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Process Equipment and Plant Design

Process Equipment and Plant Design
Steam side heat transfer co-efficient for design consideration under ordinary condition can be assumed to be about __________ kcal/hr.m².°C.

2500
7500
1250
15000

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

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

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Process Equipment and Plant Design
In a multipass shell and tube heat exchanger, the problem of differential expansion between the shell and tube passes is taken care of by using a

Neither A nor B
Either A or B
Floating head tube sheet
U-bend

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Process Equipment and Plant Design
Lug support is

All of these
Provided usually for vessels of much smaller height than skirt supported vessels
Same as bracket support
The most suitable for thick vertical vessel

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Process Equipment and Plant Design
Power required for agitation depends upon the

Agitator type & speed of agitation
All of these
Size of agitator & the tank
Height & properties of the liquid

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Process Equipment and Plant Design
Which of the following factors determine the amount of entrainment in a distillation column?

Vapour velocity in the volume between the plates
Plate spacing
Depth of liquid above the bubble cap slots
All of these

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