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JPS5922143B2 - Greenhouse air conditioning methods and equipment - Google Patents
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JPS5922143B2 - Greenhouse air conditioning methods and equipment - Google Patents

Greenhouse air conditioning methods and equipment

Info

Publication number
JPS5922143B2
JPS5922143B2 JP55128434A JP12843480A JPS5922143B2 JP S5922143 B2 JPS5922143 B2 JP S5922143B2 JP 55128434 A JP55128434 A JP 55128434A JP 12843480 A JP12843480 A JP 12843480A JP S5922143 B2 JPS5922143 B2 JP S5922143B2
Authority
JP
Japan
Prior art keywords
greenhouse
water
air
heat
temperature
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP55128434A
Other languages
Japanese (ja)
Other versions
JPS5752729A (en
Inventor
利孝 菊井
豊樹 古在
真紀夫 林
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
TOSHIN KISETSU KK
Original Assignee
TOSHIN KISETSU KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by TOSHIN KISETSU KK filed Critical TOSHIN KISETSU KK
Priority to JP55128434A priority Critical patent/JPS5922143B2/en
Publication of JPS5752729A publication Critical patent/JPS5752729A/en
Publication of JPS5922143B2 publication Critical patent/JPS5922143B2/en
Expired legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/25Greenhouse technology, e.g. cooling systems therefor
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P60/00Technologies relating to agriculture, livestock or agroalimentary industries
    • Y02P60/14Measures for saving energy, e.g. in green houses

Landscapes

  • Greenhouses (AREA)
  • Central Heating Systems (AREA)

Description

【発明の詳細な説明】 熱帯植物を育成したり、野菜・草花などを促成栽培した
9などする時に用いる温室は通常寒冷時に燃料を燃やし
て温室内の空気を暖めることで運営されている。
[Detailed Description of the Invention] Greenhouses used for growing tropical plants or forced cultivation of vegetables, flowers, etc.9 are usually operated by burning fuel to warm the air inside the greenhouse in cold weather.

即ち例えば冬期に於て晴天の日の昼には透明材料で造ら
れた屋根・側壁を透過する太陽光線による熱で温室内の
気温が充分に或いは必要以上に上昇するから換気孔から
の空気の出入りを調節するだけで適温に保っているが夜
間或いは曇天・雨天の時は燃料を燃やして直接又は間接
に温室内の空気を暖めることで適温を保っている。
For example, during the winter on a sunny day, the temperature inside the greenhouse rises sufficiently or more than necessary due to the heat from the sun's rays passing through the roof and side walls made of transparent materials. The temperature is maintained at the appropriate temperature simply by adjusting the entrance and exit, but at night or on cloudy or rainy days, the temperature is maintained by burning fuel and directly or indirectly warming the air inside the greenhouse.

従って温室運営の経費の内燃料費が非常に大きな部分を
占める。
Therefore, fuel costs account for a very large portion of the costs of operating a greenhouse.

更に又冬期快晴の日の昼に太陽光線による熱で温室内の
気温が上昇する場合太陽光線エネルギーの60%前後は
空気を温める熱に費やされるが残り40%前後は土壌表
面からと植物の葉の表面からの水分の蒸発に対する潜熱
に費やされる。
Furthermore, when the temperature inside the greenhouse rises due to the heat from the sun's rays during the afternoon on a clear day in winter, around 60% of the sun's energy is used to heat the air, but the remaining 40% comes from the soil surface and the leaves of the plants. is spent on latent heat for the evaporation of water from the surface.

従って水分の蒸発が活発であるから温室内の湿度が上が
9過ぎてしばしば病害の原因とな9又植物育成に悪影響
を及ぼすことが多い。
Therefore, since moisture evaporates actively, the humidity in the greenhouse often exceeds 9°C, which often causes diseases and adversely affects the growth of 9-pointed plants.

本発明は温室にヒートポンプによる空気調和装置を設け
、冬期晴天の日の昼間太陽熱により温室内の温度・湿度
が上昇する場合、空気調和装置の除湿器で除湿して低湿
度に保ち除湿により発生する凝縮熱と太陽熱によシ気温
が必要以上に上昇することを防ぐため取去る顕熱とで別
に装備する水槽の水温を上昇させて蓄熱し、太陽熱のな
い夜間にその水槽の蓄熱分を放出させて温室内の空気を
適温に保つ様にするものであって、この方法により得ら
れる利益は次の通りである。
The present invention installs an air conditioner using a heat pump in a greenhouse, and when the temperature and humidity inside the greenhouse rise due to solar heat during the daytime on a sunny day in winter, the dehumidifier of the air conditioner dehumidifies the air to keep the humidity low. In order to prevent the temperature from rising more than necessary due to condensation heat and solar heat, the sensible heat that is removed is used to raise the water temperature in a separately equipped aquarium, storing heat, and releasing the heat stored in that aquarium at night when there is no solar heat. This method maintains the air in the greenhouse at an appropriate temperature, and the benefits obtained by this method are as follows.

