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This thesis addresses the detailed numerical investigation of double di usive mixed convection
ow within ventilated enclosures equipped with di erent thermal and solutal boundary
conditions. Geometric modulations are included by considering di erent sizes and
locations of inlet port, outlet port, heat sources and contaminant sources. The
ow of
uid, heat and contaminants are analyzed by streamlines, isotherms and isoconcentrations
for a wide range of
ow governing parameters. The trends of average Nusselt number,
Sherwood number, entropy generation and cooling e ciency are investigated with the
variation of Reynolds number, Richardson number and buoyancy ratio to improve the
performance of the ventilated system.
In this thesis, two air distribution forms are studied: one is displacement ventilation
and other is mixing ventilation to drive and control the indoor air environment. The
mathematical model is formulated based on the pre-assumptions that the
uid is Newtonian,
viscous and incompressible and the
ow is laminar. A control volume based SIMPLE
algorithm is used to solve the
ow governing equations, that are represented by a coupled
set of non-linear partial di erential equations. Chapter-1 of the thesis includes the basic
de nitions and various solution algorithms used for
uid
ow problems.
Chapter-2 deals with the double di usive mixed convection
ow inside a ventilated
enclosure due to the presence of thermosoluted square block at the middle region. The
block is at higher temperature and concentration as compared to the inlet cold
uid
which is at lower temperature and concentration and is passed through various slots of
the left vertical wall and
ush-out through the right vertical wall. E ective heat and mass
transfer performance is studied by changing the locations of inlet and outlet port with the
variation of
ow governing parameters which is mostly applicable for building ventilation
and cooling of equipments. Chapter-3 is focused on the numerical simulation of
uid
i
ii
ow, heat and mass transfer in a ventilated enclosure where a thermo-contaminated square
block is placed inside the enclosure. Simulations are performed for di erent locations and
di erent sizes of the thermo-contaminated block with xed inlet and outlet port along the
vertical walls where coolant air is supplied and contaminated air is
ushed out. The heat
and contaminant transfer rate along the surface of the block are compared for di erent
block locations with the variation of Richardson number, Reynolds number and buoyancy
ratio and found that maximum cooling inside the enclosure is obtained when thermocontaminated
block is placed near the outlet port.
Mixed convection
ow in a parallelogrammic shaped ventilated system lled with air-
CO2 mixture with uniform discrete heat and CO2 contaminant sources is numerically
studied in Chapter-4. The impact of inclination angle of horizontal walls on average
rate of heat transfer and mass transfer, average temperature, entropy generation, Bejan
number, cooling e ciency and performance evaluation criterion inside the system is evaluated
with respect to the location of inlet port, outlet port and heat sources. Chapter-5
is focused on maximizing the removal rate of heat and contaminants due to wall heater
and a thermosoluted block in a slot-ventilated enclosure. Cold fresh air is in ltrated into
the enclosure through an inlet port located along right vertical wall and polluted air is
expelled through the chimney shaped outlet port located along the upper wall. The best
suited inlet port location along with inclination angle of outlet chimney is determined in
terms of maximum heat transfer rate with minimum entropy generation.
Subsequently, a numerical simulation of three-dimensional mixed convection due to
thermosolutal gradients in a slot-ventilated enclosure is presented in Chapter-6 due to
discrete heat and contaminant sources under di erent
ow conditions. The numerical simulations
are performed for a wide range of
ow governing parameters to nd the e ects of
inlet and outlet port locations for achieving acceptable average temperature inside the enclosure
to obtain maximum heat and mass transfer rate with minimum entropy generation. |
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