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PERFORMANCE ANALYSIS OF EVAPORATIVE COOLING WITHCOOLNESS RECOVERY SYSTEM AND HEATING COOLING
WATER ASSISTED IN ANIMAL HOUSES
2551
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PERFORMANCE ANALYSIS OF EVAPORATIVE COOLING WITH COOLNESS
RECOVERY SYSTEM AND HEATING COOLING WATER ASSISTED IN ANIMALHOUSES
2549 550,000
29 2551
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2549
. . . . . . .
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i
Abstract ii iv
1
1.1 11.1.1 Evaporative cooling 3
1.1.2 4
1.1.3 Coolness recovery system 6
1.2 61.3 81.4 8
1.4.1
Evaporative Cooling 81.4.2 131.4.3 13
2
2.1 Evaporative Cooling 172.2 21
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2.3 212.3.1 212.3.2 242.3.3 25
3
3.1 263.1.1 26
Evaporative Cooling 3.1.2 26
3.1.3 28
3.1.4 28 3.1.1 - 3.1.3
3.1.5 29
3.1.6 293.1.7 29
3.2 293.2.1 293.2.2 30
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4
4.1 324.1.1 32
4.1.2 334.2 42
4.2.1 424.2.2 43
4.2.3 44
(Wetted media)
4.2.4
464.3 48
4.3.1 484.3.2 51
4.4 534.4.1 53
4.4.2
54
5
5.1 555.1 56
57
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1.1 2 1.2 10 1.3 Wetted media 12 1.4 Wetted media 12 2.1 Evaporative cooling 20
4.1 3 33 4.2 35 4.3 43
4.4 49
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1.1 2542 3 1.2 Evaporative cooling 4
Wetted media 1.3 5 1.4 5 1.5 7
- 1.6 Evaporative cooling 9 1.7 11 1.8 11 1.9 14
1.10 15 2.1 direct evaporative cooling 17 2.2 Indirect evaporative cooling 18 2.3 Direct / indirect Evaporative cooling 19
2.4 Indirect/direct evaporative cooling 19 2.5 23
2.6 25 3.1 27
3.2 Wetted media 28 3.3 28 3.4 30 3.5 K 30
3.6 Memmert DO 6057 31
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3.7 31 3.8 31 4.1 34 4.2 36 4.3 37
4.4 38 4.5 39 4.6 40
4.7 43 4.8 44
4.9 45 4.10 (Wetted media) 46 4.11 47 4.12 47 4.13 48 4.14 49
4.15 50 4.16 Condenser Evaporator 51 4.17 52 4.18 53
4.19 54
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PERFORMANCE ANALYSIS OF EVAPORATIVE COOLING WITHCOOLNESS RECOVERY SYSTEM AND HEATING COOLING
WATER ASSISTED IN ANIMAL HOUSES
NATTHAWUD DUSSADEE, ATIPONG NANTAPHAN, PRAPAKORNTARACHAI, CHURAT TARARUK AND TANONGKIAT KIATSIRIROAT
--------------------------------------------------------------------
2 1 2
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1
26.7-28.8 oC 76.2-85.1 %8.9 % 50.6 % 0.021-0.036 m2/m2 28.3-58.3 m3/h/m2 85.1-87.3 % 2 R22 1,000 30 oC 26 oC 12 () 2.6 oC 48-52 oC 8-10 ()
24.8 oC 14.8 oC 27.8 %
8.6 %
Abstract
The main objective of this research was to study the performance of evaporativecooling that used heating cooling water produced by solar energy which functioned toproduce heat during midday and coolness during midnight. This study was divided intotwo parts: (1) study of the performance of existing animal houses in order to determinethe variables in designing animal houses utilizing heating cooling water; and (2) to
develop the production system for heating cooling water through heating pipes
constructed and tested for their performance in animal houses using ground water pipes
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to increase the efficiency of heat conveyance and distribution of temperature within theanimal house.
