1. Introduction

4. GENERAL METHODS OF CALCULATION OF HEAT EXCHANGERS

4.1. Method of factor F

This method uses a correction value F:


Proposing the general equation of heat step:

Insulating Δtm the first equation:

It proposed the 2 thermal balance equations:

Where:

q = heat a fluid that is transmitted to another (J / s)

W1 = mass flow of hot fluid (1) (kg / s)

W2 = mass flow of cold fluid (2) (kg / s)

Cp1 = heat capacity of the hot fluid (1) (J / kg · K)

Cp2 = cold fluid heat capacity (2) (J / kg · K)

T1i = initial temperature of the hot fluid (1) (K)

T10 = final temperature of hot fluid (1) (K)

T2i = initial temperature of cold fluid (2) (K)

T20 = cold end temperature of the fluid (2) (K)

U = convection coefficient (KJ / h · m 2 K)

A = area of the passage of heat (m 2)

∆Tm = logarithmic mean temperature difference

With equations 1, 2 and 16 can find the variables necessary to find the value of F graphically.

This correction value F is a function of R, P and configuration (2:1, 1:1, 2:4, etc.)

Where:

With equations 17 and 18, and the configuration of heat exchanger can go to the chart and find
the value of F.

We can find two types of problems:

- DESIGN PROBLEM.

INFORMATION:

With this information you must be find the area (A0 or Ai).

The steps to follow in order to find this area are:

 

1) Proposed the two heat balance equations to find q:

2) Proposed the general equation of heat step:

 

Insolate area (A0):

Insolate area (Ai):

3) Make diagram of temperature distribution and calculate Δtlog.

4) Calculate R and P:

 

5) Go to the graph and found the two values of R and Q, find F, as shown below
( calculated value of P = 0.6 and R = 1.0):

6) Finally, using the general equation of heat step through the area is calculated
(A0 o Ai):



- HEAT PROBLEM.

INFORMATION:

With this information and using different equations have to find the final temperature
(T10 and T20).

These problems can be solved by groping along the following steps:

-Rough estimate temperature (assume T'10 T'20).

1) Proposed the general equation of heat step:

2) Make the diagram of distribution temperatures and calculate ∆Tlog.

3) Calculate R and P:

 

4) Go to the graph and found the two values of R and P, find F, as shown below ( calculated value of P = 0.6 and R = 1.0):

5) In general equation of heat step, is the value of heat flux (q):

6) Proposed the two equations of thermal balance to find the temperatures:

7) Check the values found are equal to those alleged. Otherwise, they must assume new initial values and repeat the process explained.

- Rough estimate heat flow (we assume q').

1) Proposed the two equations of thermal balance to find the temperatures:

2) Proposed the general equation of heat step:

3) Make the diagram of distribution temperatures and calculate ∆Tlog.

4) Calculate R and P:

5) Go to the graph and with values of R and P, found F.

6) In general equation of heat step, is the value of heat flux (q):

7) Check the values found are equal to those alleged. Otherwise, they must assume new initial values and repeat the process explained.

2. Configurations of heat exchangers
3. Calculation of concentric tubes heat exchangers
4. General methods of calculation of heat exchangers
  4.1. Method of factor F
    4.1.1. Graphs of factor F for different equipment
    4.1.2. Example 1
    4.1.3. Example 2
  4.2. Method ε-NTU

5. Test

6. Nomenclature
7. References

 

© UPC. Universitat Politécnica de Catalunya. EPSEM