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Process Equipment and Plant Design

Process Equipment and Plant Design
for couplings and unions would be

60
350
Negligible
200

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Process Equipment and Plant Design
Skirt support is the most suitable for supporting __________ vessels.

Large horizontal
Small horizontal
Thick walled
Tall vertical

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Process Equipment and Plant Design
Which of the following types of reactors is the safest from operation point of view?

A liquid phase catalytic reactor
A vapor phase reactor
A liquid phase reactor
Pot type reactor

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Process Equipment and Plant Design
Tubes are fixed to the tube sheet (a thick circular metallic plate) by the method of tube rolling and brazing (non-removable) or ferrule connection (removable). Thickness of the tube, sheet is normally __________ the outside diameter of the tube but in no case it should be less than 22 mm (7/8").

Half
Equal to
1.5 times
Three fourth

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Process Equipment and Plant Design
In a shell and tube heat exchanger, tube side __________ of the mass velocity.

Neither A nor B
Both A & B
Pressure drop is proportional to the square
Heat transfer co-efficient is proportional to 0.8th power

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Process Equipment and Plant Design
Cylindrical pressure vessels in horizontal condition is generally supported on a __________ support.

Skirt
Lug
Saddle
Guy wire

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