Solar Energy Part 3: Thermo-solar San Jose State University FX Rongère February 2008.
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Transcript of Solar Energy Part 3: Thermo-solar San Jose State University FX Rongère February 2008.
Thermo-solar
Absorption of the solar radiation Heating of a fluid to transfer energy
to a process Differences come from the type of
solar collectors and from the type of working fluid
Thermodynamics The state of a system of pure material at the
equilibrium is determined by two variables: Energy: E, e (lower case per unit of mass)
Entropy: S, s
Energy balance: conservation – Closed system
Entropy balance: no conservation – Closed system
AA
AA
Closed
WQdt
dE
A A
A
Closed T
Q
dt
dS
First law
Second law
0
Thermodynamics “Thermodynamics is a funny subject. The first time you
go through it, you don't understand it at all. The second time you go through it, you think you understand it, except for one or two small points. The third time you go through it, you know you don't understand it, but by that time you are so used to it, it doesn't bother you any more.”
“The second law of thermodynamics holds, I think, the supreme position among the laws of Nature. If someone points out to you that your pet theory of the universe is in disagreement with Maxwell’s equations - then so much the worse for Maxwell’s equations. If it is found to be contradicted by observation, well, these experimentalists do bungle things sometimes. But if your theory is found to be against the second law of thermodynamics I can give you no hope; there is nothing for it but to collapse in deepest humiliation.
Thermodynamics (2)
Open system (mass transfer) Energy balance
Entropy balance
).( AAAA
AA
AA
AOpen
khmWQdt
dE
AA
AA A
A
Open
smT
Q
dt
dS.
Thermodynamics (3)
Material characteristics provide relations with Pressure and Temperature
Ideal gas:
),(
),(
).(.
TPss
TPuu
kuMeME
P
dPR
T
dTCpds
dTCpdh
dTRCpdTCvdu
..
.
).(.
T
dTCds
dPvdTCdh
dTCdu
.
..
.
Incompressible fluid:
KmolJR ..314.8 1
Heat exchange
Energy balance:
2
'
2,
244
2,
2,
..
).(
..
.
.
.
dTgradk
dTTh
dTT
da
da
hm
cond
ambconv
sky
diffussol
directsol
es
Efficiency
oC
0 38 76 114 152 190 228 266 304oF
Eff
icie
ncy
(%
)
A
hmEfficiency
diffusSoldirectSol
es
.
.
,,
Flat-plate Collector
Up to 80oC (150oF) – Home heating, Water heating
Sometimes vacuum is made in the collector to prevent convection
Glass decreases radiation and convection Insulation is usually of polyurethane foam or mineral wool, sometimes mineral fiber insulating materials like glass wool, rock wool, glass fiber or fiberglass are used.
All technologies use selective surface coating to: Maximize solar radiation
absorption Minimize collector emission
Selective surface coating
Black chrome, black nickel, and aluminum oxide with nickel (galvanization) Titanium-nitride-oxide layer, (steam in vacuum process)
0
0.5
1
1 2 3
Wave length λ, μm
Em
issi
vity
, Ab
sorp
tivi
ty, ε
λ, a
λ
How a heat pipe works?
Evaporation process capture more energy by mass unit than one-phase flow. Example, water and steam:
Lv=2,260 kJ/kg, Cp=4.18 kJ/kg/K required flow is about 50 times lower than for
water heating
Size is smaller, loss are reduced The flow is maintained in natural
convection if the collector is angled over the horizontal
Step2: Heat transfer modeling
Radiation heat transfer
244
2,
2,
..
.
.
dTT
da
daQ
sky
diffussol
directsolA
rad
Radiation absorbed by water
0%
20%
40%
60%
80%
100%
0 0 1 10 100 1,000
Depth (cm)
Abso
rbed s
ola
r ra
dia
tion (%)
aΣ = .8 to .9εΣ = .8 to .9
Source: R Siegel, J R. Howel Thermal Radiation Heat Transfer Hemisphere Publishing 1981
Step2: Heat transfer modeling
Convective heat transfer
airwLairte TTAL
kC
..Pr.Re.. 3
18.0
2, ).( dTThQ ambconv
Aconv
airL
LV
.
Re
Parameter Signification SI American
Cte Empirical constant 0.037 0.037
kair Air conductivity 0.026 [W/ m/ K] 0.015[Btu.ft/ (h.ft2.oF)]
L Length of the swimming pool in wind direction
[m] [ft]
V Wind speed [m/ s] [ft/ h]
νair Air viscosity 14.3 10-6 [m2/ s] 0.554 [ft2/ h]
A Swimming pool area [m2] [ft2]
T Temperature [K] [oF]
Φconv Convective transfer [W] [Btu/ h]
Source: ASHRAE Application Handbook p 49-2
Step2: Heat transfer modeling
Convective Heat Transfer
0.0
5.0
10.0
15.0
20.0
25.0
30.0
0 2 4 6 8 10
Wind speed (m/s)
Con
vect
ion
coeff
ecie
nt
W/m
2/K
Step2: Heat transfer modeling
Evaporation
FaVCCppLv
Am
dLvmQ
awA
evap
evapA
evap
)..).(.(
..
