VASAVI COLLEGE OF ENGINEERING (Autonomous)
IBRAHIMBAGH, HYDERABAD – 500 031
DEPARTMENT OF MECHANICAL ENGINEERING
B.E. VI Semester (Main) Examinations, May-June 2023
Heat Transfer (PE-II)
Time: 3 hours Max. Marks: 60
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Note: Answer all questions from Part-A and any FIVE from Part-B
Part-A (10 x 2 = 20 Marks)
- Define thermal conductivity and write its units.
- What is meant by critical thickness of insulation?
- Define fin efficiency and fin effectiveness.
- What is lumped system analysis?
- What are the advantages of dimensional analysis?
- What is the physical significance of Nusselt number?
- Define condensation and boiling.
- State Stefan Boltzmann’s law of radiation.
- What is a radiation shield?
- Define shape factor.
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Part-B (5 x 8 = 40 Marks)
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a) Derive the general heat conduction equation in Cartesian coordinates.
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b) A furnace wall is made up of three layers of thicknesses 25 cm, 10 cm and 15 cm with thermal conductivities of 1.65, K and 9.2 W/mK respectively. The inner surface is at 850°C and the outside surface is at 100°C. If the temperature at the interface of the first two layers is 550°C, determine the value of K and the percentage of total heat resistance.
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a) Derive an expression for temperature distribution and heat dissipation in a straight fin of rectangular profile for the case when the fin is infinitely long.
b) A steel rod (k = 32 W/mK), 12 mm in diameter and 60 mm long, with an insulated end is to be used as a spine. It is exposed to surroundings with a temperature of 60°C and a heat transfer coefficient of 55 W/m2K. Determine the fin effectiveness and the heat dissipation from the fin.
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a) Explain the significance of dimensionless numbers:
i) Reynolds number ii) Prandtl number iii) Grashoff number iv) Stanton number
b) A horizontal steam pipe of 50 mm diameter is placed in a room at 20°C. The outside surface temperature of the pipe is 134°C. Determine the heat loss per unit length of the pipe by free convection. Use the correlation: Nu = 0.53(Gr.Pr)1/4
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a) Differentiate between forced and free convection.
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b) Air at 20°C flows over a flat plate at a velocity of 3 m/s. The plate is 2.8 m long and 1.5 m wide. Calculate the following: i) Boundary layer thickness at the trailing edge of the plate ii) Total drag force iii) Total heat transfer from the plate, if the plate is maintained at 60°C.
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a) Differentiate between Film wise and Drop wise condensation.
b) A vertical plate 400 mm high and 200 mm wide is to be used to condense saturated steam at atmospheric pressure. If the plate temperature is maintained at 80°C, calculate the condensation rate and the heat transfer rate.
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a) State and prove Kirchhoff’s law of radiation.
b) Two large parallel plates with emissivities 0.5 and 0.8 exchange heat. Find the percentage reduction in heat transfer when a polished aluminum radiation shield of emissivity 0.04 is placed between them.
- Write short notes on any two of the following:
a) Fouling factor
b) Shell and tube heat exchanger
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c) Transient heat conduction
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