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Process Equipment and Plant Design

Process Equipment and Plant Design
Welded joint efficiency in the design of chemical process equipment is taken as

0.55
0.95
0.75
0.85

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Process Equipment and Plant Design
Wind load consideration in the design of a support can be neglected, when the vessel is

Short (< 2 m) and housed indoor
Tall (say 30 metres), but is full of liquid
Tall but empty
None of these

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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
Sieve plate
Bubble cap plate
Packed

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Process Equipment and Plant Design
For high pressure process equipments/vessels, the connected nozzle should be

Screwed
Welded
Flanged
Brazed

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Process Equipment and Plant Design
Slope of countercurrent flow rotary drier is in the range of __________ meter/metre.

0 to 0.08
0 to 0.8
0 to 2.2
0 to 1.5

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Process Equipment and Plant Design
Of the pressure vessels, with same thickness but different diameters, which one withstands higher pressure?

Strength of the vessel is same irrespective of the diameter
Larger dia long vessel
Smaller dia vessel
Larger dia vessel

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