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The following are the key points: Transient, Diffuse Gray, Fin Efficiency, Heat Transfer Steady, Heat Generation, Thermal Conductivity, Medium Constant, Diffuse Gray, Minimum Fin Spacing, Solar Absorptivity
Typology: Exams
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Instructions: Answer Question 1 and any FOUR other questions.
Examiners: Mr. W. Corr Mr. P. Clarke Prof. M. Gilchrist
Q1. (i) Consider a medium in which the heat conduction equation is given in its simplest form as:
2 0 2 2 r ∂∂ rT + ∂∂ T r =
Q2. (a) Distinguish clearly between the effectiveness and the efficiency of a heat transfer fin. (3 marks) (b) (i) Steam at 120°C flows through 30mm OD thin-walled pipe as shown below. Circumferential aluminium fins (thermal conductivity 180 W/m.K) of D60 mm, WT 2mm and S 3mm are proposed as shown. The overall heat transfer coefficient to the surroundings at 25°C is 60 W/m^2. Determine:
Q3. (a) Describe the essential assumption underlying lumped capacitance modelling and the two system characteristics which flow therefrom. (4 marks) (b) Show that the step response of such a system can be modelled as a 1st^ order transient with
(c) A person, fully clothed, is found dead at 5 pm in a room whose temperature is 20°C. The temperature of the body is measured to be 25°C when found and the heat transfer coefficient is estimated to be 8 W/m^2 .K. Modelling the body as a 300mm diameter, 1700mm long cylinder: (i) Estimate the time of death (6 marks) (ii) Comment on the validity of your analysis (3 marks) (iii) If the body were found nude, how will your result change? (2 marks)
Assume near-water properties for the corpse: 1000 kg/m^3 ; 0.62 W/m.K; 4.2 kJ/kg.K
Q6. Air at 100 kPa and 10°C flows across a bank of tubes 15 rows high and 5 rows deep at a velocity of 7 m/s measured at a point in the flow before the air enters the tube bank. The surfaces of the tubes are maintained at 65°C. The diameter of the tubes is 25 mm; They are arranged in an in-line manner so that the spacing in both the normal and parallel directions to the flow is 37.5 mm. Calculate: (i) The heat transfer coefficient for the bundle (8 marks) (ii) The exit temperature of the air (6 marks) (iii) The total heat transfer per unit length of bundle (6 marks) Refer to Tables 6.1 and 6.
− M Cp
Ash Te Ts ( Ts Ti ) exp &
Q7. (a) Air at 27°C and 1 atm flows over a flat plate at a speed of 2 m/s. Calculate the boundary-layer thickness at distances of 0.2 and 0.4 m from the leading edge of the plate. The viscosity of air at 27°C is 1.85 x 10 -5^ kg/ms. Assume unit depth in the z direction. (8 Marks) (b) Assume that the plate is heated over its entire length to a temperature of 60°C. Calculate the heat transferred in (i) the first 0.2 m of the plate, and (6 marks) (ii) the first 0.4 m of the plate. (6 Marks)
Refer to Table 7