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Thermal-Hydraulic Performance of Printed Circuit Heat Exchanger in ...

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Head loss <strong>in</strong> PCHE<br />

∆p<br />

=<br />

ρg∆H<br />

=<br />

115 o 100 o<br />

∑<br />

m<br />

ρ K<br />

m<br />

b<br />

U<br />

2<br />

2<br />

m<br />

+<br />

∑<br />

m<br />

ρ 0.316Re<br />

m<br />

−0.25<br />

loss <strong>in</strong> elbows + loss <strong>in</strong> a straight pipe<br />

La<br />

U<br />

md 2<br />

2<br />

m<br />

I. K b =K 1 *K 2 *K 3<br />

from <strong>Hydraulic</strong> Eng<strong>in</strong>eer<strong>in</strong>g, A.<br />

II.<br />

from <strong>Hydraulic</strong> Eng<strong>in</strong>eer<strong>in</strong>g, A. Lencastre, , 1987<br />

from JSME Textbook, 2003<br />

III. CFD FLUENT<br />

:<br />

∆<br />

p calc<br />

∆p<br />

− ∆p<br />

exp<br />

exp<br />

= 14 − 37%<br />

2⎛θ<br />

⎞<br />

4⎛θ<br />

⎞<br />

∆p K = 0.946s<strong>in</strong> ⎜ ⎟ + 2.047s<strong>in</strong> ⎜ ⎟<br />

:<br />

calc<br />

− ∆pexp<br />

= 6 − 32%<br />

b<br />

⎝ 2 ⎠ ⎝ 2 ⎠<br />

∆pexp<br />

: N/A yet<br />

2005/1/5 Tokyo Institute <strong>of</strong> Technology 17

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