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Process Equipment and Plant Design

Process Equipment and Plant Design
The absorption factor is defined as (where, S₁ = slope of the equilibrium curve, S₂ = slope of the operating line)

S₂/S₁
S₁.S₂
1/S₁.S₂
S₁/S₂

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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.

19
28
16
38

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Process Equipment and Plant Design
Flanges are connected to pipes by

Brazing
All of these
Screwing
Welding

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Process Equipment and Plant Design
Spherical shaped pressure vessel is considered to be the most ideal, because it can

Be supported very easily
Be fabricated very easily
Withstand higher pressure for a given metallic shell thickness
Be designed without wind load considerations

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Process Equipment and Plant Design
Thickness of the frame of a plate and frame filter as compared to that of plates is

Either A or B
Less
Same
More

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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.

1.25
3.5
2.5
1.75

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