Thermosyphon Cooling

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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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    - 8 -

    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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    - 10 -

    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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    - 11 -

    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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    - 12 -

    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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    - 13 -

    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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    - 15 -

    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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    - 16 -

    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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    - 17 -

    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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    - 18 -

    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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    - 19 -

    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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    - 21 -

    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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    - 29 -

    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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    - 32 -

    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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    - 34 -

    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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    - 35 -

    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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    - 36 -

    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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    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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    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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    - 50 -

    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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    - 57 -

    (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