JPS58220627A - Environment control apparatus for heating underground heat exchange greenhouse - Google Patents
Environment control apparatus for heating underground heat exchange greenhouseInfo
- Publication number
- JPS58220627A JPS58220627A JP57102370A JP10237082A JPS58220627A JP S58220627 A JPS58220627 A JP S58220627A JP 57102370 A JP57102370 A JP 57102370A JP 10237082 A JP10237082 A JP 10237082A JP S58220627 A JPS58220627 A JP S58220627A
- Authority
- JP
- Japan
- Prior art keywords
- greenhouse
- air
- heat
- temperature
- underground
- 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.)
- Pending
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/25—Greenhouse technology, e.g. cooling systems therefor
Landscapes
- Greenhouses (AREA)
- Central Heating Systems (AREA)
- Air Conditioning Control Device (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
温室栽培に使用する石油類の消9R量は非常に多量であ
るが、石油ショック以来この省エネルギー化が高まり、
この有効な方法としては、太陽熱の利用が実用化さfま
た。特に本発明と関連する地中熱交換暖房は設備費が安
く、蓄熱効果については、初期的実用効果を発揮してい
るが′1:1
、まだ研究の余地が残さiている。反面、その欠・陥と
して、夜間に地中熱を引出す時、温室内の湿度が^くな
り、外気が低温の時は温室の内壁、トマト、キュウリ等
の農作物の葉及び果実実等に結露し、細菌やカビ類の活
性化による疫病や呼吸作用の低下の原因となっていた。[Detailed Description of the Invention] The amount of petroleum used in greenhouse cultivation is extremely large, but since the oil crisis, energy conservation has increased,
An effective method for this is the use of solar heat. In particular, the geothermal heat exchange heating system related to the present invention has low equipment costs and has shown initial practical effectiveness in terms of heat storage effect; however, there is still room for further research. On the other hand, the drawback is that when extracting geothermal heat at night, the humidity inside the greenhouse increases, and when the outside temperature is low, condensation forms on the inner walls of the greenhouse, leaves and fruits of crops such as tomatoes and cucumbers. However, the activation of bacteria and fungi caused epidemics and decreased respiratory function.
また日中の地中への蓄熱効果を上げるため、換気を極力
押えるためCo、が不足し、夜間の湿度の上列と、日中
のCo、の不足がこの/ステムの犬^な欠陥上なってい
た。第1〜第4の発明は、この7ステムの熱効率を更に
高め、夜間の温室内の湿度を下げ、日中の室内の高温度
抑制を効果的に行い、併せて日中のCO,濃度を上げ、
細菌やカビ類を吸着除去し、これをより省エネルギー下
で行うことを目的と(7た装置にである。In addition, in order to increase the heat storage effect underground during the day, ventilation is suppressed as much as possible, resulting in a lack of Co, and the upper row of humidity at night and the lack of Co during the day cause this /stem dog^^ defect. It had become. The first to fourth inventions further enhance the thermal efficiency of these seven stems, lower the humidity in the greenhouse at night, effectively suppress high temperatures in the room during the day, and also reduce CO and concentration during the day. Raise,
The purpose of this device is to adsorb and remove bacteria and mold, and to do this in an energy-saving manner.
上記の目的を達成するための杭−め発明は、加熱により
簡単に再生できる吸着創生としてアルミナゲル、合成ゼ
オライト、活性炭等の単独または混合状態の吸着j−の
Iツ「冗個所に、円心回転式送風管をを如付け、該送風
管に対し、除湿(吸着)用送風□!□と、再生(脱着)
中熱)虱とを交互に送風し、吸着層出口にエンタルピー
降下用のクーラー及び加湿器を取り付り、除湿、加湿、
再生の切換を室内にセットしたヒュミデイスタット隅整
差の時間中と、吸着剤の能力減退(吸着熱の減少)を指
示するサーモスタットの設定温度で行い、再生の終r及
び除加湿の開始をヒュミデイスタットの設定の上限また
は下限及び再正適正温度を指示するサーモスタットの設
定温度で行い、再生のための熱源は昭和55年特許願第
62953号の高負荷小型燃焼炉付高圧バーナーを[重
用することを特徴とする地、中熱交換式湯室暖房の環境
調整装置である。In order to achieve the above object, the present invention is based on the adsorption of alumina gel, synthetic zeolite, activated carbon, etc. alone or in a mixed state as an adsorption material that can be easily regenerated by heating. Attach a center-rotating type blower pipe, and use the blower □!□ for dehumidification (adsorption) and regeneration (detachment).
