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Process Equipment and Plant Design

Process Equipment and Plant Design
In case of a shell and tube heat exchanger, the effect of L/D on inside film heat transfer co-efficient (hi) vanishes after a Reynold number of

10000
3000
1000
5000

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Process Equipment and Plant Design
Optimum reflux ratio in a continuous distillation column is determined by the

Total cost consideration (fixed cost of the column plus the cooling water & steam cost)
None of these
Flooding limit of the column
Maximum permissible vapour velocity

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Process Equipment and Plant Design
Vertical vessels are not supported by

Skirts
Saddles
Brackets
Columns

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Process Equipment and Plant Design
Safety valves are provided in chemical equipments to guard against excessive

Temperature
Noise
Pressure/pressure fluctuation
Turbulence

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Process Equipment and Plant Design
In a shell and tube heat exchanger having square pitch, the shell side equivalent diameter is given by (where, P = pitch, d = outside diameter of the tube)

(P² - πd²/4)/πd
Πd/4P²
4(P² - πd²/4)/πd
4P²/πd

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

Bulk modulus
Modulus of elasticity
Modulus of rigidity
None of these

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