■)冬期晴天の白昼間の太陽熱の一部を水槽に蓄熱し夜
間の寒冷時に放出して温室を適温に保つのであるから燃
料を燃やして温室を暖める場合に比べ格段に燃料が少な
くてすむ。
■) Part of the solar heat during clear daylight in winter is stored in a water tank and released during cold nights to keep the greenhouse at an appropriate temperature, so it requires significantly less fuel than heating the greenhouse by burning fuel.

曇天・雨天の時はやむを得ないから燃料を使うが快晴の
時は後に詳しく説明する様にはソ燃料なしですますこと
ができる。
When it's cloudy or rainy, it's unavoidable to use fuel, but when it's sunny, you can do without fuel, as I'll explain in detail later.

2)温室内の湿度を適度に保つから病害の発生が非常に
少な(なる。
2) Since the humidity in the greenhouse is kept at a suitable level, the incidence of diseases is extremely low.

3)温室内の温度を低く保つことによシ植物の葉面から
の水分の蒸発従って根からの水分の吸上げが活発になり
それに基いて養分の、吸上げも多(なるから植物の育成
が促進される。
3) By keeping the temperature in the greenhouse low, the evaporation of water from the leaf surfaces of plants and the uptake of water from the roots become active, which in turn increases the uptake of nutrients. is promoted.

4)冬期晴天時温室内の湿度が高いと屋根面、壁面の内
面に結露する。
4) If the humidity inside the greenhouse is high during clear skies in winter, condensation will form on the inner surfaces of the roof and walls.

この様に結露することは水蒸気の潜熱が外気に持ち去ら
れたことを示すもので即ち熱損失が太き(折角得られた
エネルギーを無駄に捨てることになる。
This condensation indicates that the latent heat of the water vapor is carried away to the outside air, which means that the heat loss is large (the energy that has been obtained through the effort is wasted).

本発明では湿度を低(保つから結露せず従って熱損失が
少な(即ち太陽熱を高度に利用できる。
In the present invention, since the humidity is kept low (no dew condensation occurs), there is little heat loss (that is, solar heat can be utilized to a high degree).

本発明を実施例につき詳しく説明すると次の通シである
The present invention will be described in detail with reference to embodiments as follows.

第1図に於て1は温室であシ屋根・外壁は太陽光線を通
す様透明な材料で構成されている。
In Figure 1, 1 is a greenhouse whose roof and outer walls are made of transparent material to allow sunlight to pass through.

2は植物を植える土壌であシ3は植物を示す。2 is the soil in which the plants are planted, and 3 represents the plants.

4は空気調和装置のセットを示しこのセットは温室の中
又は外に装備きれる。
4 represents an air conditioner set, which can be installed inside or outside the greenhouse.

これは個々の機器を夫々単独に据付けて管及びダクトで
結んでも良いし或いは各機器を一つのケースの中に機能
的に結合して取付けたユニット式にして装備しても良い
が第1図ではセット1示す意味で点線で囲んである。
This can be done by installing each piece of equipment individually and connecting them with pipes and ducts, or by installing a unit type in which each piece of equipment is functionally combined and installed in one case, but as shown in Figure 1. Here, it is surrounded by a dotted line to indicate set 1.

5は空気ダクトを示しフローシート形式に1本の線で簡
略に表示しである。
5 indicates an air duct, which is simply represented by a single line in a flow sheet format.

このダクトは温室の中を通しても良いめであるが第1図
では粉られしくならない様温室の外を通して画いである
This duct can be run inside the greenhouse, but in Figure 1 it is shown running outside the greenhouse to avoid dust.

6は蒸発器(空気冷却器)、7は圧縮機、8は凝縮器(
空気加熱器)、9は膨張弁であシこの4つでヒートポン
プの冷媒サイクルが完結する。
6 is an evaporator (air cooler), 7 is a compressor, and 8 is a condenser (
(air heater), 9 is an expansion valve, and these four complete the refrigerant cycle of the heat pump.

凝縮器(空気加熱器)8は一般のものと異シ共通のフィ
ン群を貫通する2つの管路10,11が交互に配置され
で構成されている。
The condenser (air heater) 8 is composed of two conduit lines 10 and 11 which are alternately arranged and pass through a common group of fins.

第1の管路10には冷媒が通シ冷媒はここで放熱して液
化する。
A refrigerant passes through the first pipe line 10, and the refrigerant radiates heat here and liquefies it.

第2の管路11にはポンプ12によシ水槽13の水が循
環して通される。
Water from a water tank 13 is circulated through the second pipe line 11 by a pump 12 .

14は通風機である。ダクト5を通って来た温室からの
空気は蒸発器6.凝縮器8を通過し通風機14の吸引側
に入シ、通風機14の排出側は温室内に開口しているか
ら温室内の空気は空気調和装置4を通って矢印の様に循
還する。
14 is a ventilator. The air from the greenhouse coming through duct 5 is sent to evaporator 6. The air passes through the condenser 8 and enters the suction side of the ventilator 14, and since the discharge side of the ventilator 14 is open into the greenhouse, the air in the greenhouse passes through the air conditioner 4 and circulates as shown by the arrow. .

