1. Introduction

3. CALCULATION OF CONCENTRIC TUBES HEAT EXCHANGERS

3.1. Calculation hypothesis

Here the hypothesis used in mathematical models of concentric tubes heat exchangers or double tube:

1- It works with stationary regime.

2- The temperature is based on the length.

3- Kinetic ∆E is approximately 0 ( with the same diameter pipe, will have the same rate all the time).

4- ∆E potential is approximately 0 ( It doesn't matter if the pipe is horizontal or vertical).

5- Heat (q) of radiation is approximately 0 ( Non-radiating materials and non-radiating fluids).

6- The physical properties of fluids are constant with temperature.

7- The convection coefficient (h) is not a function of temperature.

8- The global coefficient of heat pass (U) are not a function of temperature.

9- Working with adiabatic conditions (no heat exchange with the environment).

2. Configurations of heat exchangers
3. Calculation of concentric tubes heat exchangers
3.1. Calculation hypothesis
3.2. Mathematical model counter configuration
3.3. Matematical model parallel configuration
3.4. Calculation general of concentric tubes heat exchangers
3.5. Diagrams of temperature distribution
3.6. Comparison counter flow-parallel flow
  3.7. Example 1
  3.8. Example 2
  3.9. Test
4. General methods of calculation of heat exchangers

5. Test

6. Nomenclature
7. References  
 

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