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Process Equipment and Plant Design

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

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

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Process Equipment and Plant Design
For annular flow of a fluid, the ratio of the equivalent diameter for pressure drop calculation to the equivalent diameter for heat transfer calculation is

(d1 + d2)/d1
D1/(d1 + d2)
(d1 + d2)/d2
D2/(d1 + d2)

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Process Equipment and Plant Design
__________ tray arrangement is recommended for distillation column having diameter upto 4 ft.

Split flow
Radial flow
Cross flow
Cascade

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

Linear
Volumetric
None of these
Shear

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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.

2500
1250
7500
15000

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Process Equipment and Plant Design
In a shell and tube heat exchanger having square pitch, the shell side equivalent diameter is given by (where, P = pitch, d = outside diameter of the tube)

4P²/πd
4(P² - πd²/4)/πd
(P² - πd²/4)/πd
Πd/4P²

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