A cooler and a humidifier for enthalpy reduction are installed at the outlet of the adsorption layer to dehumidify, humidify,
The regeneration is switched during the corner adjustment time of the humidistat set indoors and at the set temperature of the thermostat that instructs the decrease in adsorbent capacity (reduction in heat of adsorption), and the end of regeneration and the start of dehumidification. The heat source for regeneration is a high-pressure burner with a high-load small combustion furnace of Patent Application No. 62953 filed in 1981. This is an environment control device for indoor and medium heat exchange type hot water room heating.
第2の発明は、地中蓄熱送風パイプに多数の孔または吹
出口を設け、パイプの外側に天燃産膠質土、斜方沸石等
の層を作りまたはパイプを使用せ^状の膠質土、斜方沸
石等の層を作り、蓄熱すべき温風をこの1−中に導き、
同物質の強大なる吸水力により、蓄熱時に起る凝縮水分
及びt41−F水等を吸11ヌして、パイプ内への水の
浸入を防ぎ、蓄熱1轡内の空気の流通をよくシ、蓄熱効
果及び熱交換効果を向上さぜることを特徴とする温室の
地中蓄熱装置である。The second invention is to provide an underground heat storage blower pipe with a large number of holes or outlets, and to create a layer of natural colloidal soil, chabazite, etc. on the outside of the pipe, or to use the pipe to create a layer of colloidal soil, chabazite, etc. Create a layer of chabazite, etc., and guide the warm air to store heat into this layer.
Due to the strong water absorption power of this material, it absorbs condensed moisture and t41-F water that occur during heat storage, prevents water from entering the pipes, and improves air circulation within the heat storage tank. This is an underground heat storage device for a greenhouse, which is characterized by improving heat storage and heat exchange effects.
NXAの発明は、日中の温室内の高温抑制は第1項と同
じ方法の多面的吸着F輪を使用して湿分及び有害物質を
吸着除去し、吸着熱により温度が上昇した空気を、吸着
層出tjにセットした水冷クーラーで冷却し、併せて空
気のエンタルピーを下げ、この低湿度(RH20%以下
)、低エンタルピーの空気を室内にセット(7た加湿器
または細g発生装置の水滴中を通過させ、この空気の旺
盛なる気化熱により、室内の空気を冷却し、温室内の温
度及び湿度を栽培上ベストの環境状態にコントロールす
ると共に、吸熱した水は廃棄せず温室外に備けたクーリ
ングタワーにより冷却し、これを循環して行う、こ、J
:を特徴とした温室の冷却及び環境装置である。NXA's invention suppresses the high temperature inside the greenhouse during the day by adsorbing and removing moisture and harmful substances using multifaceted adsorption F-rings in the same manner as in Section 1. The adsorption layer is cooled with a water cooler set at the outlet tj, and the enthalpy of the air is also lowered, and this low humidity (RH 20% or less), low enthalpy air is set indoors (7) using water droplets from a humidifier or fine g generator. The strong heat of vaporization of this air cools the indoor air, controlling the temperature and humidity inside the greenhouse to the best environment for cultivation, and the water that has absorbed heat is stored outside the greenhouse instead of being discarded. This is done by cooling with a girder cooling tower and circulating it.
