Questions 51–57 of 57. Imported answers require independent review unless marked reviewed.

Topic practice 57 questionsPage 6 of 6

Question 36

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Vapour bubbles are formed in the nucleate boiling regime at a frequency of 10 bubbles per second per nucleation site. There are 100 nucleation sites per m² of heating area. The latent heat of vaporization and the density of vapour under the operating condition are 1000 kJ/kg and 1 kg/m³ respectively. The diameter of each bubble is 10⁻³ m. Assume that the entire heat supplied is used for vapour generation. The heat flux (in Watt per m² of heating area) is ______________ (rounded off to third decimal place).

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Question 55

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A hot liquid is to be cooled in a 1-1 shell and tube heat exchanger from 80 °C to 50 °C. Cooling water enters the tube side at 30 °C, and exits at 45 °C. The properties of the liquids are constant. Also, the overall heat transfer coefficient is same for counter-current and co-current modes. The percentage saving in heat transfer area for counter-current option with respect to the area of co-current option is __________ (rounded off to third decimal place).

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Question 12

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The one-dimensional unsteady heat conduction equation is

where

– temperature,

– time,

– radial position,

– thermal conductivity,

– density, and

– specific heat.
For the cylindrical coordinate system, the value of

in the above equation is
Your answerChoose one option.

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Question 13

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In a heat exchanger, the inner diameter of a tube is 25 mm and its outer diameter is 30 mm. The overall heat transfer coefficient based on the inner area is 360 W/m²·°C. Then, the overall heat transfer coefficient based on the outer area, rounded to the nearest integer, is ______ W/m²·°C.

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Question 39

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Let

be the spectral blackbody radiation intensity per unit wavelength about the wavelength

. The blackbody radiation intensity emitted by a blackbody over all wavelengths is
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Question 40

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A fluid flows over a heated horizontal plate maintained at temperature

. The bulk temperature of the fluid is

. The temperature profile in the thermal boundary layer is given by:

Here,

is the vertical distance from the plate,

is the thickness of the thermal boundary layer and

is the thermal conductivity of the fluid. The local heat transfer coefficient is given by
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Question 41

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In nucleate boiling, the pressure inside a bubble is higher than the pressure of the surrounding liquid. Assuming that both the liquid and vapour are saturated, the temperature of the liquid will ALWAYS be
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