Experiment 1. This trial was conducted in private chicken laying houses incomparison with poultry houses of Maejo University Farm. Results showed thatevaporative cooling was able to control the atmospheric temperature in animal houses at26.7-28.8oC, relative humidity at 76.2-85.1%. Further results indicated that private animalhouses were less able to control the relative humidity than the animal houses in MJUFarm at about 8.9% and had lower energy consumption at 50.6%. The animal housesconstructed wet screen per area at 0.021-0.036 m2/m2. Rate of expelled air per housearea was 28.3-58.3 m3/h/m2. In addition, it was found that the efficiency for cooling was85.1-87.3%.
Experiment 2. Results indicated that production of heating cooling waterthrough heating pipes by using thermosiphon R22 as working substance, was able toreduce the temperature of 1,000 liter water tank from 30oC to 26oC within a period of 12
hours (during midnight). It was able to reduce the water temperature from normal level atabout 2.6oC and produce hot water at 48-52oC within a period of 8-10 hours (midday).
Test results on the rate of heat conveyance of wet sheet showed that when thetemperature of cool water from 24.8oC to 14.8oC, the conveyance rate was increased at27.8%. The installation of rotation system for ground water in the animal house showedthat the water rotation system was less able reduce the temperature of animal houses ascompared with animal houses having no such system and was also less able to control
the relative humidity. In addition, it has cooling efficiency of more than 8.6%, in which thelow relative humidity of air in the animal houses was more appropriate for raising animalsand the high efficiency of the animal houses was able to reduce the expenses on
electrical energy.
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i
PERFORMANCE ANALYSIS OF EVAPORATIVE COOLING WITHCOOLNESS RECOVERY SYSTEM AND HEATING COOLING
WATER ASSISTED IN ANIMAL HOUSES
--------------------------------------------------------------------
2 1 2
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ii
1
26.7-28.8 oC 76.2-85.1 % 8.9% 50.6 % 0.021-0.036 m2/m2 28.3-58.3m3/h/m2 85.1-87.3 % 2 R22
1,000 30 oC 26 oC 12 () 2.6 oC 48-52 oC 8-10 ()
24.8 oC 14.8 oC 27.8 %
8.6 %
Abstract
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- 1 -
1
1.1
(Evaporative cooling) 1
5-8 3 4 80 oF 5 82 oF (, 2538) 8 62 72 74 76 78 80 82 84 oF 4,800 2,719.72 / (, 2542)
21-24 oC 60-80 % 0.76-1.27 m/s(, 2538) Cooling effect 1
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- 2 -
1.1
(oC) (oC)
(4.5-6.8 ) 3 4 (6.8-11.3 .) (11.3-22.7 ) 3 4 (22.7-27.2 )
(22.7-68.0 )
32-3529-3224-2921-2718-24
15.6-2115.6-2415.6-18
29272118
15.6
121212
: (2544)
10-15 oC
1.1
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- 3 -
0
10
20
30
40
50
60
Jan F eb M a r A pr M ay Ju n Ju l A ug Se p Oc t
(C)
Me a nMean max .Mean min.
1.1 2542
:
1.1.1 Evaporative cooling
Wetted media Evaporative Cooling Wetted media 1.2
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- 4 -
Wetted
media
- - -
.
Wetted
media
.
1.2 Evaporative cooling
Wetted media
1.1.2
!!!
!!!
