Heat and Thermodynamics Introduction
Heat and Thermodynamics
Introduction
Definitions! Internal energy
! Kinetic and potential energy! Joules
! Enthalpy and specific enthalpy! H= U + p x V! Reference to the triple point! Engineering unit ! H is the work done in a process! J, J/kg
More Definitions
! Work! Standard definition W = f x d! In a gas W = p x V
! Heat! At one time considered a unique form of
energy! Changes in heat are the same as changes
in enthalpy
Yet more definitions! Temperature
! Measure of the heat in a body! Heat flows from high to low temperature! SI unit Kelvin
! Entropy and Specific Entropy! Perhaps the strangest physics concept! Notes define it as energy loss! Symbol S! Units kJ/K, kJ/(kgk)! Entropy increases mean less work can be done by
the system
Sensible and Latent Heat! Heat transfers change kinetic or
potential energy or both! Temperature is a measure of kinetic
energy! Sensible heat changes kinetic (and
maybe potential energy)! Latent heat changes only the potential
energy.
Sensible Heat
! Q is positive for transfers in! c is the specific heat capacity ! c has units kJ/(kgC)
)( if ttcmQ =
Latent Heat
! Heat to cause a change of state (melting or vaporization)
! Temperature is constant
m
v
lmQlmQ==
Enthalpy Changes
! Enthalpy changes take into account both latent and sensible heat changes
hmQ =
Thermodynamic Properties of H2O
TemperatureC
Specific enthalpy
100C
SuperheatedSteam
Latent heat
Wet steam
Sensible heat
Subcooledliquid
Saturatedsteam
Saturatedliquid
Saturation temp
Pressure Effects
Laws of Thermodynamics
! First Law! Energy is conserved
! Second Law! It is impossible to convert all of the heat
supplied to a heat engine into work! Heat will not naturally flow from cold to hot! Disorder increases
Heat Transfer
Radiation
4TAQ
Conduction
TlAkQ =
l
AT1T2
More Heat Transfer
Convection
Mass Flow
TAhQ =
Condensation
Latent heat transfer from vapor
Daltons Law
If we have more than one gas in a container the pressure is the sum of the pressures associated with an individual gas.
...321 +++= PPPPc
Condensing Heat Exchanger
CoolantIn
CoolantOut
SteamIn
WaterOut
P
T
P=PsaturationT=Tsaturation
Non-Condensables in Heat Exchanger
CoolantIn
CoolantOut
SteamIn
WaterOut
P
T
P=Psaturation+PgT=Tsaturation
Condenser AppearsSubcooled
For You to do
HTS Normal Operation
Reactor Thermal Power
Fuelbundle/
HTS
Moderator
End shield/shield tank
QSCQM
Bleed cooler
Boiler
PreheaterBoiler
blowdown
Feedwater
HT pump
2nd stage Reheatdrains
Steam toturbine
Feed & bleedQL
Pipingloses
QP
QHT
Reactor Power and T
! T is an indicator of reactor power if boiling is not taking place
TcmQ =
! At boiling T stops changing! In boiling channels total enthalpy
increase must be calculated
Fuel Safety
! No overpowering! Adequate cooling
Fuel Heat Transfer
D
A
Critical heat flux
Singlephase
convection
Nucleateboiling Partial film boiling Full film boiling (dryout)
S
u
b
c
o
o
l
e
d
b
o
i
l
i
n
g
S
a
t
u
r
a
t
e
d
(
b
u
l
k
)
b
o
i
l
i
n
g
Tsheath = Tsat
L
o
g
(
h
e
a
t
f
l
u
x
)
CF
Log (Tsheath Tcoolant)
B
Tcoolant = Tsat
E
Two new terms
! Critical Heat Flux! CHF! The maximum heat flux nucleate boiling
can transfer
! Dryout! When dry patches of vapor exist on the
fuel sheath
Uniform Heating
Inlet Outlet
Tcoolant
Single-phase
convection
Subcoolednucleateboiling Saturated nucleate (bulk) boiling Dryout
Tsheath surface
Tsat
Fuel element
Coolant
Factors Affecting CHF
! Coolant Sub-cooling! Vapour Quality! Coolant Velocity
Actual and Critical Heat Flux
Channel distance
C
h
a
n
n
e
l
p
o
w
e
r
inlet outlet
CHF
Actual h
eat flux
Bundles in dryout
Critical Channel Power
! CCP! The minimum channel power that gives
dryout! Varies with coolant conditions! Varies with flux shape
Boiling and Flow
Inlet OutletChannel position
9.6
9.8
10.0
10.4
10.2Boiling starts
Non-boiling mode
Boiling mode
P
r
e
s
s
u
r
e
M
P
a
(
a
)
Temperature Profile2800
2400
2000
1600
1200
800
400
T
e
m
p
e
r
a
t
u
r
e
,
C
Fuel melting point
Fuelsheath
Coolant
Fuelsheath
Coolant
Fuel pellet
More Temperature Profiles
Overratingand dryout
2400
2000
1600
1200
800
400
T
e
m
p
e
r
a
t
u
r
e
,
C
FuelsheathCoolant
Fuelsheath Coolant
Fuel pellet
Fuel meltingpoint
