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Process Equipment and Plant Design

Process Equipment and Plant Design
A shell may by termed as thin if its thickness to diameter ratio is less than 0.1. The factor which can be neglected in the calculation of membrane stresses is

Deformation
Bending
Elongation
Shear

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Process Equipment and Plant Design
Baffles may be eliminated for

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

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Process Equipment and Plant Design
Liquid gradient over the tray results due to the

Large reflux ratio
Large plate spacing
Resistance offered to flow of liquids by caps & risers and the flow of gas
Low gas velocity

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Process Equipment and Plant Design
Needle valves are generally not used for

Very accurate flow control
Smaller sizes of pipe
High pressure throttling service
Very large diameter pipes

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Process Equipment and Plant Design
With increase in temperature drop (in a shell and tube heat exchanger), the LMTD correction factor, FT

Decreases very rapidly
Remains constant
Increases very rapidly
Increases linearly

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Process Equipment and Plant Design
Which of the following types of reactors is the safest from operation point of view?

A vapor phase reactor
A liquid phase catalytic reactor
Pot type reactor
A liquid phase reactor

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