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- 5 -
wetted media
1.3 3 (Evaporator ) (Adiabatic) (Condenser) 2 Condenser Evaporator
h e a t s in k
h e a t s o u r c e
l i q u i d
v a p o u r
c o n d e n s e r
s e c t i o n
a d i a b a t i c
s e c t i o n
E v a p o r a t o r
s e c t i o n
1.3
Cooling water tank
Heating water tank
Day as evaporator Night as condenser
Day as condenser
Night as evaporator
Thermosyphonsolar collector
1.4
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- 6 -
1.4 2
Evaporator Condenser Condenser Evaporator Condenser Evaporator Condenser ( ) ( )
1.1.3 Coolness Recovery Evaporative cooling
20-27 oC 6-7 oC Wetted media
70-87 % (Coolness recovery system)
Evaporative cooling
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- 7 -
(Coolness Recovery System)
Wetted media Evaporative cooling Wetted media Wetted media 1.5
Cooling water
Heating water
Cooling
water tank
Heating
water tank
Thermosyphon
solar collector
Animal house
Wetted
media
Heating
space
Coolness
recovery
system
Ambient
air
Cooling
air
pump
pump
1.5 -
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1.2 1.2.1
1.2.2 1.2.3
1.3 1.3.1
1.3.2
1.3.3
1.3.4 1.3.5
1.4
1.4.1 Evaporative Cooling
Wetted media Wetted media Wettedmedia Wetted media 6 Wetted media 3-12 oC (Mastalerz, 1977)
1.88 kJ/cm3 (Williams and Shumack, 1983)
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- 9 -
1.6 Evaporative cooling
Evaporative cooling (2543) 1.2 ( (2543), (2544), (2542), (2544), (2538))
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1.2
7-8 /. 12-14 /.
5
6-9 oC 7 oC/ 3.95 . 3.62 . 0.33 . 2 ./ 0.80 0.40 0.40 4-6 % 2-4 % 2 %
47 40 7 2 . 5.88 / 6.63 / 0.75 /
(2542) 1.7 1.8 27.1 oC 20.5 oC 30.5 oC
19 oC () (2538) 21 oC 24 oC
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1.7: (2542)
1.8: (2542)
Hellickson and Walker (1983) Evaporative cooling Wetted media Wetted media Corrugated cellulose 6 1.75 m/s 1.3 Wetted media 10 L/min-m Wetted media Wetted media 1.4
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1.3 Wetted media
1.4 Wetted media
Watt (1963) Evaporative cooling 7.5 2.4 L/min-m2 of Wetted media (Wiersma andBenham, 1974)
Evaporative Cooling
Wettedmedia Evaporative Cooling
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1.4.2
(2545) (Thermosyphon Heat Exchanger) (Plate HeatExchanger)
(2542) 1 (Internal Rate of Return, IRR) 27.89 % , (2542) ,
(2544)
1.4.3
Fukada et al. (1993) 3-4oC. 1.9 Kiatsiriroat, eta.l (1998)
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9oC Lee, et al. (1993)
Vasiliev.L.L, et al. (1993)
1.9 : Fukada et al. (1993)
Dussadee (2002)
10 26.9%wb 1 30 oC 65 oC
37-38o
C
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1.10 : Dussadee (2002)
(2546) PE 2,000
4 20 2 16 2 4.8 R-134a PE 2 32 oC 19 oC 110
(2538)
(2526 ) radiative cooling 2 30.4 x 243.8 5 10 22, 26 , 28 oC
Paddy
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22, 26, 28 OC -14 , 5, 25 oC
24.00 184 W/m2 , 122 W/m2 Wetted media Evaporativecooling Wetted media
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2
2.1 Evaporative Cooling
Evaporative cooling (Wetted media) Evaporative cooling
