Code No.: 320353 III B.Tech II-Semester Examinations April 2003
OR
HEAT TRANSFER (Mechanical Engineering)
2.a) b)
3.a) b)
4.a)
What is critical thickness of insulation on a small diameter wire or pipe, explain its physical significance and derive an expression for the same. Calculate the rate of heat loss for a red brick wall of length 5m, height 4m, and thickness 0.25m, the temperature of the inner surface is 1100C and that of the outer surface is 400C. The thermal conductivity of red brick k = 0.70 w/m-0k. Calculate also the temperature at an interior point of the wall, 20cm distance from the inner wall. Derive an expression for heat flow through a sphere and prove that if the thickness of the sphere is small it can be taken as a flat slab. A steam pipe 20cm outer diameter is covered with 2.5cm thick layer of insulation material with an average thermal conductivity of 0.08 w/m-0k. The temperature of the pipe surface is 4000C and that of the outer surface of insulation is 500C. Find the loss of heat from a length of 10 meters of the pipe line. What is lumped capacity? What are the assumptions for lumped capacity analysis? Define Reynolds, Nusselt, Prandtl and Stanton numbers. Explain their importance in convective heat transfer.
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b)
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b)
Explain why the conductivity of metals decreases and conductivity of insulating material increases with increases in temperature. A metallic plate, 3cm thick is maintained at 4000C on one side and 1000C on the other side. How much heat is transferred through the plate? Take k for the metallic plate as k=370 w/m-0k.
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1.a)
Max. Marks: 70 Answer any FIVE questions All questions carry equal marks Use of heat transfer data books are permitted ---
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Time: 3 Hours
5.a)
Aj
b)
Discuss briefly thermal and hydrodynamic boundary layer and obtain Reynold’s analogy in forced convection. A plate 20cm height and 1m wide is placed in air at 200C. If the surface of the plate is maintained at 1000C calculate the boundary layer thickness and local heat transfer coefficient at 10cm from the leading edge. Also calculate the average heat transfer coefficient over the entire length of the plate.
Contd…2
Code No.: 320353
7.a) b)
8.a)
b)
Using dimensional analysis obtain an expression for Nusselt number in terms of Reynolds and Prandtl numbers. A light oil with 200C inlet temperature flows at the rate of 500 Kg/minute through 5cm inner diameter pipe which is enclosed by a jacket containing condensing steam at 1500C. If the pipe is 10 meter long, find the outlet temperature of the oil. State and explain Kirchhoff’s identity. What are the conditions under which it is applicable? Assuming the sun to be black body at a temperature of 57000C calculate (i) The emissive power of the surface of the sun. (ii) Wavelength for maximum spectral intensity. (iii) Heat energy emitted by the sun per unit time assuming its diameter as 1.391 109m.
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b)
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6.a)
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Distinguish between (i) A black body and gray body (ii) Absoptivity and emissivity of the surface. Write short notes on (i) Wein’s-displacement law. (ii) Steafon-Boltzman law.
320353 III B.Tech II-Semester Examinations April ...
4.a) What is lumped capacity? What are the assumptions for lumped capacity · analysis? b) Define Reynolds, Nusselt, Prandtl and Stanton numbers. Explain their importance · in convective heat transfer. 5.a) Discuss briefly thermal and hydrodynamic boundary layer and obtain Reynold's · analogy in forced convection.
b) Derive an expression for the heat loss per square metre of the surface area for a · furnace wall when the thermal conductivity varies with temperature ...
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Code No:320455. III-B.Tech. II Semester Examinations April, 2003 · MICROWAVE ENGINEERING · (Electronics and Communication Engineering) · Time: 3 Hours · Max. Marks: 70 · Answer any FIVE questions · All questions carry equal marks · --- · 1. A two-cav
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