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Process Equipment and Plant Design

Process Equipment and Plant Design
Cooling water fouling factors vary in the range of 0.001 to 0.003

(BTU/hr.ft² . °F)⁻¹
(kcal/hr.m² .°C)⁻¹
(W/m².°K)⁻¹
(kcal/hr. m. °C)⁻¹

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Process Equipment and Plant Design
Which tube arrangement in a heat exchanger would facilitate highest heat transfer rate?

Diagonal square pitch
Triangular pitch
Heat transfer rate is independent of tube arrangement
Square pitch

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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)
Flooding limit of the column
None of these
Maximum permissible vapour velocity

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Process Equipment and Plant Design
Any shell opening greater than 5 cms for a storage tank must be reinforced for reason of

None of these
Making the joint leak proof
Reduction of discontinuity in shape at the junction
Preventing the local overstressing of the shell around the opening

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Process Equipment and Plant Design
For storing hazardous chemicals in large storage tanks, the minimum safe distance between the two tanks should range between __________ times the tank diameter.

1 to 1.5
2.5 to 3.5
4 to 5
6 to 8

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Process Equipment and Plant Design
Log mean temperature difference in case of multi-pass shell and tube heat exchanger is always

Both B & C
Less than arithmetic mean value
More than arithmetic mean value
More than geometric mean value

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