2 direct evaporative cooling Indirect evaporative cooling 2.1 2.2
2.1 direct evaporative cooling
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2.2 Indirect evaporative cooling
Direct evaporating 2.1 Wetted media 1 (Dry side) 2 (Wetted side) Wettedmedia (Latent heat) (Psychometric) 2.3
Indirect evaporating 2.3 Primary air Secondary air Secondary air
Primary air (Sensible heat) Primary air Indirect evaporative cooling 2.3 Direct evaporative cooling Indirect evaporative cooling Directevaporative cooling Indirect/direct evaporative cooling 2.4
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Indirect evaporative cooling Pre-cool Direct evaporativecooling
2.3 Direct / indirect Evaporative cooling
2.4 Indirect/direct evaporative cooling
Direct evaporative cooling () (Adiabatic) 100 % 100 % Wetted media 100 % Direct
evaporative cooling
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- 20 -
100x
1wb
T
1db
T
2dbT
1dbT
Eff
(2.1)
Tdb1 Tdb2 Wetted media , oC
Twb1 ,oC
2.1 Evaporative cooling
(Effectiveness) 65% 85% indirectEvaporative cooling Direct Evaporative cooling (Foster, 1996)
2.1 Evaporative cooling
: Foster (1996)
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2.2
2.5 2 condenser 1
1 evaporator 2
condenser 2
Wetted media Evaporative cooling Wetted media
2.3
2.3.1
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- 22 -
)iToT)(pCm(condQ (2.2)
( pCm ) , W/K To Ti
)aTcT(hAcondQ (2.3)
h , W/m2
K A , m2 Tc Ts C h
Lump capacity analysis
)vTw(TeUAdt
wdT
pwmC (2.4)
m , kgCpw , J/kg
oC
Tw , oCTv ,
oCAe , m
2U , W/m2K
(2.4) (2.5)
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- 23 -
.)( tvTwTeUApwmc
ttwT
ttwT
(2.5)
(2.6),
),,( avgvTavgwTeA
condQ
U
(2.6)
Condenser Condenser (Sky radiation)
(Wet bulk temperature) 2.5
2.5
)4sT4skyT(AradQ (2.7)
Emittance,
A condenser, m2Tsky , KTs Condenser, K
-
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- 24 -
Swimbank (1963) (Tsky) (Tair)
2.10552.0 airsky TT (2.8)
Whillier (1967)
6 airsky TT (2.9)
(2.8) 30 oC (2.9) 20oC
2.3.2
14o18o
65-100 Evaporator Condenser
,
)(
ATG
ihi
Tfho
TmCp
(2.10)
m , kgCp , kJ/kg-
oCTho ,
oCThi ,
oCA , m2GT , kJ/m
2
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- 25 -
2.3.3
(Effectiveness: E ) 2.6
cihi
cicocc
hohihh
TTCpmQ
TTCpmQ
TTCpmQ
Q
QE
minmax
max
(2.11)
Q (W)
T (C)
Cp (J/kg C)Subscripts
h c i o
HeatExchanger
Tco
Tho
Tci, m
c
Thi, m
h
2.6
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- 26 -
3
3.1
3.1.1 Evaporative
Cooling
Evaporative Cooling
Wetted media Wetted media
wetted media
3.1.2
3.1
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- 27 -
3.1
Wetted Media Evaporative Cooling
Wetted media 3.2
Wetted media
Wetted media
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- 28 -
wettedmedia
Flow
meter
pump
3.2 Wetted media
orifice plate
T
P
T
P
T
P
T
P
radiator
blower
flow mixer
T
P
temperature measurement
pressure measurement
s
heater
flow mixer
P T
3.3
3.1.3
3.1.4 3.1.1 - 3.1.3
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3.1.5
3.1.6
3.1.7
3.2
3.2.1 (Energy Auditing)
Evaporative Cooling
3
76
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- 30 -
3.43.2.2
1.