この実施例の装置に基き具体的数1直の一例を交えて説
明すると次の通シである。
Based on the apparatus of this embodiment, the following formula will be explained using a specific example of the number 1 rotation.

表日本地区で(ま冬期は快晴の日が多(その日中温室内
の透過日射熱量は経験によシ平面積に対し1700kc
a7/m2 ・日とみなすことができる。
In the Omote Japan area, there are many sunny days in the winter (the amount of solar radiation transmitted through the greenhouse during the day is 1,700 kc relative to the flat area).
It can be considered as a7/m2 ・day.

温室の平面積を100 m2 と仮定し日照時間を8時
間とすると1時間当り受熱量は 1700kcu/m2 ・日X100m2÷8時圃/日
=21000kca17′時となる。
Assuming that the planar area of the greenhouse is 100 m2 and the sunshine duration is 8 hours, the amount of heat received per hour is 1700 kcu/m2 - day x 100 m2 ÷ 8 o'clock field/day = 21000 kca17' hour.

日中の温室内の気温を23℃、外気温を10℃とすると
屋根・外壁(その総面積を200m2とする)を通って
外部に失なわれる熱量は(経験による熱貫流率は大体4
.8kcal/rIL2・時−’cである)4.8 k
c al/ m2・時・℃X200rrL2×(23−
10)T、=12500 kcat/Rである。
If the temperature inside the greenhouse during the day is 23℃ and the outside temperature is 10℃, the amount of heat lost to the outside through the roof and outer walls (assuming a total area of 200m2) is (based on experience, the heat transfer coefficient is approximately 4
.. 8kcal/rIL2・hour-'c) 4.8 k
c al/m2・hour・℃×200rrL2×(23-
10) T, = 12500 kcat/R.

即ち入射熱の約60%が屋根・外壁から失われ、残り4
0%が潜熱となって水分を蒸発させる。
In other words, approximately 60% of the incident heat is lost through the roof and exterior walls, and the remaining 4.
0% becomes latent heat and evaporates water.

そしてこれで入熱と出熱がバランスし室内温を23℃に
保つことになる。
This balances heat input and heat output and maintains the indoor temperature at 23°C.

蒸発水分の量は(21000kcat/時−12500
kca、/。
The amount of evaporated water is (21000 kcat/hour - 12500
kca,/.

7時)÷580 kc a、/、/に9=14.7に9
7時となる。
7 o'clock) ÷ 580 kc a, /, / to 9 = 14.7 to 9
It's 7 o'clock.

ダクト5を通って蒸発器(空気冷却器)6に入る空気は
温室1の中のふん囲気と同じであシこれを温度23°C
2湿度80%と推定する。
The air entering the evaporator (air cooler) 6 through the duct 5 is the same as the ambient air inside the greenhouse 1 and is kept at a temperature of 23°C.
2Estimate the humidity to be 80%.

蒸発器6はフィン付き管で構成され冷媒の蒸発によシ直
接空気を冷却する形式のものである。
The evaporator 6 is constructed of a finned tube and is of a type that directly cools air by evaporating a refrigerant.

空気がこれを通過すると冷却され且つ水分がフィン上に
結露し除湿される。
As the air passes through it, it is cooled and moisture condenses on the fins to dehumidify it.

除湿により生じた水は流れて受皿15の上に落ち集めら
れて管16により外に排出される。
Water generated by dehumidification flows and collects on a saucer 15 and is discharged to the outside through a pipe 16.

(第1図では蒸発器6のフィンが水平になっている様に
画かれているがこれはフィンが垂直になる様に画(と冷
媒管の通過経路が解りにくくなるためやむを得ず水平に
画いたもので実際のものは結露した水が流れ易い様フィ
ンか垂直になる様な配置にする。
(In Figure 1, the fins of the evaporator 6 are drawn horizontally, but this is because the fins are drawn vertically (and the route of the refrigerant pipes is difficult to understand, so I had to draw them horizontally. In reality, the fins are placed vertically so that condensed water can flow easily.

)通風機14によシ循壊する風量を60rrL3/分と
し蒸発器6を適当に設計して温度23℃、湿度80%で
入って来た空気が冷却除湿されて温度16℃、湿度95
%になる様にすることができる。
) By setting the air flow rate circulated by the ventilation fan 14 to 60rrL3/min and designing the evaporator 6 appropriately, the air that came in at a temperature of 23°C and a humidity of 80% is cooled and dehumidified, and the air is cooled and dehumidified to a temperature of 16°C and a humidity of 95%.
%.

この時除かれる水分を計算すると次の通シである。Calculating the water removed at this time is as follows.

