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Process Equipment and Plant Design

Process Equipment and Plant Design
The absorption factor is defined as (where, S₁ = slope of the equilibrium curve, S₂ = slope of the operating line)

S₁/S₂
1/S₁.S₂
S₁.S₂
S₂/S₁

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Process Equipment and Plant Design
Angled baffles are preferred in the agitation tank to control the swirling action; if the viscosity of the liquid to be mixed is about 200 poise. However, the baffle may be completely eliminated for mixing liquids having viscoisty above __________ poise.

1000
600
1500
300

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Process Equipment and Plant Design
In a heat exchanger, shell side fluid velocity can be changed by changing the tube

Neither A nor B
Layout
Pitch
Both A & B

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Process Equipment and Plant Design
The thermal stress in a metallic bar does not depend upon the

Neither A nor B
Both A & B
Cross-sectional area
Changes in temperature

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

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Process Equipment and Plant Design
__________ closure is the weakest enclosure for cylindrical vessels.

Torispherical
Conical or flat plate
Hemispherical
Elliptical

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