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Process Equipment and Plant Design

Process Equipment and Plant Design
Nominal size of a pipe is an indication of its __________ diameter.

Inner
None of these
Outer
Approximate

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Process Equipment and Plant Design
Normally, the ratio of the total riser area to the tower cross sectional area (for bubble cap towers of diameter more than 3 ft) is around

0.55-0.85
0.35-0.75
0.1-0.2
0.4-0.6

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Process Equipment and Plant Design
Bubble cap plate column is

Used only for distillation, not for absorption
A finite stage contactor
A differential stage contactor
A continuous contactor

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Process Equipment and Plant Design
The dust collection efficiency of a cyclone separator

None of these
Is inversely proportional to the mass of the dust particle
Is directly proportional to the radius of the dust particle path
Decreases with increase in gas flow rate

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Process Equipment and Plant Design
In a rotary drier, the average retention time of solid is(where Z = length of the drier, metres ρ = apparent solid density, kg/m³ L = flow rate of dry solids, kg/see. m² drier cross-section H = hold up of solid.)

Z.H/L.ρ
H.ρ/L
Z.H.ρ/L
L/Z.H.ρ

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Process Equipment and Plant Design
Tube wall thickness depends on the cor-rosiveness of the fluids and their operating pressure & temperature and is specified by Birmingham wire gauge (B.W.G)-a number which varies from 8 to 18 with the numbers 14 and 16 being more commonly used. Outside diameter of tubes varies from about 15 to 50 mm; however a tube of less than __________ mm outside diameter is generally not recommended for fouling fluids.

16
19
38
28

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