温度23℃、湿度80%の空気の絶対湿度は0、014
1 kg/kg空気、温度16°C2温度95%の空気
の絶対湿度はo、o lo 7kg/kg空気であるか
ら絶対湿度の差は 0.0141−0.0107=0.0034 kg/k
g空気 でちゃ、循還空気量は60が7分であるから1時間当り
除湿量は 0.0034 kg/kg空気×6空気rL3/分X1
.2kg/rIL3×60分=14.7に9/時。
The absolute humidity of air at a temperature of 23°C and humidity of 80% is 0.014
1 kg/kg air, temperature 16°C2 The absolute humidity of air at 95% temperature is o, o lo Since it is 7 kg/kg air, the difference in absolute humidity is 0.0141-0.0107 = 0.0034 kg/k
With g air, the amount of recirculated air is 60 = 7 minutes, so the amount of dehumidification per hour is 0.0034 kg/kg air x 6 air rL3/min x 1
.. 2kg/rIL3 x 60 minutes = 14.7 to 9/hour.

即ち先に計算した日光入射によシ蒸発する水分の量と〒
致するから温室内の蒸発水分は蒸発器6で全部除去され
、従って温室内の湿度は80%に保たれる。
In other words, the amount of water evaporated by sunlight incident calculated earlier and 〒
Therefore, all of the evaporated water in the greenhouse is removed by the evaporator 6, and therefore the humidity in the greenhouse is maintained at 80%.

蒸発器6を通って冷却除湿された空気は引続き凝縮器(
空気加湿器)8を通過する。
The cooled and dehumidified air passes through the evaporator 6 and continues to the condenser (
air humidifier) 8.

凝縮器8は先に述べた通シ特殊構造のものである。The condenser 8 is of the special construction previously mentioned.

即ち冷媒が放熱液化する第1管路10とポンプ12によ
シ水槽13の水が循還して通過する第2管路11が共通
のフィン群を貫通して交互に配置されたものである。
That is, a first pipe line 10 through which the refrigerant radiates heat and is liquefied, and a second pipe line 11 through which water from a water tank 13 circulates through the pump 12 are arranged alternately through a common fin group. .

その詳細斜視図を第2図に示した。第2図に於て17は
フィン群であシ金属板を数m’ttt乃至十数間程度の
間隔で図の様に並べである。
A detailed perspective view is shown in FIG. In FIG. 2, reference numeral 17 indicates a fin group, and metal plates are arranged at intervals of several m'ttt to more than ten as shown in the figure.

そのフィン群を貫通して管18,19,20,21゜2
2.23が並べられる。
Pipes 18, 19, 20, 21°2 pass through the fin group.
2.23 are arranged.

管18は上部で管19に接続され管19は下部で管20
に接続され管20は上部で管21に接続される。
Pipe 18 is connected at the top to pipe 19, which in turn is connected to pipe 20 at the bottom.
The tube 20 is connected to the tube 21 at the top.

管18と管21の中間に管22が、又管19と管20の
中間に管23が配置され、管22と管23は上部で接続
される。
A tube 22 is placed between the tubes 18 and 21, and a tube 23 is placed between the tubes 19 and 20, and the tubes 22 and 23 are connected at the upper portion.

冷媒は管18の入口から入シ管19゜20.21を通っ
て管21の出口から出る。
The refrigerant enters from the inlet of pipe 18, passes through pipes 19, 20, 21, and exits from the outlet of pipe 21.

又水は管23の人口から入り管22の出口から出る。Also, water enters through the tube 23 and exits through the outlet of the tube 22.

第2図は解り易くするため管の数を最小限度にして画い
であるが実際のものは第2図に於ける手前又は先方に管
を多数並べ更にススの右又は左に冷媒の管列と水の管列
を交互に多数段並べ第2図に準じて接続して作られる。
Figure 2 is drawn with the number of tubes minimized to make it easier to understand, but in reality, a large number of tubes are arranged in front or in front of the soot, and there is also a row of refrigerant tubes on the right or left of the soot. It is made by arranging a large number of rows of water pipes alternately and connecting them as shown in Figure 2.

又フィンの数も熱負荷に応じて適当な枚数が並べられる
Also, the number of fins is arranged appropriately depending on the heat load.

空気はフィンの間を矢印24の様に通過する。Air passes between the fins as shown by arrow 24.

凝縮器(空気加熱器)80作用を説明すると次の通りで
ある。
The operation of the condenser (air heater) 80 will be explained as follows.

第2図の冷媒管群18.19゜20.21は第1図では
第1管路10で代表され又第2図の水管群22.23は
第1図では第2管路11で代表される。
The refrigerant pipe group 18, 19, 20, 21 in FIG. 2 is represented by the first pipe 10 in FIG. 1, and the water pipe group 22, 23 in FIG. Ru.

以下第1図について説明する。FIG. 1 will be explained below.

今仮に第1図に於て凝縮器8が水管路11を持たず冷媒
管路10だけを持った普通の凝縮器(空気加熱器)とす
る。
Assume now that the condenser 8 in FIG. 1 is an ordinary condenser (air heater) having only a refrigerant pipe 10 and no water pipe 11.

