State Fourier’s law of heat conduction? Mention the significance of negative sign in heat conduction equation.
[3 marks]Differentiate Critical thickness of Insulation and Optimum thickness of Insulation
[4 marks]Describe the different kind of Boundary conditions used in heat transfer studies
[7 marks]An electrically heated plate dissipates heat by convection at a rate of q = 8000 W/m2 into ambient air at T = 25 °C. If the surface of hot plate is at T = 125 f W °C. Calculate heat transfer coefficient for convection between plate and air.
[3 marks]What is lumped System analysis? Mention the importance of Biot number in lumped system analysis.
[4 marks]Develop expression for one dimensional steady state temperature distribution T(r) in a sphere where inner surface at r = a and outer surface of r = b of hollow sphere are maintained at temperatures of Tand Trespectively.12 Consider that thermal conductivity (k) of sphere is constant
[7 marks]Atmospheric air at T = 400 Kwith a velocity u = 1.5 m/s flows over a flat plate L = 2 m long maintained at uniform temperature of T = 300K. W Calculate average value of heat transfer coefficient and average heat transfer rate from airstream to plate over entire length of L = 2m.
[7 marks]Write the significance of following dimensionless numbers used in heat transfer studies (i) Reynolds number (ii) Prandtl number (iii) Nusselt number
[3 marks]Differentiate velocity boundary layer and thermal boundary layer
[4 marks]Estimate the total heat loss by convection and radiation from an unlagged steam pipe, 50 mm o.d. at 415 Kto air at 290K (17 °C). Emissivity e = 0.90 Film coefficient for calculation of heat loss by natural convection is given by h = 1.18 (T/D )0.25 W/m2K C O
[7 marks]Mention the factors governing the rate of heat transfer in forced and natural convection.
[3 marks]Define Absorptivity, Reflectivity and Transmissivity
[4 marks]Calculate heat transfer area of 1 – 2 heat exchanger from the following data. Inlet and outlet temperatures of cold fluid are 303 Kand 318 Krespectively. Overall heat transfer coefficient = 4100 W/m2 K. Heat loss = 407 kW. LMTD correction factor = 0.84.1
[7 marks]What is drop wise condensation? Explain why heat transfer coefficient is lesser for film wise condensation than drop wise condensation?
[3 marks]With neat diagrams explain classification of heat exchangers according to flow arrangement.
[4 marks]Aheat exchanger is required to cool 20 kg/s of water from 360K to 340K by means of 25kg/s of water entering at 300K. If the overall heat transfer coefficient is 2000 W/m2K. calculate the surface area required in
[7 marks]Acounter current concentric heat exchanger
[ marks]Aco-current flow concentric tube heat exchanger. (Take Cof water P = 4.187 kJ/kg K)
[ marks]Discuss the phenomena of hysteresis in a boiling curve.
[3 marks]Why saturated steam is used as heating medium in industries?
[4 marks]What is understood by boiling point elevation in evaporators
[3 marks]What is Vapor recompression? Mention different methods in which vapor recompression can be done.
[4 marks]With help of boiling curve mention different regimes in a pool boiling.
[7 marks]Define the terms of Capacity & Economy in Evaporators
[3 marks]Explain the different methods of feeding of multiple effect evaporators.
[4 marks]An evaporator operating at atmospheric pressure is designed to concentrate 5% solute to 20 % solute by weight at a rate of 5000 kg/h. Dry saturated steam at a pressure corresponding to saturation temperature of 399K is used. The feed is at 298 Kand boiling point rise is 5 K. Overall heat transfer coefficient is 2350 W/m2 K. Calculate economy of evaporator and area of heat transfer to be provided assuming that there is no boiling point elevation for the solvent. Data: Latent heat of Condensation of steam = 2185 kJ/kg Latent heat of vaporization of water at 101.325 kPa and 373 K = 2257 kJ/kg Specific heat of feed = 4.187 kJ/ kg K
[7 marks]Describe the significance of - NTU method for heat exchange analysis.
[7 marks]