain rosetter'.

Volumetric
None of these
Linear
Shear

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Process Equipment and Plant Design
The shell side pressure drop in a shell and tube heat exchanger is maximum for __________ baffle.

Segmental
Disk and ring
Orifice
Independent of the type of

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

80-100
0.1-0.5
1-5
10-20

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