Article | REF: BE9517 V1

Heat exchangers – Thermal rating and sizing.

Authors: André BONTEMPS, Jean-François FOURMIGUé

Publication date: October 10, 2014, Review date: August 24, 2021

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ABSTRACT

In this article, the principles of the sizing of a heat exchanger together with that of rating an existing heat exchanger are given. Two approaches are described, an analytical one and a numerical approach. In the analytical approach, the two main methods are proposed: the so-called LMTD (Logarithmic Mean Temperature Difference) method more adapted to sizing and, the effectiveness – NTU (Number of Transfer Units) method more adapted to rating. For numerical approach, after some bases about numerical methods, the emphasis is put on examples of utilization showing the given help to the analysis of sizing and possible conception mistakes (distribution, internal geometries, heat transfer intensification…)

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AUTHORS

  • André BONTEMPS: Professor Emeritus - Geophysical and industrial flows laboratory (LEGI) - Joseph Fourier University

  • Jean-François FOURMIGUé: Engineer – Researcher - French Atomic Energy and Alternative Energies Commission - This article is an updated version of the [B 2 340] article previously written by A. BONTEMPS, A. GARRIGUE, Ch. GOUBIER, J. HUETZ, Ch. MARVILLET, P. MERCIER and R. VIDIL.

 INTRODUCTION

The tools available to the engineer for sizing a heat exchanger or evaluating the performance of an existing exchanger are very numerous, and the choice may seem very difficult. In fact, they all complement each other and can be used successively when sizing a unit.

Analytical methods are all that's needed to size a heat exchanger, or to evaluate the performance of a heat exchanger already defined within the framework of an industrial process already well mastered and a range of conventional equipment already used on a similar process. This is the type of method on which manufacturers' tools are based. The advantage they offer is that they draw on databases of performance, pressure losses and exchange coefficients, based on measurements carried out on their exchangers. The two main methods described in this article are the DTML (logarithmic mean temperature difference) method, which is better suited to sizing, and the – NUT (number of transfer units) efficiency method, which is better suited to evaluating the heat transfer of an already defined exchanger.

Numerical simulation comes later, when we move away from conventional configurations, particularly for fluids and operating regimes, and when problems may arise in terms of distribution or local heat exchange. Simulations can then provide much more detailed information, with 1D, 2D or 3D representation of flows and heat transfers.

A table of notations and symbols is included at the end of the article.

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KEYWORDS

  |     |   cryogenic   |   petrochemistry


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