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Problem 1
(Thermal Conductivity and the Mechanisms of Energy Transport)

Predict the thermal conductivity of methane at 110.4 atm and 1270F by the following
method:
   Use Fig.9.2-1. Obtain the necessary critical properties from Appendix E.
   Use the Eucken formula to get the thermal conductivity at 1270F and low pressure.
   Then apply a pressure correction by using Fig.9.2-1
   (Cp, CH4 = 8.35 cal/mol.K)


Problem 2
(Principles of Heat Flow in Fluids)

                                  3
   Water at 100C flowing in a       -in. 16 BWG condenser tube and saturated steam at
                                  4
1050C condensing on the outside. hi = 12 kW/m2.0C, ho = 14 kW/m2.0C, km = 120 W/m.0C
   1) Calculate the overall heat-transfer coefficient based on both inside and outside
      areas ?
   2) Calculate the temperatures of the inside and outside surfaces of the tube ?


Problem 3
(Principles of Heat Flow in Fluids)

        Aniline is to be cooled from 200 to 1500F in a double-pipe heat exchanger having
a total outside area of 70 ft2. For cooling, a stream of toluene amounting to 8600 lb/h at a
                                                                1
temperature of 1000F is available. The exchanger consists of 1 -in. Schedule 40 pipe in
                                                                4
2-in. Schedule 40 pipe. The aniline flow rate is 10000 lb/h.
    1) If flow is countercurrent, what are the toluene outlet temperature, the LMTD, and
       the overall heat-transfer coefficient ?
    2) If flow is parallel, what are they ?
    3) If the overall heat-transfer coefficient is 70 Btu/ft2.h.0F, how much aniline can be
       cooled ?




(Note: Using Appendix to obtain the necessary data for solution)

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Kt Mrs D Problems 1a

  • 1. Problem 1 (Thermal Conductivity and the Mechanisms of Energy Transport) Predict the thermal conductivity of methane at 110.4 atm and 1270F by the following method: Use Fig.9.2-1. Obtain the necessary critical properties from Appendix E. Use the Eucken formula to get the thermal conductivity at 1270F and low pressure. Then apply a pressure correction by using Fig.9.2-1 (Cp, CH4 = 8.35 cal/mol.K) Problem 2 (Principles of Heat Flow in Fluids) 3 Water at 100C flowing in a -in. 16 BWG condenser tube and saturated steam at 4 1050C condensing on the outside. hi = 12 kW/m2.0C, ho = 14 kW/m2.0C, km = 120 W/m.0C 1) Calculate the overall heat-transfer coefficient based on both inside and outside areas ? 2) Calculate the temperatures of the inside and outside surfaces of the tube ? Problem 3 (Principles of Heat Flow in Fluids) Aniline is to be cooled from 200 to 1500F in a double-pipe heat exchanger having a total outside area of 70 ft2. For cooling, a stream of toluene amounting to 8600 lb/h at a 1 temperature of 1000F is available. The exchanger consists of 1 -in. Schedule 40 pipe in 4 2-in. Schedule 40 pipe. The aniline flow rate is 10000 lb/h. 1) If flow is countercurrent, what are the toluene outlet temperature, the LMTD, and the overall heat-transfer coefficient ? 2) If flow is parallel, what are they ? 3) If the overall heat-transfer coefficient is 70 Btu/ft2.h.0F, how much aniline can be cooled ? (Note: Using Appendix to obtain the necessary data for solution)