Nominal rating,normal cooling
Overratingwithout dryout
Light loadand dryout
2800
Possible film ofgaseous fission
products (on LOCA)
Vapour filmdue to dryout
Bad things to do to fuel
Low HTS Pressure
Tsat at reduced pressure
Tsat at normal pressure
Coolanttemperature at
reducedpressure
Channel position
C
o
o
l
a
n
t
t
e
m
p
e
r
a
t
u
r
e
Inlet Outlet
CHF at reducedpressure
CHF at normal pressure
Channel position
H
e
a
t
f
l
u
x
Inlet Outlet
a) Temperature profile
b) Heat flux profile
Actual hea
t flux
Coolant temperature atnormal pressure
Reduced FlowSaturation temperature
Reduced flow
Normal flow
a) Temperature profile
Channel position
C
o
o
l
a
n
t
t
e
m
p
e
r
a
t
u
r
e
Inlet Outlet
Outlet
CHF at reducedflow
CHF at normal flow
Channel position
H
e
a
t
f
l
u
x
Inletb) Heat flux profile
Actual hea
t flux
Dryout zone
Inlet High Temperature
Saturation temperature
High inlettemperature
Normal inlettemperature
Channel position
C
o
o
l
a
n
t
t
e
m
p
e
r
a
t
u
r
e
Inlet Outlet
CHF at high inlettemperature
CHF at normal inlet temperature
Channel position
H
e
a
t
f
l
u
x
Inlet Outlet
a) Temperature profile
b) Heat flux profile
Actual hea
t flux
Flux Tilt to Outlet
Saturation temperature
Channel position
C
o
o
l
a
n
t
t
e
m
p
e
r
a
t
u
r
e
Inlet Outlet
CHF at skewed flux
CHF at normal flux
Channel position
H
e
a
t
f
l
u
x
Inlet Outlet
a) Temperature profile
b) Heat flux profile
Normal he
at flux
Normal flux
Skewed heat
flux
Skewed flux
Dryoutzone
Flux Tilt to Inlet
Saturation temperature
Channel position
C
o
o
l
a
n
t
t
e
m
p
e
r
a
t
u
r
e
Inlet Outlet
CHF at skewed fluxCHF at normal flux
Channel position
H
e
a
t
f
l
u
x
Inlet Outlet
a) Temperature profile
b) Heat flux profile
Normal he
at flux
Normal flux
Skewed heat
flux
Skewed flux
Excessive Channel Power
Saturation temperature
Channel position
C
o
o
l
a
n
t
t
e
m
p
e
r
a
t
u
r
e
Inlet Outlet
CHF at excessivechannel power
CHF at normal channel power
Channel position
H
e
a
t
f
l
u
x
Inlet Outlet
a) Temperature profile
b) Heat flux profile
Normal he
at flux
Normal channelpower
Excessivechannel power
Dryout zone
Excessiveheat flux
For You to do
HTS Components
HTS Feed & Bleed
BleedCondenser
! Non-condensable gases! Reduce heat transfer! Steam pressure rises! Increased reflux
cooling! Vessel appears sub
cooled
! Degassing Orifice
Pressurizer Control
Boiler Shrink and Swell
! Boilers are probably more correctly called steam generators
Steady State Shrink and Swell
Zero Load Low Load Full Load
Rise inLevel
Rise inLevel
Transient Shrink and Swell
! Shrink and swell from short term effects! Reactor power boiler level
! Boiling increases
! Boiler Pressure boiler level ! Water flashes to steam! Steam expands
Effects on the Downcomer! Water flow into the
annulus increases! Water flow out of
the annulus decreases
! Instrumentation sees a level increase
ExpansionForces
CycloneSeparators
DowncomerAnnulus
Boiler Level Control
SwellMargin
ShrinkMargin
SwellMargin
ShrinkMargin
Constant Level Full Power Level
Zero Power Level
Fixed Level Control Ramped Level Control
Improper Level! Low
! If tubes are uncovered! Reduce heat transfer! Time in loss of feedwater events is reduced! Reactor power automatically reduced
! Setback or stepback and finally a trip
! High! High vapor content in steam! Slugs of water to turbine! Turbine trip
Boiler Pressure
! Boiler pressure is the key parameter in matching heat source to sink
! Reactor Leading! Reactor Lagging
Warm-up and Cool-down
! Heat transfer in the boiler
mTAUQ =
! A low power levels the HTS is about the same temperature as the boiler
Rx for Warm-up
! Put some energy into HTS from pumps and reactor power
! Increase boiler pressure! Boiler temperature follows (saturated
vessel)! HTS temperature follows that
Rx for Cool-down
! Heat sources are pumps and decay heat! Boiler pressure is ramped down ! Steam energy released is greater that
energy input! Down go temperatures! Limit around 130-150C due to huge
volume of steam required
Ideal Temperature Ramps
! 2.8C a minute! This rate minimizes
! Thermal stress! Probability of delayed hydride cracking! Feedwater loss
For You to do
Heat and Thermodynamics COURSEHeat and Thermodynamics Presentation