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Process Equipment and Plant Design

Process Equipment and Plant Design
Baffles may be eliminated for

Low viscosity liquids (< 200 poise)
High viscosity liquids (> 600 poise)
Large diameter tanks
None of these

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

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

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Process Equipment and Plant Design
The design stress, which is more than the damaging stress, is the least unit stress that will render a member unfit for service before the end of its normal life. The design stress factor or factor of safety indicates the margin between design stress and the __________ stress.

Working
Damaging
Allowable
None of these

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Process Equipment and Plant Design
Apex angle of conical heads used in the bottom heads of chemical process equipments is usually

60°
30°
75°
45°

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Process Equipment and Plant Design
Lug support is

Same as bracket support
All of these
Provided usually for vessels of much smaller height than skirt supported vessels
The most suitable for thick vertical vessel

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Process Equipment and Plant Design
The practical representative values of HETP for a number of commercial operations lies within a range of __________ metre.

0.2-0.5
1.2-1.5
0.1-0.2
0.4-0.9

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