蒸発器6を通過して温度16℃、湿度95%になった空
気がこの凝縮器(空気加熱器)を通ることで暖められる
The air that has passed through the evaporator 6 and has reached a temperature of 16° C. and a humidity of 95% is heated by passing through this condenser (air heater).

凝縮器の出口の空気の温度を計算して見る。Calculate and check the temperature of the air at the outlet of the condenser.

蒸発器6で空気から冷媒に移る熱量は次の通シである。The amount of heat transferred from the air to the refrigerant in the evaporator 6 is as follows.

湿シ空気線図から23℃、80%のエンタルピーは0、
4.1 kcal/kg、 16℃、95%のエンタ
ルピーは10.3 Kca17kg従って冷媒の得る熱
量は(14,1−10,3)kca77/kgX60r
rL3/分x1.2ky/77L3X60分= 164
00 kcal/時この熱量を移動するための圧縮機7
の動力は(1馬力当9の移動量を3000kcat/時
とする) 16.400Kca4/時÷3,000Kca4/時・
馬力=5.5馬カニ4.1 K、 W。
From the humidity psychrometric diagram, at 23°C, the enthalpy at 80% is 0.
4.1 kcal/kg, 16℃, 95% enthalpy is 10.3 Kca17kg Therefore, the amount of heat obtained by the refrigerant is (14,1-10,3)kca77/kgX60r
rL3/min x 1.2ky/77L3 x 60 min = 164
00 kcal/hour Compressor 7 to transfer this amount of heat
The power is (Assuming the displacement of 9 per horsepower is 3000kcat/hour) 16.400Kca4/hour ÷ 3,000Kca4/hour・
Horsepower = 5.5 horses Crab 4.1 K, W.

従って凝縮器で冷媒から空気に移る熱量は16.400
kca、/、/時+860 k c a t/に−WH
X4.1に−W−=19,900kca、/、/時従っ
て凝縮器入口で16℃であった空気は出口でGま 19.900kca、/7時÷(0,24kc at/
kg ・℃×60m3/分X 1.2に9/m3X60
分)=19℃ たけ温度上昇し16+ 19=35℃になる。
Therefore, the amount of heat transferred from the refrigerant to the air in the condenser is 16.400
kca, /, / hour +860 kca t/ -WH
In X4.1, -W- = 19,900kca, /, /hour Therefore, the air that was 16℃ at the condenser inlet becomes G at the outlet, 19.900kca, /7 hours ÷ (0,24kc at/
kg ・℃×60m3/min×1.2 to 9/m3×60
) = 19℃ The temperature rises to 16 + 19 = 35℃.

これでは温度が高過ぎていけないので適温即ち23°C
程度にするため凝縮器の次の水による空気冷却器を設置
することが必要になる。
With this, the temperature cannot be too high, so keep it at a suitable temperature, i.e. 23°C.
It is necessary to install an air cooler using water next to the condenser in order to maintain the same level.

即ちこの様に空気冷却器を配置しその水管に水槽13の
水をポンプ12で循還して通し空気冷却器で奪った熱量
で水槽13の水の温度を上昇させて蓄熱すれば所期の目
的を達することができる。
That is, if an air cooler is arranged in this way and the water from the water tank 13 is circulated through the water pipes by the pump 12, the heat taken by the air cooler is used to raise the temperature of the water in the water tank 13 and store heat. You can reach your goal.

ただその様にすると凝縮器で一旦空気を過熱し矢に空気
冷却器で適温迄冷却することになるため熱交換器が大き
くなり不経済となるから前記形式の凝縮器8を装備する
方が良い。
However, if you do that, the air will be overheated in the condenser and then cooled down to an appropriate temperature in the air cooler, making the heat exchanger large and uneconomical, so it is better to equip it with the above type of condenser 8. .

凝縮器8の機能を第2図について説明すると次の通シで
ある。
The function of the condenser 8 will be explained as follows with reference to FIG.

冷媒管18に圧縮された冷媒ガスが通シフイン17に熱
が伝えられる。
The refrigerant gas compressed in the refrigerant pipe 18 passes through and heat is transferred to the sifter 17.

管18の中を通る冷媒の温度が50℃であるとする。Assume that the temperature of the refrigerant passing through the pipe 18 is 50°C.

一方水管22に水が通シフイン17が冷やされる。On the other hand, water is passed through the water pipe 22 to cool the syringe 17.

水管22を通る水の温度が26℃であったとする。Assume that the temperature of the water passing through the water pipe 22 is 26°C.

フィン17は熱伝導の良い金属製であるから管18から
熱を受は速やかに管22に熱を与えるがそのフィン17
の温度は管18の温度50℃と管22の温度26℃との
ほぼ中間即ち(50+26)÷2−38℃附近になる。
Since the fins 17 are made of metal with good thermal conductivity, they receive heat from the tube 18 and quickly transfer the heat to the tube 22, but the fins 17
The temperature is approximately midway between the temperature of the tube 18 of 50°C and the temperature of the tube 22 of 26°C, that is, approximately (50+26)÷2-38°C.

