Short note
AN EXACT FORMULA FOR CALCULATING THE TOTAL HEAT
FLUX TRANSFERRED BY AN INFINITE CYLINDRICAL FIN

 

R.M.S. GAMA, J.J. PEDROSA   and   M.R. NIGRI

Mechanical Engng. Department, Rio de Janeiro State University, Brazil .

Corresponding author: R. M. S. Gama rsgama@terra.com.br, rogerio.gama@eng.uerj.br

Cite this article as: 

Gama, R.M.S., Pedrosa, J.J., Nigri, M.R. (2022) “An exact formula for calculating the total heat flux transferred by an infinite cylindrical fin”, Latin American Applied Research 52(3), pp 235-237.


Abstract-- This note presents an explicit formula for evaluating the total heat flux in an infinite cylindrical fin. The formula is valid even for nonlinear descriptions, especially when the thermal conductivity depends on the temperature and when thermal radiation can not be neglected.

Keywords-- Nonlinear ordinary equation, unbounded domain, exact result.

I. INTRODUCTION

The steady-state heat transfer process in a fin is usually described by a boundary value problem, involving a second-order ordinary differential equation.

Many times the descriptions are non-linear (especially when thermal conductivity depends on the temperature, when there exists radiation heat transfer, or when there exists natural convection in porous fins) and the calculation of the total heat flux requires a considerable effort, since, in general, the authors look for determining the temperature distribution for, in a second step, evaluating the heat flux.

Nevertheless, when the fin is cylindrical and may be considered infinite, the heat transferred from/to the fin can be calculated in a very simple and exact way, even when the heat transfer process is described by a nonlinear differential equation.

II. METHODS

Let us begin considering the problem below, which describes the heat transfer process in an infinite cylindrical fin (Incropera and Dewitt, 1996)

                                   (1)

in which  depends on  (usually an absolute temperature) in such a way that

                               (2)

=constant,

and the function  (thermal conductivity) is a function such that (Arpaci, 1966; Woodcraft, 2005, Gama, 2017)

                          (3)

for any , ,  constants.

      Taking into account that the heat flux along the fin is always nonzero, let us write, from Eq. (1), the following equation

                          (4)

that enables us to write the following separable differential equation (Wylie, 1975)

                              (5)

yielding

    (6)

in which  the (unique) root of . Since it is expected that, when , we reach the thermal equilibrium, the following holds

                                        (7)

Now, let us take into account that the original problem represents a mathematical description of a cooling fin (the case in which  ). In such case, the temperature must be a non-increasing function of the position  and, therefore

 at .   (8)

Equation (8) may be improved in order to describe heating fins too. Aiming to do this, we can rewrite Eq. (8) as follows

 at . (9)

in which  when  and  when .

The total heat transferred by the fin is easily, and without the need of knowing the temperature distribution, obtained from

                                  (10)

in which  is the sectional area of the fin.

III. SOME EXAMPLES

The most classical problem involving cylindrical fins is the linear one in which  is a constant and the governing equation may be written as

In this case, we have one of the most known results in heat transfer (Incropera and Dewitt, 1996). The temperature distribution is given by

                                   (12)

The total heat flux (transferred by the fin) is given by the well-known result below

Using Eq.(10) we obtain (note that, here, ) one of the most known results in heat transfer (Holman 1976)

                            (14)

The above results refer to a situation in which the thermal conductivity does not depend on the temperature. Nevertheless, Eq. (10) allows the calculation of the total heat, directly, even when the thermal conductivity is temperature-dependent. In other words, we can calculate, directly, the total heat flux even if  is the solution of

,                    (15)

 at

 at .

For instance, suppose that  in which  is a positive constant (representing the thermal conductivity for  and   is a constant different from zero. In this case, Eq. (15) is a nonlinear problem whose solution seems to be very difficult to be obtained. Nevertheless, the total heat flux is easily obtained from Eq. (10) as follows

                       (16)

Despite  is a non-zero constant, it is interesting to evaluate the limit of the above expression as . Aiming to this, we have

            (17)

An interesting description is found in the article of Gorla and Bakier (2011), which considers a porous cylindrical fin. The governing equation employed in that paper may be represented as (the authors considered only temperatures above  and constant thermal conductivity)

         (18)

 at

 at .

in which   and   are positive constants.

The cases considered by Gorla and Bakier (2011) involving infinite fins, were approximated by a numerical scheme, using boundary conditions and choosing a large .

