presentation on weld
TRANSCRIPT
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N.C.INSTITUTUTE OF TECHNOLO
ISRANA PANIPAT-132107
A SEMINAR PRESENTATION
ON
HEAT EXCHANGER
SUBMITTED TO:
SUBMITTED BY:
MR. MANISH KUMAR
ANUJ
3412303
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Heat Transfer/Heat Exchanger
How is the heat transfer?
Mechanism of Convection
Heat Exchanger
Classification of Heat Exchanger
Classification of direct transfer type Heat Exchanger
Temperature Profile
Log-Mean Temperature Difference
The Effectiveness-NTU Method
Application
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How is the heat transfer?
Heat can transfer between the surface of asolid conductor and the surrounding
medium whenever temperature gradientexists.
Conduction
Convection
Natural convectionForced Convection
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Natural and forced ConvectionNatural convection occurs whenever heat flows
between a solid and fluid, or between fluid layers.
As a result of heat exchange
Change in density of effective fluid layers taken
place, which causes upward flow of heated fluid.If this motion is associated with heat transfermechanism only, then it is calledNaturalConvection
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Forced Convection
If this motion is associated by mechanicalmeans such as pumps, gravity or fans, themovement of the fluid is enforced.
And in this case, we then speak ofForcedconvection.
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A device whose primary purpose is thetransfer of energy between two fluids isnamed aHeat Exchanger.
Heat Exchangers
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CLASSIFICATION OF HEATEXCHANGER
.DIRECT TRANSFER TYPE HEATEXCHANGER
.DIRECT CONTACT TYPE HEATEXCHANGER
.REGENERATIVE OR STORAGE TYPE HEAT
EXCHANGER
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CLASSIFICATION OF
DIRECT TRANSFER TYPEHEAT EXCHANGER
Parallel Flow Cross Flow Counter Current Flow
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Temperature Profiles
T = Approach Temperature
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The closed-type exchanger is the mostpopular one.
One example of this type is the Double pipeexchanger.
In this type, the hot and cold fluid streamsdo not come into direct contact with each
other. They are separated by a tube wall orflat late.
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Log-Mean Temperature Difference
We can also relate the total heat transfer rate to thetemperature difference between the hot and cold
fluids.
.
LM
ch
TUAQ
TTTlet
=
=
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The log mean temperature differencedepends on the heat exchanger
configuration
Th,in
Th,out
Th,in
Tc,in
Th,out
Tc,in
Tc,out
Tc,out
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LMTD Parallel-Flow HX
ocohch
icihch
LMLM
TTTTT
TTTTT
TT
TTTTUAQ
,,2,2,2
,,1,1,1
)12
12
:FlowParallelforWhere
/ln(
==
==
==
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LMTD Counter-Flow HX
Tlm,F! Tlm,PF F"# $%&' : %F %PF
icohch
ocihch
LMLM
TTTTT
TTTTT
TT
TTTTUAQ
,,2,2,2
,,1,1,1
)12
12
:FlowounterforWhere
/ln(
==
==
==
LMTD M l P dC
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LMTD- Multi-Pass and Cross-Flow
%ppl* a correction factor to obtain +&T
t: Tube $ide
CFLMLMLM TFTTUAQ , ==
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The Effectiveness-NTU Method
Define Qmaxfor Cc< ChQmax= Cc(Th,i- Tc,i)
for Ch< CcQmax= Ch(Th,i- Tc,i)
or Qmax= Cmin(Th,i- Tc,i)
Q =Cmin
(Th,i
- Tc,i
)
)(
)(
)(
)(
,,min
,,
,,min
,,
ma- icih
icocc
icih
ohihh
TTC
TTC
TTC
TTC
q
q
=
==
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The Effectiveness-NTU Method
For any heat exchanger:
=f(NTU,Cmin/Cmax)
NTU (number of transfer units) designatesthe nondimensional heat transfer size of theheat exchanger:
minC
UANTU=
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Applications of Heat Exchangers
Heat Exchangers
prevent car engine
overheating and
increase efficiency
Heat exchangers areused in Industry for
heat transfer
Heat
exchangers are
used in AC and
furnaces
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THANK YOU