フィン17の隙間を通過する空気の温度を21’Cとす
れば38−21=17℃の温度差により空気に熱を与え
ることになる。
If the temperature of the air passing through the gap between the fins 17 is 21'C, heat will be given to the air by a temperature difference of 38-21=17C.

冷媒管18,19,20,21から放熱する熱量の一部
を空気に与え残りを水管22,23に云えるのであるが
その比率を調節するには水管22.23を通過する水の
量を加減すれば良い。
A part of the heat radiated from the refrigerant pipes 18, 19, 20, 21 can be given to the air and the rest can be sent to the water pipes 22, 23, but in order to adjust the ratio, the amount of water passing through the water pipes 22, 23 must be Just adjust it.

水管22,23を通過する水量を減らせば水温が上がシ
従ってフィン17の温度が高(なり空気に与える熱量が
多(なる。
If the amount of water passing through the water pipes 22 and 23 is reduced, the water temperature will rise, and therefore the temperature of the fins 17 will be high (and the amount of heat given to the air will be large).

水量が減っているから水温は上がるが水全体の受熱量は
減る。
Because the amount of water is decreasing, the water temperature increases, but the amount of heat received by the water as a whole decreases.

空気に与える熱量を少な(し水の受熱量を多(したい時
は逆に水量を増せば良い。
If you want to give less heat to the air (and receive more heat from water), you can conversely increase the amount of water.

この様にして第1図に於て凝縮器8を出る空気は温度2
3℃になって(湿り空気線図から湿度が61%になるこ
とが解る)通風機14により温室1内に送り込まれ温室
1内は23℃に保たれる。
In this way, in FIG. 1, the air leaving the condenser 8 has a temperature of 2.
When the temperature reaches 3°C (it can be seen from the psychrometric diagram that the humidity is 61%), the air is sent into the greenhouse 1 by the ventilator 14, and the temperature inside the greenhouse 1 is maintained at 23°C.

又温室1内の湿度は蒸発による水分が加わり80%とな
る。
Moreover, the humidity inside the greenhouse 1 becomes 80% due to the addition of moisture due to evaporation.

ポンプ12で水槽13から(み上げられた水は凝縮器8
内の水槽11を通って加熱され水槽13に戻る。
The water pumped up from the water tank 13 by the pump 12 is sent to the condenser 8.
It passes through the water tank 11 inside and is heated and returns to the water tank 13.

従って水槽13内の水は段々温度が上がる。Therefore, the temperature of the water in the water tank 13 gradually increases.

前記実施例の数置に基き水槽13の蓄熱量を計算して見
ると次の通りである。
The amount of heat stored in the water tank 13 is calculated as follows based on the numbers in the above embodiment.

凝縮器8で35℃になるべき空気温を23℃に押えるた
め水の方に移す熱量は (35−23) ’CX O,24kca、ff7kg
・’CX 60 m”/分X 1.2kg/rrt3X
60分=12400kca、/。
The amount of heat transferred to the water in order to suppress the air temperature, which should be 35℃ in condenser 8, to 23℃ is (35-23) 'CX O, 24kca, ff7kg
・'CX 60 m”/minX 1.2kg/rrt3X
60 minutes = 12400kca, /.

7時 水槽80寸法を巾2.2mX長さ2.2mX高さ2.2
mとし貯水量を内容積の90%即ち9600tとする。
7 o'clock water tank 80 dimensions width 2.2m x length 2.2m x height 2.2
m, and the amount of water stored is 90% of the internal volume, or 9600 t.

水槽は外部に対し充分保温されるがそれでも熱損失はま
ぬがれない。
Although the aquarium is sufficiently insulated from the outside, heat loss cannot be avoided.

水温平均を25℃。外気温平均を3℃、保温材の熱貫流
率を1.0 kca7/m2 ・℃・時とすると槽の
外表面積は2.2rrLX2.2 mX 6 =29
rn2であるから熱損失は1.0 kcat/ rn”
・℃・時×29rrL2×(25−3) ’CC50
40kca/l、/時水槽8の入熱時間即ち日照時間を
8時間とすると水槽の蓄熱量の自利用し得る熱量は 12400 kcal/時×8時−640kcal/時
×24時 83800 kcat/日となる。
The average water temperature is 25℃. If the average outside temperature is 3℃ and the thermal conductivity of the insulation material is 1.0 kca7/m2 ・℃・hour, the outer surface area of the tank is 2.2rrLX2.2mX 6 = 29
rn2, so the heat loss is 1.0 kcat/rn”
・℃・hour×29rrL2×(25-3) 'CC50
40 kcal/l/hour If the heat input time of the aquarium 8, that is, the sunshine duration is 8 hours, the amount of heat storage in the aquarium that can be used is 12,400 kcal/hour x 8 o'clock - 640 kcal/hour x 24 o'clock, 83,800 kcat/day. Become.

そして水温上昇は 83800kcat÷9600 kca l/’C=8
.7℃二9°C となる。
And the water temperature rise is 83800kcat ÷ 9600 kcal/'C=8
.. The temperature will be between 7°C and 9°C.

