Influence of the switch -over period of an alternately active bi -heater on heat transfer enhancement inside a cavity Anish Pal1 Riddhideep Biswas1 Sourav Sarkar1 Aranyak Chakravarty 2

2025-04-27 0 0 1.02MB 29 页 10玖币
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Influence of the switch-over period of an alternately active bi-heater on
heat transfer enhancement inside a cavity
Anish Pal1,#, Riddhideep Biswas1, Sourav Sarkar1, Aranyak Chakravarty 2,*,
Achintya Mukhopadhyay1
1Department of Mechanical Engineering, Jadavpur University, Kolkata, India
2School of Nuclear Studies & Application, Jadavpur University, Kolkata, India
*Corresponding author: aranyak.chakravarty@jadavpuruniversity.in
#Present affiliation: Department of Mechanical Engineering, University of Illinois at Chicago,
Chicago, USA
Abstract
Increasing power demands on multicore processors necessitate effective thermal management.
The present study investigates natural convection heat transfer inside a square cavity with an
alternately active bi-heater that mimics two cores of a dual-core processor. Pulsating heat flux
condition is implemented on two discrete heaters with a certain switching frequency. The heat
transfer characteristics have been investigated for Prandtl number =0.71 and Rayleigh number
in the range of 103 - 106 using OpenFOAM. The results obtained for alternative active heaters
configuration have been compared with that of the steady single heater and steady double-
symmetric heaters subjected to the same heat flux. The alternately active heater configuration
showed better heat transfer characteristics than a single steady heater for all switchover periods,
and better than a double-symmetric heater for low switchover periods. However, it is found
that for higher values of the switchover period, the maximum temperature of alternately active
heaters configuration touches the temperature of steady single heater. This threshold
switchover period has been determined using a scale analysis. The threshold switchover periods
determined from scale analysis are consistent with the results obtained from numerical
simulations for different Rayleigh numbers and heater lengths.
INTRODUCTION
Technological improvements in computing systems have resulted in increasing usage of
systems with multi-core processors. Along with improvement in computing performance,
multi-core systems generate significantly larger amounts of heat which needs to be
continuously removed. This is only possible with the help of an effective thermal management
system which also ensures longevity of the system. One of the most effective means of ensuring
proper thermal management of such systems is through natural convection. Other means such
as liquid cooling and air-cooled heat sinks, although feasible, increase the cost as well as the
system weight which hinders optimisation [1]. On the other hand, the efficiency of passive heat
removal through natural convection needs to be improved in order to meet the requirements of
heat removal from high power-density electronic components.
A large number of studies are available in literature which investigated natural convective heat
transfer inside a rectangular cavity [2-16]. Several aspects of natural convection heat transfer,
such as heater position, cavity aspect ratio, and non-uniform heat flux, have been studied in
detail. However, many of these studies have considered the heaters at steady-state constant
temperature. A multi-core processor, however, involves switching of jobs between different
cores leading to localized pulsating heating depending on the core usage. Proper
characterization of such multi-core systems, therefore, requires consideration of the transient
pulsating heating of the cores. Studies on the effects of localized pulsed heating are, however,
limited [17]. The resonance effect between contained natural convection and pulsating wall
heating was described by Lage and Bejan [18]. Cheikh et al [19] reported the effect of aspect-
ratio on natural convection in a cavity due to pulsed heating. Bae and Hyun [20] reported heat
transfer enhancement due to implementation of pulsed heating in a vertical rectangular cavity
with three discrete heaters. It was found that transient-stage heating temperatures could exceed
corresponding steady-state values at higher Raleigh numbers. Mahapatra et al. [21] reported
and quantified heat transfer enhancement associated with pulsed heating employing constant
temperature conditions for the heater. Furthermore, the analysis shows that a decrease in time
period results in increased heat transfer.
In the present study, a pulsating heat flux boundary condition is imposed on the heaters (instead
of a constant temperature condition) inside a bottom heated square cavity. This emulates the
