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Process Equipment and Plant Design

Process Equipment and Plant Design
Thin spherical shells subjected to internal pressure, develop __________ stresses.

Neither A nor B
Radial
Both A & B
Circumferential

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

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

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Process Equipment and Plant Design
Vertical storage vessels are never supported by __________ support.

Lug
Skirt
Bracket
Saddle

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Process Equipment and Plant Design
Ratio of tube length to shell diameter for a shell and tube heat exchanger is

4 : 1 to 8 : 1 for liquid-liquid exchanger
8 : 1 to 12 : 1 for both liquid-liquid and gas-gas heat exchangers
< 4 : 1 for gas-gas exchangers
Both B & C

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Process Equipment and Plant Design
Length to diameter ratio of most rotary driers is in the range of

10 to 20
1 to 2
20 to 30
4 to 10

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Process Equipment and Plant Design
__________ tower is the most suitable gas-liquid contacting device involving highly corrosive fluids.

None of these
Packed
Bubble cap plate
Sieve plate

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