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Optimization and Computational Fluid Dynamics - Department of ...

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228 Marco Manzan, Enrico Nobile, Stefano Pieri <strong>and</strong> Francesco Pinto<br />

∆T =(Tbi) h − (Tbo) c =(Tbo) h − (Tbi) c<br />

(8.22)<br />

U is the global heat transfer coefficient, <strong>and</strong> A is a reference heat transfer<br />

surface, that has been taken as twice the projection <strong>of</strong> the interface wall on<br />

the horizontal plane, A =2· Ah. This choice allows the comparison <strong>of</strong> heat<br />

transfer coefficients for different surface geometries.<br />

8.4 Numerical Methods<br />

The numerical solution <strong>of</strong> the 2D <strong>and</strong> 3D wavy channel case was carried out by<br />

means <strong>of</strong> the COMSOL s<strong>of</strong>tware package [9]. Full details <strong>of</strong> the methodology<br />

have been previously published elsewhere [30] <strong>and</strong> are summarized hereafter.<br />

For the numerical simulation <strong>of</strong> the CC heat exchanger module, the ANSYS-<br />

CFX CFD package has been employed. Hexahedral structured grids have<br />

been generated by means <strong>of</strong> the ICEM-CFD grid generation package.<br />

8.4.1 <strong>Fluid</strong> Dynamic Iterative Solution<br />

For the wavy <strong>and</strong> CC channels the fluid dynamic equations are solved in a<br />

similar way. As shown in Eq. (8.5), a forcing term β appears, due to the pressure<br />

splitting introduced in Eq. (8.4). Since the Reynolds number is a given<br />

constant <strong>of</strong> the problem, the non-dimensional mean velocity in the channel<br />

must be unitary. It is, therefore, necessary to find the correct value <strong>of</strong> β that<br />

ensures this condition. Other authors [31] have used proportional-integrative<br />

iterative controls to reach the correct value <strong>of</strong> the pressure gradient, starting<br />

from a trial value. At first, a similar approach has been attempted, but it<br />

proved to be not very efficient in converging to the correct value <strong>of</strong> β, <strong>and</strong><br />

this can be a limiting factor for CPU-intensive optimization studies.<br />

By the definition <strong>of</strong> the friction factor f as the non-dimensional surface<br />

shear stress [49], it is easy to show by applying the second Newton’s law that:<br />

f = β Dh<br />

1<br />

2 ρU2 av<br />

. (8.23)<br />

Recall that, for internal flows in laminar regime, the friction factor is proportional<br />

to the inverse <strong>of</strong> the Reynolds number. From the definition <strong>of</strong> Re, it<br />

follows that:<br />

β ∝ Uav . (8.24)<br />

This relation is not strictly valid in channels with varying cross section, but<br />

nevertheless it is expected a proportionality law such as:

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