21
2
Source:ASHRAE Application Handbook p 4-6
Type of swimming pools Factor of activity (Fa)
Residential swimming pools 0.5
Condominium 0.65
Thermal baths 0.65
Hotel 0.8
Public swimming pools or Schools 1
Whirlpools, spas 1.5
Wave pools, water slides 1.5 (minimum)
Parameter Signification SI American
C1 Empirical constant 0.088 [W/ m2/ Pa] 95 [Btu/ (h.ft2.inHg)]
C2 Empirical constant 0.779 [J / m3/ Pa] 0.425 [Btu.min/ (h.ft3.inHg)]
Lv Latent heat for water vaporization
2,260,000 [J / kg] 972 [Btu/ lb]
V Wind speed [m/ s] [ft/ h]
pw Saturation pressure at outside air dew point
[Pa] [inHg]
A Swimming pool area [m2] [ft2]
pa Saturation pressure at water temperature
[Pa] [inHg]
mevap Evaporation rate [kg/ s] [lb/ h]
Dry and Moist Air
0 20 40 60 80 1000.000
0.010
0.020
0.030
0.040
0.050
T [F]
Hu
mid
ity
Ra
tio
Pressure = 1.0 [atm]
0.2
0.4
0.6
0.8
30 F 45 F
60 F
75 F
AirH2O
Dew Point
Kg water/kg air
Saturation pressure of air:Pa=Humidity Ratio*Atm Pressure
Step2: Heat transfer modeling
Conduction in the ground
2
'
. .. dTgradkQ condA
Cond
kcond: Conductivity of the soil (1 to 3 W/m/K – 0.6 to 1.8 Btu/hr/ft/oF)
Step3: Balance Equation
WheatercircWCityA
evap
Acond
Aevap
Aconv
Arad
AAAA
AA
AA
AOpen
TTCmTTCm
QQQQ
khmWQdt
dTCM
dt
dE
....
).(..
.
mcirc= Masse of water divided by 8 hours
C= Thermal capacity of the water (4,180 J/kg/K, 1 Btu/lb/oF)
Step4: Sizing the collector
Max Temperature elevation: 8oF Solar radiation:
Ex: facing south with 30o of tiltTotal Solar Radiation on a panel (Tilt 30)
San J ose J une 21, 2007
0
100
200
300
400
500
600
700
800
900
1000
0:00 6:00 12:00 18:00 0:00
Time
Rad
iation
(W
/m2)
Direct Tilt 30
Diffuse
Total
Step4: Sizing the collector
Efficiency: .8 Flow rate:
Required energy:
Required area:
8.28600,3.8
.
600,3.8
VVMmcirc
Resource: http://www.flasolar.com/php/pool_panels_entry.php
0 38 76 114 152 190 228 266 304
VV
TCmcirc .6454.4.180,4.8.28
..
VVV
AreaPanelsol
.9.0900.8.0
.645
.8.0
.645_
Units: SI
Step 5: Simulation
Heat Transfer Modes - Without Solar Heating
24oC
-200
0
200
400
600
800
5 10 15 20
Time
Heat
Tra
nsf
er
(W/m
2)
Convection
Water addition
Evaporation
Solar Radiation
If no shade and good wall insulation, solar radiation absorbed by the pool easily compensates the heat loss by evaporation and convection:
Absorbed solar radiation: 280 kWh/day
Without Solar Collector
Temperature gain in a day is about 4.5oC for 13oC, 3oC for 18oC and 2oC for 24oC.
Temperature gain during the day
without Solar heating
-2
-1
0
1
2
3
4
5
6
0 4 8 12 16 20 24
Time
Tem
pera
ture
gai
n (
oC)
13
18
24
With Solar Collector
Temperature gain in a day is about 10oC for 13oC, 8.5oC for 18oC and 7oC for 24oC. Temperature gain during the day
Solar heating (South)
-4
-2
0
2
4
6
8
10
12
0 4 8 12 16 20 24
Time
Tem
pera
ture
gai
n (oC
)
13
18
24
Addition: 300 kWh/day
Savings compared to gas heater:
10 Therm/day$ 12/day
Cost:$ 100/m2
$ 4,500Use: 60 days/yearPay back: 6 years
With Solar Collector
South-East orientation provides faster heating in the morning but less overall energy.
Addition: 290 kWh/day
Temperature gain during the day
Comparison at 24oC
-2
0
2
4
6
8
10
0 4 8 12 16 20 24
Time
Tem
pera
ture
gai
n (
oC)
Collector FacingSouth
Collector FacingSouth-East
Without SolarCollector