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Process Equipment and Plant Design

Process Equipment and Plant Design
Vertical vessels are not supported by

Brackets
Columns
Skirts
Saddles

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

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

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Process Equipment and Plant Design
The testing pressure of storage tanks and pressure vessels designed as per Indian standard codes should be about __________ times.the design pressure.

1.5 to 2
4 to 5
>5
3 to 4

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Process Equipment and Plant Design
Movement of pipeline caused by thermal expansion is taken care by providing

Changes in its direction
Expansion joint
All of these
Change in the shape of pipeline

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Process Equipment and Plant Design
Pressure drop (Δp) and the superficial gas mass velocity (G) in case of packed absorption tower operating in the preloading range are related as

Δp = G
Δp = G2
Δp = 1/G0.6
Δp = G0.5

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Process Equipment and Plant Design
Minimum tube pitch recommended for shell and tube heat exchangers is about __________ times the outside diameter of the tube.

2.5
1.25
3.5
1.75

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