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Process Equipment and Plant Design

Process Equipment and Plant Design
Hazards associated with the relief valve leakage for extremely hazardous material storage can be taken care of by providing

Dikes
Surge chamber
Rupture diaphragm
None of these

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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.

600
1000
300
1500

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Process Equipment and Plant Design
The ratio of the largest load in a test to the original cross-sectional area of the test specimen is called the __________ stress.

None of these
Breaking
Yield point
Ultimate

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Process Equipment and Plant Design
Optimum economic pipe diameter for fluid flow is determined by the

None of these
Total cost considerations (pumping cost plus fixed cost of the pipe)
Density of the fluid
Viscosity of the fluid

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Process Equipment and Plant Design
A claming section before the liquid flows into the downcomer is privided to

Ensure better vapour-liquid contact
Cool the liquid before it flows down
Permit release of entrained vapour in the liquid
Reduce the discharge fluctuation

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Process Equipment and Plant Design
Speed of the drum of the rotary vacuum filter normally ranges from __________ rpm.

3 to 8
5 to 7
8 to 15
0.1 to 2

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