例えば日の出前20℃迄下がっていた水温は日照の終る
夕方には20+9=29℃になる。
For example, water temperature that drops to 20 degrees Celsius before sunrise will drop to 20 + 9 = 29 degrees Celsius in the evening after the sunshine ends.

日が沈んだらヒートポンプの運転を止める。Stop the heat pump when the sun goes down.

即ち圧縮機7の運転を止め更にポンプ12・通風機14
も止める。
That is, the operation of the compressor 7 is stopped, and the pump 12 and the ventilation fan 14 are stopped.
Also stop.

夜になって気温が下がシ温室1内の温度が10°C以下
になったらポンプ12と通風機14を運転する。
When the temperature in the greenhouse 1 drops to 10°C or less at night, the pump 12 and the ventilation fan 14 are operated.

そうすると水管11の中を水槽13の温水が通シ凝縮器
8は温水による空気加熱器となシ温室1の気温が上がる
Then, hot water from the water tank 13 passes through the water pipe 11, and the condenser 8 acts as an air heater using the hot water, raising the temperature of the greenhouse 1.

先に説明した凝縮器(空気加熱器)の次に水による空気
冷却器を分離して設置し所期の目的を達する様にした装
置に於ては、夜間暖房の時は水による空気冷却器をその
まま空気加熱器とし、ポンプ12で水槽13の温水を循
還させれば良い。
In the device described above, in which a water-based air cooler is installed separately next to the condenser (air heater) to achieve the intended purpose, the water-based air cooler is used for night heating. It is sufficient to use the air heater as it is and circulate the hot water in the water tank 13 with the pump 12.

前記実施例に基き冬期夜間この暖房に必要な熱量を計算
して見ると次の通シである。
Based on the above embodiment, the amount of heat required for heating at night during winter is calculated as follows.

夜間の外気温な0℃とし、温室1内の空気温を10’C
Vc保つとすると屋根・外壁(前記の通り総面積を20
0m2 とする)を通って失なわれる熱量は(湯室の
中にカーテン1層を設置した場合の経験による熱貫流率
は大体3.0kcat/rrL2 ・℃・時である)3
.0kcat/rrL2・℃・時X200m2X(10
−0)’C=6000k cat/時これだけ熱を補給
すれば温室1内を10℃に保つことができるわけである
The outside temperature at night is 0°C, and the air temperature inside greenhouse 1 is 10'C.
If Vc is maintained, the roof/outer wall (as mentioned above, the total area is 20
The amount of heat lost through the curtain (assumed to be 0 m2) is (based on experience, when one layer of curtain is installed in the bathtub, the heat transfer coefficient is approximately 3.0 kcat/rrL2 ・℃・hour) 3
.. 0kcat/rrL2・℃・hour×200m2×(10
-0)'C=6000k cat/hour If this amount of heat is supplied, the temperature inside the greenhouse 1 can be maintained at 10°C.

そして暖房時間を12時間とすれば必要全熱量は 6000kca77時X12時=72000kca7/
日 であシ、先に計算した水槽8の蓄熱量は83800k
c a 11日であるからこの蓄熱量だけで充分まかな
うことができる。
If the heating time is 12 hours, the total amount of heat required is 6000kca77 hours x 12 hours = 72000kca7/
The amount of heat stored in water tank 8 calculated earlier is 83,800k.
c a Since it is 11 days, this amount of heat storage alone is enough to cover the entire time.

即ち快晴でありさえすれば燃料を燃やすことな(温室1
を適温に保つことができるわけである。
In other words, as long as the weather is clear, there is no need to burn fuel (Greenhouse 1)
This means that it can be kept at an appropriate temperature.

曇天・雨天の山ま止むに得ず燃料を使うことになるが表
日本ではその日数は少ないから本発明による装置を備え
ることで温室栽培の燃料を大量に節約でき、しかも温室
内の湿度を適度に低く保つことで病害を防止し且つ植物
の生育を促進することができて斯界に貢献すること大な
るものがある。
It is unavoidable to use fuel during cloudy and rainy days, but in Japan there are only a few such days, so by equipping the device according to the present invention, a large amount of fuel can be saved in greenhouse cultivation, and the humidity inside the greenhouse can be maintained at an appropriate level. By keeping the temperature low, diseases can be prevented and plant growth can be promoted, making a great contribution to this world.

【図面の簡単な説明】 第1図は本発明の詳細な説明する要領図であシ、第2図
は第1図に於て8で示す熱交換器の構造例を説明する詳
細斜視図である。
[BRIEF DESCRIPTION OF THE DRAWINGS] FIG. 1 is a schematic diagram explaining the present invention in detail, and FIG. 2 is a detailed perspective view explaining a structural example of the heat exchanger shown at 8 in FIG. 1. be.