K 0.1C
3.5 K
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- 31 -
2. (Data logger)
Memmert DO 6057 1 oC
3.6Memmert DO 6057
3 (Digital AC Clamp Meter)
3.7
4 Testo 425
0.1
3.8
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4
3
1 2
3
1
4.1
4.1.1
3
76
4.1 3 2
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- 33 -
3 1
4.13
50 x 10 m2 50 x 10 m2 50 x 10 m2
4 ,120 cm ,
1 hp/5 ,120 cm ,
1 hp/4 ,120 cm ,
1 hp/ 1 , 1 hp 2 ,0.5 hp/ 2 ,0.5 hp/
1.8 x 10 m2 1.8 x 3.9 m2/ 1.75 x 3 m2/ 6,400 4,608 1,141
4.1.2
0.021-0.036 m2/m2 4.2
3.58 m/s 14,575.98 m3/h- 2 29,151.96 m3/h 58.30 m3/h-m2
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7,082.50m3/h- 2 14,165 m3/h
28.33 m3/h/m2
10,715 m3/h- 2 21,430 m3/h 42.86 m3/h-m2
28 %
4.1
24-25 oC
4.2 3
26.7 0C - 28.8 0C 4.3 30.0-37.4 0C 0.073-0.108 0C/m
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4.2
m3/h/m2
() 0C
0C
0C
0C/m
%
m2/m2
%
kW-h/day
58.30 24.3 23.3 1.0 37.4 26.3 28.4 31.7 28.5 0.108 76.2 0.036 87.3 29.54
28.33 25.4 24.1 1.3 30.0 24.8 26.5 28.7 26.7 0.073 85.5 0.028 85.1 59.68
42.86 24.6 24.5 0.1 34.2 25.7 26.6 28.9 27.1 0.106 85.1 0.021 86.1 52.82
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2121222223232424
252526
9:00 9:40 10:20 11:00 11:40 12:20 13:00 13:40 14:20 15:00 15:40 16:20 17:00()
(0C)
.
15
171921232527293133
9:00 10:00 11:00 12:00 13:00 14:00 15:00 16:00 17:00()
(0C)
.
23.0
23.5
24.0
24.5
25.0
25.5
9:00 9:40 10:20 11:00 11:40 12:20 13:00 14:00 14:40 15:20 16:00 16:40
()
(0C
)
.
4.2
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- 37 -
0
5
10
15
20
25
30
35
40
9:00 9:40 10:20 11:00 11:40 12:20 13:00 13:40 14:20 15:00 15:40 16:20 17:00
(0C)
.
05
10152025303540
9:00 9:40 10:20 11:00 11:40 12:20 13:00 13:40 14:20 15:00 15:40 16:20 17:00
(0C)
.
05
10152025303540
9 :00 9:40 10 :2 0 1 1:00 1 1: 40 1 2:20 1 3:0 0 14 :0 0 14 :40 1 5:20 1 6:00 16 :4 0
()
(0C)
.
4.3
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- 38 -
41 oC 29.3oC
12.8oC 5.4 oC 10.04 oC 28.82oC 0.108 oC/m
38.6 oC 13:40-15:20 . 27.4 oC 8.25 oC 3.65 oC 6.21oC 26.7oC 0.073 oC/m
38.1 oC 13:40 16:40 . 27.3oC 8.27 oC
5.3o
C 6.4oC 27.07 oC 0.106 oC/m 4.4
0
5
10
1520
25
30
35
9:00 9:40 10:20 11:00 11:40 12:20 13:00 13:40 14:20 15:00 15:40 16:20 17:00
()
(0C)
4.4
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- 39 -
76.2-85.1 % 4.5
39.6 % 82.9 % 76.2 % 6.7 % 4.6
59.1 % 91.4 % 85.5 %
47.14 % 91.62 % 85.07 %
0
20
40
60
80
100
9:00 10:00 11:00 12:00 13:00 14:00 15:00 16:00 17:00
(%RH)
4.5
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- 40 -
0102030405060
708090
100
9:00 9:40 10:20 11:00 11:40 12:20 13:00 13:40 14:20 15:00 15:40 16:20 17:00
(RH
%)
.
0
20
40
60
80100
9:00 10:00 11:00 12:00 13:00 14:00 15:00 16:00 17:00
(RH%)
.
0
2040
60
80
100
9:00 9:40 10:20 11:00 11:40 12:20 13:00 14:00 14:40 15:20 16:00 16:40()
(RH%)
.
