Analysis of
Fluid Flow in Axial Re-entrant Grooves with Application to Heat Pipes
by
Scott K. Thomas and
Vikrant Damle
Department of
Mechanical and Materials Engineering
Wright State
University, Dayton, OH 45435-0001
Abstract
The fully developed
laminar flow within a re-entrant groove has been analyzed using a finite
element model. Re-entrant grooves have been used in both axially-grooved heat
pipes and in monogroove heat pipes. The main benefit to using this type of wick
structure is the reduction of the liquid pressure drop along the length of the
groove due to countercurrent liquid-vapor interaction at the meniscus. All
previous researchers assumed that the pressure drop within the liquid could be modelled
as flow within a smooth tube, but the results of the current analysis show that
this assumption can lead to significant errors in the pressure drop prediction.
An extensive literature survey was completed and the results of five previous
studies were used to validate the current numerical model. It was found that
the present finite element model is both more accurate and consumes less
computer resources than a finite difference based model developed previously by
one of the authors of the current manuscript. A parametric analysis was carried
out to determine the Poiseuille number, Po = $f$Re, the dimensionless mean
velocity, $\overline {v^*}$, and the dimensionless volumetric flow rate, $\dot
{V^*}$, as functions of the geometry of the re-entrant groove (groove height
$1.0 \le H^* \le 4.0$, slot half-width $0.05 \le W^*/2 \le 0.9$, fillet radius
$0.0 \le R^*_f \le 1.0$), and the liquid-vapor shear stress ($0.0 \le
-\tau^*_{lv} \le 2.5$). It was determined that the flow variables were strongly
affected by the groove height, slot half-width and liquid-vapor shear stress,
but were relatively unaffected by the fillet radius. The case in which the
meniscus recedes into the re-entrant groove was examined, which could be a
result of evaporator dry-out or insufficient liquid fill amount. The
cross-sectional area of the liquid in the groove, $A^*_l$, the meniscus radius,
$R_m^*$, and the above-mentioned flow variables were calculated as functions of
the meniscus contact angle ($0^\circ \le \phi \le 40^\circ$) and meniscus
attachment point ($0.0 \le H^*_l \le 2.75$). In general, the flow variables
were more strongly affected by the meniscus attachment point than the meniscus
contact angle. Finally, the results of the numerical model were used to
determine the capillary limit of a low-temperature heat pipe with two different
working fluids, water and ethanol, for a range of meniscus contact angles. The
capillary limit heat transfer was found to attain a maximum value in the slot
region and then decreased dramatically when the meniscus receded into the circular
region of the re-entrant groove.