Claims (1)

【特許請求の範囲】 1 温室にヒートポンプによる空気調和装置と水温の上
昇によシ蓄熱することを目的とする水槽とを設け、冬期
晴天臼の昼間太陽熱によシ温室内の温度・湿度が必要以
上に上がることを防止するため上記空気調和装置を運転
し、その空気調和のため取除かれる熱量を上記水槽内の
水温を上げることで畜熱し、夜間寒冷時に水槽内の蓄熱
分を温室内に放熱してその温度を適温に保つことを特徴
とする温室運営方法。 2 温室にヒートポンプによる空気調和装置を設は通風
機により温室内の空気が空包調和装置を通って循還する
様にし、冬期晴天臼の昼間温室の空気がヒートポンプの
蒸発器(空気冷却器)を通って冷却除湿され引続きヒー
トポンプの凝縮器(空気加熱器)及び水にする冷却器を
通って温室に適応する温度迄暖められて温室に戻る様に
し、この水による冷却器に別に設けた水槽内の水をポン
プで循環させて空気調和のため取除か扛た余分の熱量を
水槽内の水温を上げることで蓄熱し、夜間寒冷時に水槽
の温水をポンプで水・空気熱交換器の水側な通して循環
し、一方通風機により温室内の空気を上記熱交換器の空
気側を通して循環させて温水から熱を受は温室の気温を
適温に保つ様にしたことを特徴とする温室の空気調和装
置。 3 ヒートポンプの凝縮器(空気加熱器)及び水による
冷却器として共通のフィン群を貫通する2つの管路が交
互に配置されて構成され、第1管路には冷媒を通し第2
管路には水を通し、冷媒の凝縮によシ発生する熱量の一
部を空気に与え残部を水に移す様にした冷媒凝縮熱交換
器を用いる事を特徴とする特許請求の範囲第2項記載の
温室の空気調和装置。
[Scope of Claims] 1. A greenhouse is equipped with an air conditioner using a heat pump and a water tank whose purpose is to store heat by increasing the water temperature, so that the temperature and humidity inside the greenhouse can be adjusted by the daytime solar heat of the winter clear sky. In order to prevent the temperature from rising above the above level, the air conditioner is operated, and the amount of heat removed for air conditioning is stored by raising the water temperature in the water tank, and the heat stored in the water tank is transferred into the greenhouse during cold nights. A method of operating a greenhouse characterized by radiating heat and maintaining the temperature at an appropriate temperature. 2. Install an air conditioner using a heat pump in the greenhouse so that the air inside the greenhouse is circulated through the air conditioner using a ventilator, and the air in the greenhouse during the day when the weather is sunny in winter is transferred to the heat pump's evaporator (air cooler). The water is then cooled and dehumidified through the heat pump condenser (air heater) and the water cooler, where it is heated to a temperature suitable for the greenhouse and returned to the greenhouse. The water inside the aquarium is circulated by a pump and removed for air conditioning.The excess heat is stored by raising the temperature of the water in the aquarium, and during cold nights, the hot water in the aquarium is pumped to cool the water in the water/air heat exchanger. The greenhouse is characterized in that the air inside the greenhouse is circulated through the sides of the heat exchanger, and the air inside the greenhouse is circulated through the air side of the heat exchanger using a ventilation fan to receive heat from the hot water and maintain the temperature of the greenhouse at an appropriate temperature. Air conditioner. 3 The heat pump condenser (air heater) and the water cooler are constructed by having two pipes that pass through a common group of fins arranged alternately, and the first pipe passes a refrigerant and the second pipe passes through a common fin group.
Claim 2, characterized in that a refrigerant condensing heat exchanger is used in which water is passed through the conduit and part of the heat generated by condensing the refrigerant is transferred to the air and the remainder is transferred to the water. Greenhouse air conditioner as described in section.
JP55128434A 1980-09-16 1980-09-16 Greenhouse air conditioning methods and equipment Expired JPS5922143B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55128434A JPS5922143B2 (en) 1980-09-16 1980-09-16 Greenhouse air conditioning methods and equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55128434A JPS5922143B2 (en) 1980-09-16 1980-09-16 Greenhouse air conditioning methods and equipment

Publications (2)

Publication Number Publication Date
JPS5752729A JPS5752729A (en) 1982-03-29
JPS5922143B2 true JPS5922143B2 (en) 1984-05-24

Family

ID=14984642

Family Applications (1)

Application Number Title Priority Date Filing Date
JP55128434A Expired JPS5922143B2 (en) 1980-09-16 1980-09-16 Greenhouse air conditioning methods and equipment

Country Status (1)

Country Link
JP (1) JPS5922143B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1707912A1 (en) * 2005-04-01 2006-10-04 Fiwihex B.V. Heat exchanger and greenhouse
NL1029280C1 (en) 2005-06-17 2006-12-19 Fiwihex B V Housing with a cooling.
RO138182A2 (en) * 2022-11-10 2024-05-30 Institutul Naţional De Cercetare-Dezvoltare Pentru Maşini Şi Instalaţii Destinate Agriculturii Şi Industriei Alimentare Automated plant for collecting atmospheric humidity

Also Published As

Publication number Publication date
JPS5752729A (en) 1982-03-29

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