4.6
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87.3 % 85.1 % 86.1 %
2
1. 2 2 3 21.110C 25.560C 26.670C ( )
2. 2 2 3 4 21.110C 25.560C 26.670C 26.670C (
)
2 1 20:00 . 8:00 . 24 1 12 1 3.6 1
29.54 kW-h/d 10,782 kW-h/y 2.98 /kW-h 32,130.4
59.68 kW-h/d 21,783 kW-h/y 2.98 /kW-h 64,913.3
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52.82kW-h/d 19,279 kW-h/y 2.98 /kW-h
57,451.4
27.1-28.5 oC () 76.2-85.1 % 50.6 %
9.3 %
2
4.2
4.2.1
2 Evaporator Condenser
Condenser Evaporator Condenser Evaporator Condenser
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( ) ( )
Cooling water tank
Heating water tank
Day as evaporator Night as condenser
Day as condenser
Night as evaporator
Thermosyphon
solar collector
4.7
4.3
Condenser Evaporator
1.15 x 2.15 m2 0.65 x 1.2 m2 2.47 m2 0.78 m2/ 8 in2 8 in2
R22 R22
- % 50
4.2.2
24-38 oC
1,000 30
o
C 26 oC 12
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- 44 -
2.6 oC 48-52 oC
8-10 ()
2022242628
303234363840
17
:30
:00
22
:10
:00
02
:50
:00
07
:30
:00
12
:10
:00
16
:50
:00
21
:30
:00
02
:10
:00
06
:50
:00
11
:30
:00
16
:10
:00
20
:50
:00
01
:30
:00
06
:10
:00
10
:50
:00
15
:30
:00
()
(0C)
4.8
4.2.3 (Wetted media)
40x40 ANSI/ASHRAE .
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- 45 -
4.9
1
1.5-2 /
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500-2,000 24.8 oC 14.8 oC 26 oC 2 m/s
( 543.3 752.5 27.8 % (UA, W/K) 509.4 664.0 W/K
0
500
1000
1500
2000
2500
3000
3500
4000
1.00 1.50 2.00 2.50 3.00 3.50 4.00
v (m/s)
Tai = 26 C, Twi = 24.8 C
Tai = 38 C, Twi = 24.8 C
Tai = 26 C, Twi = 14.8 C
4.10 (Wetted media)
4.2.4
ANSI/ASHRAE .
4.11 4.12 4.13
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4.11
4.12
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4.13
3
4.3
4.3.1 4.1-4.2
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4.4
4.4
3.5 x 9 m2 1 ,96 cm , 1 hp/ 1 , 1 hp
1.8 x 3 m2
4.14
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4.15
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4.3.2
Condenser 1.15 m. x2.15 m. 2.47 m2Condenser 2 Evaporator 0.65 m. x 1.2 m. 0.78 m2 4.16 0.7 m. 1.3 m. 1.10 m. 1,110
Condenser Evaporator
4.16 Condenser Evaporator
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Cold
water
Hot
water
Water
pump
Valve
Valve
suction
pump
Fan
Cooling padReturn line
Water ground tube
Temperaturecontrol box
Temp
sensor
4.17
. 1 oC
1 oC 1 oC
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4.4
4.4.1
15-17 oC 2 19.7 20.1 oC
4 5.8 % 8.2%
5.0
10.0
15.0
20.0
25.0
30.0
35.0
40.0
6:00
7:00
8:00
9:00
10:00
11:00
12:00
13:00
14:00
15:00
16:00
17:00
18:00
Time
Temperature(C)
Tw Th_without return Ta Th_with return
4.18
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4.4.2
45-50 oC 27 oC 27 1 o C 100 / 27.3 oC 28.8 oC 26.2 oC
10.0
20.0
30.0
40.0
50.0
60.0
18:00
19:00
20:00
21:00
22:00
23:00
0:00
1:00
2:00
3:00
4:00
5:00
6:00
Time
Temperatu
re(C)
Ta Thouse Tset Twater
4.19
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5
5.1
R22 50 %
2 1
26.7-28.8o
C 76.2-85.1 % 8.9 % 50.6 % 0.021-0.036 m2/m2 28.3-58.3 m3/h/m2 85.1-87.3 % 2 1
1,000 30 oC 26oC 12 () 2.6 oC 48-52 oC 8-10 ()
24.8 oC 14.8 oC
26 oC 2 m/s
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27.8 % (UA, W/K) 509.4 664.0 W/K
5.8 % 8.6 %
5.2
1.
