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Heat Transfer

Heat Transfer
Steam economy in case of a triple effect evaporator will be

1
Between 0 and 1
> 1
< 1

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Heat Transfer
Boiling point elevation of a solution of NaOH

Is almost independent of temperature
Both B and C
Increases rapidly with temperature rise
Is almost independent of pressure

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Heat Transfer
The outlet temperature of cooling water in a heat exchanger is generally not allowed to exceed above 50°C in industrial practice mainly to avoid

Excessive corrosion
Decrease in heat exchanger efficiency
Uneconomic LMTD
Its evaporation loss

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Heat Transfer
For a counter current heat exchanger with Tih = 80°C, T°c = 60°C, T°h = 50°C and Tic = 30°C, and the temperature difference between the two streams being the same everywhere along Z, the direction of flow of hot fluid. The temperature profile should satisfy

dT/dZ = 0
d²T/dZ² = 0
d²T/dZ² < 0
d²T/dZ² > 0

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Heat Transfer
In case of evaporators, liquid entrainment results primarily due to

high heat transfer rate
foaming of the solution
high heat transfer rate
high vacuum in the evaporator

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Heat Transfer
For turbulent flow in a tube, the heat transfer co-efficient is obtained from the Dittus-Boelter correlation. If the tube diameter is halved and the flow rate is doubled, then the heat transfer co-efficient will change by a factor of

37
1
1.74
6.1

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