CH EN 3453 Heat Transfer 2014 Fall Utah Homework HW 08 Solutions

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Homework 8 – Problem 1 A. Define the following terms: (use symbols and equations if necessary) a. Thermal entrance region b. Hydrodynamic entrance region c. Fully developed flow d. Log mean temperature difference B. Draw a simple diagram of each of the following types of concentric heat exchangers (Chapter 11) . Parallel flow . Counterflow A. Define the following terms: (use symbols and equations if necessary) a. Thermal entrance region For laminar flow: For turbulent flow on the other hand, the entry region is approximated by Nusselt number correlations in Section 8.4.2. b. Hydrodynamic entrance region For laminar flow: and for turbulent flow: c. Fully developed flow Once a flow is characterized as ‘fully developed’ (and remains that way), the thermal and physical properties seize changing. This includes density and even the convective heat transfer coefficient. d. Log mean temperature difference For external flow (bank of tubes): (i=in, o=out) For heat exchangers: (h=hot, c=cold, i=in, o=out) B. See Figure 11.1

Transcript of CH EN 3453 Heat Transfer 2014 Fall Utah Homework HW 08 Solutions

Page 1: CH EN 3453 Heat Transfer 2014 Fall Utah Homework HW 08 Solutions

Homework 8 – Problem 1 A. Define the following terms: (use symbols and equations if necessary)

a. Thermal entrance region b. Hydrodynamic entrance region c. Fully developed flow d. Log mean temperature difference

B. Draw a simple diagram of each of the following types of concentric heat exchangers (Chapter 11)

e. Parallel flow f. Counterflow

A. Define the following terms: (use symbols and equations if necessary)

a. Thermal entrance region For laminar flow:

For turbulent flow on the other hand, the entry region is approximated by Nusselt number correlations in Section 8.4.2.

b. Hydrodynamic entrance region For laminar flow:

and for turbulent flow:

c. Fully developed flow Once a flow is characterized as ‘fully developed’ (and remains that way), the thermal and physical properties seize changing. This includes density and even the convective heat transfer coefficient.

d. Log mean temperature difference For external flow (bank of tubes): (i=in, o=out)

For heat exchangers: (h=hot, c=cold, i=in, o=out)

B. See Figure 11.1

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