2.
3.
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(2538). . .
(2526). RadiativeColling. 4 . (- ) . 13-16 2526.
.87 98 (2542). . .
(2543). . . 8 90
(2543). ..
8 89. (2543). ..
27 108. (2543).
. 27 106. (2544). .
8 93.
Dussadee, N. (2002). Design of Heat Pipe for Reduction of Heat Accumulation in aThermosyphon Paddy Bulk Storage, Ph.D. Dissertation, The Joint GraduateSchool of Energy and Environment, King Mongkut's University of TechnologyThonburi.
Fukuda M., F. Tsuchiya., K.Ryokai., M. Mochizuki, and K.Mashiko. (1993). Developmentof an artificial permafrost storage using heat pipes. Proceedings of 7th
International Heat Pipe Conference, Vol. 2, Begell House, U.S.A., pp.305-317.
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Foster, R.E. (1996). Evaporative Air Conditioning Fundamentals: Environmental &Economic Benefits Worldwide, Proceeding of the International Institute of
Refrigeration Conference, Denmark, pp.1.6-1.10.Hellickson M.A and Walker J.N (1983). Ventilation of Agricultural Structures. ASAEKiatsiriroat T., N. Lakdee and T. Roongrojwattana., (1998). Heat Extraction from ground
with heat pipes. 12thMechanical Engineering Seminar, ChulalongkornUniversity, November, Bangkok, Thailand.
Lee Y. and C.Z. Wu., (1993). Use of two-phase closed thermosyphon in concretecuring process: comparison of analysis and experiment. Proceedings of 7thInternational heat pipe conference, Vol. 2, Begell House, U.S.A., pp.319-325.
Mastalerz, J.W. (1977). EvaporativeCooling,P20-29. In : Mastalerz, J.W. TheGreenhouse Environment. United State of America : The Pennsylvania StateUniversity.
Williams, G.S. and Shumack, R.L. (1983). Cooling Greenhouse. In: Williams, G.S.;Shumack, R.L. , Greenhouse flowers and bedding plants for Agribusiness
studies. United State of American : The interstate Printer & Publishers, Inc.Watt, JR. (1963). Evaporative Air Conditioning. The Industry Press.Wiersma F. and S.Benham. (1974). Design Criteria for Evaporative Cooling. ASAE paper
NO. 74 4527, ASAE, St.Joseph, MI 4980.Josef Tanny and Shabtai Cohen , (2002). Screenhouse Microclimate and ventilation an
ExperimentalG.Desmaraisand C.Ratti,1998, Heattranfer Modelling of screenhoues,McGill
University,CanadaKiatsiriroat T. and N. Dussadee.,(2001). Reduction of Heat Accumulated in
Thermosyphon-Paddy Bulk Storage. Int. J. Ambient Energy, Vol.22, No.1,pp.12-18.
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Rossel H.W,1979, A New and economical screehouse for virus research in topicalareas, FAO. Plant Protect,Bull,pp.74-76
Simmons,J.D. and Lott ,B.D.,(1996). Evaporative Cooling Performance Resulting FromChanges In Water Temperature Applied Engineering inAgriculture,Vol.12,No.4,pp.497-500
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iv
A
pA m2
paC kJ/kg K
wh hw
LH kJ/kg
th ( ) KJ/kgLh KJ/kg
sh KJ/kgi , m kg
aoutm
m3/s
n P Q cfmTdb1
0C
Tdb2 Wetted media0C
Twb1 0C
aT K
t evapV m/s
kV fpm