job scheduling between the cores of a dual core processor. Study has been conducted for a
range of Ra (104 to 106) for three different heater characteristics - alternately active heater,
steady asymmetric and steady double asymmetric heater. The major objective of this work is
to identify a suitable range of the switchover time period for the alternately active heaters for
which the heat transfer can be augmented. Furthermore, it is worth mentioning that the limited
studies that have reported heat transfer enhancement due to implementation of pulsed heating
have not mentioned the minimum switch-over frequency that needs to be maintained in order
to obtain the heat transfer augmentation. Proper quantification of the minimum switchover
frequency is imperative because not adhering to this minimum frequency of alteration will not
provide any heat-transfer augmentation. The work not only implements a pulsating heat flux
boundary, which is a more authentic representation of the heaters than studies involving a
temperature boundary condition, but also endeavours to enumerate the switchover frequency
that keeps the maximum system temperature below the permissible limit in the cavity for any
combination of Ra and heater length. A rigorous scale analysis has been carried out in this work
to ascertain this minimum switching frequency. This information allows the designer to
determine the cooling rate of the electronic equipment with an aim to estimate the optimum
switchover time for maximum possible heat transfer. The results of this analysis would provide
the necessary information for better scheduling of jobs on a multi-core processor to ensure
maximum heat transfer within the permissible junction temperature limit.
PROBLEM DESCRIPTION
Physical configuration and assumptions
The modelled system of heaters and the associated flow domain is depicted in Fig. 1 for the
various configurations studied. The heaters represent the cores of a dual core processor and are
assumed to be present on the bottom wall of a square cavity. The side walls of the cavity are
kept isothermal at a lower temperature, while the top and bottom walls of the cavity are
assumed to be adiabatic. All cavity walls are assumed to be rigid and impermeable.
Three different heater configurations are considered. The first configuration (Case 1, Fig. 1a)
pertains to the case of alternate switching of heaters. Two heaters (H1 and H2) of equal length
( & ) and placed apart at a distance (  are alternatively subjected to uniform
heat flux i.e., at a particular instant of time, only a single heater is active. Active condition of a
heater corresponds to the imposition of uniform heat flux, while in inactive state the heater is
subjected to adiabatic boundary condition. The alternate activation and deactivation of the
heaters is shown in Fig. 2 as a pulse graph. The second configuration (Case 2, Fig. 1b)
corresponds to steady, double symmetric heaters with both heaters remaining active for the
entire duration. Besides the heaters, all other conditions remain similar to Case 1. In order to
ensure that equivalent thermal energy is supplied to the domain as that in Case 1, each of the
two heaters are considered to be half the length ( of that considered in the Case 1
( such that  
. The third configuration (Case 3, Fig. 1c) considers
a single steady asymmetric heater with the heater length ( being same as that in Case
1.
The working fluid is considered to be laminar and incompressible with constant isotropic and
homogenous thermo-physical properties. The contributions of radiative heat transfer and
viscous dissipation are neglected in the energy balance. Boussinesq approximation is utilised
for modelling the natural convective effects.
Governing Equations and Boundary conditions
The governing equations for conservation of mass, momentum and energy in the cavity are
formulated based on the assumptions made and are represented by Eqs. 1-4.


 (1)







 (2)






 (3)




 (4)
The following scaling parameters are used to obtain the dimensionless form of the equations
(Eqs. 6-9)




 (5)

 



 (6)





 (7)





 (8)




 (9)
摘要:

Influenceoftheswitch-overperiodofanalternatelyactivebi-heateronheattransferenhancementinsideacavityAnishPal1,#,RiddhideepBiswas1,SouravSarkar1,AranyakChakravarty2,*,AchintyaMukhopadhyay11DepartmentofMechanicalEngineering,JadavpurUniversity,Kolkata,India2SchoolofNuclearStudies&Application,JadavpurUni...

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Influence of the switch -over period of an alternately active bi -heater on heat transfer enhancement inside a cavity Anish Pal1 Riddhideep Biswas1 Sourav Sarkar1 Aranyak Chakravarty 2.pdf

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