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Process Equipment and Plant Design

Process Equipment and Plant Design
The difficulty of liquid distribution in packed towers is accentuated, when the ratio of tower diameter to packing diameter is

> 20 < 50
< 30
< 7
> 7 < 15

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

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

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Process Equipment and Plant Design
Lug support is

Provided usually for vessels of much smaller height than skirt supported vessels
Same as bracket support
The most suitable for thick vertical vessel
All of these

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Process Equipment and Plant Design
Most of the storage vessels/tanks are made cylindrical, because of the fact that a cylinder

Both A & B
Neither A nor B
Has greater structural strength
Is easy to fabricate

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Process Equipment and Plant Design
Rotary driers are most economically designed for the number of heat transfer units (HTU) from

0.01 to 1
5 to 10
1.5 to 2.5
10 to 20

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

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

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