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Process Equipment and Plant Design

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

None of these
Packed
Sieve plate
Bubble cap plate

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

Radial
Circumferential
Neither A nor B
Both A & B

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Process Equipment and Plant Design
Value of Peclet number = ∞, is the representative of

Plug flow
Complete back mixing
Laminar flow
Eddy diffusivity = 0

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Process Equipment and Plant Design
A minimum clearance of about __________ mm is maintained between the distillation column wall and the bubble cap.

76
95
38
19

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

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

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Process Equipment and Plant Design
In case of a shell and tube heat exchanger, the effect of L/D on inside film heat transfer co-efficient (hi) vanishes after a Reynold number of

3000
5000
10000
1000

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