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Applied Thermodynamics and Heat Engines
                         S.Y. B.Tech. (Production)

                                     Assignment - II

1. Elaborate the concept of thermal contact resistance.

2. Steam at T∞1= 320 °C flows in a cast iron pipe (k = 80 W/m·°C) whose inner and outer
   diameters are D1 = 5 cm and D2 = 5.5 cm, respectively. The pipe is covered with 3-cm-
   thick glass wool insulation with k = 0.05 W/m·°C. Heat is lost to the surroundings at T2 =
   5°C by natural convection and radiation, with a combined heat transfer coefficient of h2 =
   18 W/m2·°C. Taking the heat transfer coefficient inside the pipe to be h1 = 60 W/m2·°C,
   determine the rate of heat loss from the steam per unit length of the pipe. Also determine
   the temperature drops across the pipe shell and the insulation.
                                    (ANS : Q = 121 W, ΔTpipe = 0.02 °C, ΔTinsulation = 284 °C)

3. Define the total and spectral blackbody emissive powers. How are they related to each
   other?

4. Water enters a 2.5-cm-internal-diameter thin copper tube of a heat exchanger at 15 °C at
   a rate of 0.3 kg/s, and is heated by steam condensing outside at 120 °C. If the average
   heat transfer coefficient is 800 W/m2.ºC, determine the length of the tube required in
   order to heat the water to 115 °C.
   (ANS : 61 mtr)

5. Under what conditions is the effectiveness–NTU method definitely preferred over the
   LMTD method in heat exchanger analysis?

6. A 6-m-long section of an 8-cm-diameter horizontal hot water pipe passes through a large
   room whose temperature is 20 °C. If the outer surface temperature of the pipe is 70 °C,
   determine the rate of heat loss from the pipe by natural convection.
   The properties of air at the film temperature of Tf = (Ts + T∞)/2 =(70 + 20)/2 = 45 °C and
   1 atm are :
   k = 0.02699 W/m.°C, Pr = 0.7241
   ν = 1.749 X 10-5 m2/sec, β = 1/Tf = 1/318 K.
   Use the following formula for Nu.
         
                    0.387 Ra D
                                 1/ 6
                                                 
                                                 
    Nu  0.6                            8 / 27 
                                         
                                                                              (ANS : 443 W)
         
               1  (0.559 / Pr) 9 / 16          
                                                 

7. What does the Grashof number physically represent? How does the Grashof number
   differ from the Reynolds number?

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Se prod thermo_assignment 2

  • 1. Applied Thermodynamics and Heat Engines S.Y. B.Tech. (Production) Assignment - II 1. Elaborate the concept of thermal contact resistance. 2. Steam at T∞1= 320 °C flows in a cast iron pipe (k = 80 W/m·°C) whose inner and outer diameters are D1 = 5 cm and D2 = 5.5 cm, respectively. The pipe is covered with 3-cm- thick glass wool insulation with k = 0.05 W/m·°C. Heat is lost to the surroundings at T2 = 5°C by natural convection and radiation, with a combined heat transfer coefficient of h2 = 18 W/m2·°C. Taking the heat transfer coefficient inside the pipe to be h1 = 60 W/m2·°C, determine the rate of heat loss from the steam per unit length of the pipe. Also determine the temperature drops across the pipe shell and the insulation. (ANS : Q = 121 W, ΔTpipe = 0.02 °C, ΔTinsulation = 284 °C) 3. Define the total and spectral blackbody emissive powers. How are they related to each other? 4. Water enters a 2.5-cm-internal-diameter thin copper tube of a heat exchanger at 15 °C at a rate of 0.3 kg/s, and is heated by steam condensing outside at 120 °C. If the average heat transfer coefficient is 800 W/m2.ºC, determine the length of the tube required in order to heat the water to 115 °C. (ANS : 61 mtr) 5. Under what conditions is the effectiveness–NTU method definitely preferred over the LMTD method in heat exchanger analysis? 6. A 6-m-long section of an 8-cm-diameter horizontal hot water pipe passes through a large room whose temperature is 20 °C. If the outer surface temperature of the pipe is 70 °C, determine the rate of heat loss from the pipe by natural convection. The properties of air at the film temperature of Tf = (Ts + T∞)/2 =(70 + 20)/2 = 45 °C and 1 atm are : k = 0.02699 W/m.°C, Pr = 0.7241 ν = 1.749 X 10-5 m2/sec, β = 1/Tf = 1/318 K. Use the following formula for Nu.   0.387 Ra D 1/ 6   Nu  0.6  8 / 27    (ANS : 443 W)   1  (0.559 / Pr) 9 / 16   7. What does the Grashof number physically represent? How does the Grashof number differ from the Reynolds number?