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Process Equipment and Plant Design

Process Equipment and Plant Design
__________ tower is the most suitable gas-liquid contacting device involving highly corrosive fluids.

None of these
Packed
Bubble cap plate
Sieve plate

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Process Equipment and Plant Design
Le/D for a Tee (used as elbow, entering branch) would be

Both B and C
Less than that for Tee (used as elbow, entering run)
More than that for Tee (used as elbow, entering run)
Around 90

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Process Equipment and Plant Design
Excessive liquid gradient on a tray may result in the

Back trapping
All of these
Gas blowing beneath cap skit
Maldistribution of gas

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Process Equipment and Plant Design
Friction factor for turbulent flow in a new pipe is given by

f = 25/NRe
f = 0.04/NRe0.16
f = 16/NRe
f = 0.22 NRe0.05

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Process Equipment and Plant Design
Pressure drop per tray in the atmospheric distillation column is about __________ psi.

0.01 - 0.5
0.5 - 1.0
0.07 - 0.12
43833

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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
>5
3 to 4
4 to 5

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