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Process Equipment and Plant Design

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

0.5 - 1.0
43833
0.01 - 0.5
0.07 - 0.12

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Process Equipment and Plant Design
Frame thickness in the plate and frame filter press is normally in the range of __________ inches.

1 to 12
0.25 to 4
1 to 5
0.25 to 8

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Process Equipment and Plant Design
Rotary driers are most economically designed for the number of heat transfer units (HTU) from

5 to 10
10 to 20
1.5 to 2.5
0.01 to 1

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Process Equipment and Plant Design
Fouling factor must be included in the calculation of over all design heat transfer coefficient, when the liquid

Containing suspended solids flows at low velocity
Is highly viscous
Containing suspended solids flows at high velocity
Is of high specific gravity

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Process Equipment and Plant Design
Lug support is meant for supporting __________ vessels.

Small
Tall but empty
Large horizontal cylindrical
Thick walled tall

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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.

1250
7500
15000
2500

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