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Process Equipment and Plant Design

Process Equipment and Plant Design
Baffles may be eliminated for

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

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Process Equipment and Plant Design
In a shell and tube heat exchanger, the 'tube pitch' is defined as the

Shortest distance between two adj acent tube holes
None of these
O.D. of the tube for square pitch
Shortest centre to centre distance between adjacent tubes

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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
Low pressure steam (with saturation temperature between 105 to 120°C) is usually used in the vacuum evaporators, which normally employ a vacuum of about __________ mm Hg (referred to a 760 mm mercury barometer).

650
750
450
250

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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
2.5
1.75
3.5

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Process Equipment and Plant Design
The ratio of linear stress to linear strain is termed as the

Modulus of elasticity
Bulk modulus
Modulus of rigidity
None of these

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