With the result presented here, no numerical scheme is necessary and the total heat flux for an infinite fin is exactly reached, even if the thermal conductivity was assumed temperature-dependent. The total heat flux for the problem (Gorla and Bakier, 2011), when , is given (exactly) by

            (19)

      

IV. NUMERICAL APPROXIMATION

Many times the integral that appears in Eq. (10) requires the use of a numerical approximation. Despite the original problem involves an unbounded domain, the integration is carried out between two finite temperatures. So, Eq. (10) can always be approximated by a numerical integration formula (Wylie ,1975).

This common procedure makes the calculation of the total heat flux even simpler to be carried out, even in situations involving complicated functions.

V. CONCLUSIONS

Many authors spent a lot of time and effort evaluating the total heat flux in infinite cylindrical fins. Even so, the obtained results, many times, lie far from the exact result, since the considered fins are very long, but finite and the solutions usually are obtained with the aid of numerical schemes involving second-order differential equations and two boundary conditions. These schemes were used in Kiwan (2007), Darvish et al. (2013), Waseem et al. (2020) and Li and Pang (2020).

The exact solutions obtained by Moitsheki et al. (2020) also involve only finite fins, but consider temperature-dependent thermal conductivity. The dependence of thermal conductivity on the temperature must be considered in all cases involving large temperature variations (Goldberg et al., 2001).

The extremely simple and special result presented here provides the most efficient tool for determining the total heat flux in an infinite fin with temperature dependent thermal conductivity.

It is to be noticed that infinite fins consist of a bound for finite fins and the knowledge of the total heat transferred by an infinite fin is an important information.

ACKNOWLEDGMENT

The author R. M. S. Gama, gratefully, acknowledge the support provided by Brazilian Agency CNPq (Grant 306364/2018-1). The authors acknowledge the partial support provided by the Brazilian Agency CAPES (Finance code 001).

REFERENCES

Arpaci, V.S. (1966) Conduction Heat Transfer. Addison-Wesley Publishing Company, Massachusetts.

Darvish, M.T., Gorla, R.S.R. and Khani, F. (2013) Natural convection and radiation in porous fins. International Journal of Numerical Methods for Heat & Fluid Flow, 23, 1406-1420.

Gama, R. M. S. (2017) Closed-form formulae for the Kirchhoff transformation assuming a piecewise constant temperature dependent thermal conductivity. Latin American Appl. Research. 47, 53-57.

Goldberg, Y., Levinshtein, M.E. and Rumyantsev, S.L. (2001) Silicon Carbide (SiC) Properties of Advanced Semiconductor Materials GaN, AlN, SiC, BN, SiC, SiGe. Levinshtein, M.E., Rumyantsev, S.L., Shur, M.S. (Eds.) John Wiley & Sons, Inc.

Gorla, R.S.R. and Bakier, A.Y. (2011) Thermal analysis of natural convection and radiation in porous fins. Int. Comm. Heat and Mass Transfer, 38, 638-645.

Holman, J. P. (1976) Heat Transfer, Mcgraw-Hill. New York.

Incropera, F. and Dewitt, P.D. (1996) Introduction to Heat Transfer. 3rd edition. John Wiley & Sons Inc. New York.

Kiwan, S. (2007) Effect of radiative losses on the heat transfer from porous fins. Int. J. Thermal Sci. 46, 1046-105.

Li, W and Pang, Y. (2020) Application of Adomian decomposition method to nonlinear systems. Adv.Differ Equ. 2020, 67.

Moitsheki, R. J., Hayat, T. and Malik, M.Y. (2010) Some exact solutions for a fin problem with a power law temperature-dependent thermal conductivity. Nonlinear Analysis: Real World Applications. 11, 3287-3294.

Waseem, W., Sulaiman, M., Islam, S., Kumam, P., Nawaz, R., Raja, M. A. Z., Farooq, M. and Shoaib, M. (2020) A Study of Changes in Temperature Profile of Porous Fin using Cuckoo search Algorithm, Alexandria Engineering Journal. 59, 11-24.

Woodcraft, A. (2005) Recommended values for the thermal conductivity of aluminium of different purities in the cryogenic to room temperature range, and a comparison with copper. Cryogenics. 45, 626-636.

Wylie, C.R. (1975) Advanced Engineering Mathematics, 4th Edition, McGraw-Hill Kogakusha.

 

Received: October 3, 2021

Sent to Subject Editor: November 20, 2021

Accepted: January 13, 2022

Recommended by Subject Editor Fabio Giannetti