This is a greenhouse cooling and environmental device featuring:
第4の発明は第1項と同じ多面曲成イイ階に地中熱父換
式爾室暖房に係わる室内または室外の空気を循環通函さ
せて、栽培上有害なる物質例えば過剰の湿分、COl、
NH,、FOHO,害菌類、殺菌剤の残留ガス等を吸着
除去(7、サーモスタット、ヒュミグイスタット、ガス
flll)ill I’ip等により栽培上ベストの環
境を連続してコントロールし、吸着剤の再生を昭和55
年特許顧第62953号の高負荷燃焼炉付高圧バーナー
をCO,発生機として兼用し、通′帛日中行われる吸小
剤の再生時に廃熱の一部を温宰内に放出してCO,の補
給を行い、大部分の廃熱を地中へ蓄熱することを特徴と
する地中熱交換式温室11iff房の蓄熱及び環境調整
装置である。The fourth invention is to circulate indoor or outdoor air related to underground heat exchange type rear room heating on the same multi-curved floor as in the first item, and to eliminate substances harmful to cultivation, such as excessive moisture. COL,
Adsorb and remove NH, FOHO, harmful fungi, residual gas from disinfectants, etc. (7. Thermostat, humiguistat, gas full). Continuously control the best environment for cultivation using I'ip, etc., and remove the adsorbent. Revival of 1975
The high-pressure burner with a high-load combustion furnace disclosed in Patent No. 62953 of 2013 is also used as a CO generator, and a part of the waste heat is released into the heating chamber during the regeneration of the small absorbent during the entire working day. This is a heat storage and environment adjustment device for an underground heat exchange type greenhouse 11iff, which is characterized by replenishing heat and storing most of the waste heat underground.
第1項及び第4項の発明において、昭和55年特許i第
62953号の高負荷小型健焼炉付高王バーナーを使用
するメタリットは次のとおりである。即ち、従来は吸着
剤の再生熱源として4沼電熱を使用しており、 110
0K/Hr の電力を使用するこの稗の装置は珍しく
なかった。しかし昨今のエネルギー事情では許されない
ことであり、またこの種の大型装置へを農業関係に使用
する例が少ないため、こ、の熱源の研究開発が行われて
いなかった。本発:明では、昨今のエネルギー事情や農
業関係への新規開発のため、どうしてもこの間−を解決
しなくては実用効果を上げることができなかったもので
ある。本発明では先に出願した[高負荷小型燃焼炉付高
圧バーナー」を吸着剤の再生熱源に採用し、た。その特
長とする点は次項のとおりである。In the inventions of Items 1 and 4, the Metalit using the high-load small-sized hard-burning furnace-equipped Takao burner of Patent I No. 62953 of 1980 is as follows. That is, conventionally, Yonkuma electric heat was used as a regenerating heat source for adsorbent, and 110
This type of device using 0K/Hr power was not uncommon. However, current energy conditions do not allow this, and there are few examples of large-scale equipment of this kind being used in agriculture, so research and development of this heat source has not been carried out. In the present invention, due to the recent energy situation and new developments related to agriculture, it was necessary to solve this problem in order to achieve practical effects. In the present invention, the previously applied ``High Pressure Burner with High Load Compact Combustion Furnace'' is used as the heat source for regenerating the adsorbent. Its features are as follows.
(1)燃焼炉が小さく、能力が大きく負荷率は普通燃焼
炉の30〜50倍である。(1) The combustion furnace is small and has a large capacity, and the load factor is 30 to 50 times that of a normal combustion furnace.
(2)火炎が短く、燃焼炉内で完全燃焼し、1000℃
以上熱ガスを吐出する〇
(3)熱ガスの圧力が高い(400〜2000rula
q)ので、再生時の吸着剤層や、廃熱風の地中の蓄熱層
の圧力抵抗に充分拐ち勝つ能力をもっている。(2) The flame is short, complete combustion occurs in the combustion furnace, and the temperature reaches 1000℃.
(3) The pressure of the hot gas is high (400 to 2000 rula)
q) Therefore, it has the ability to sufficiently overcome the pressure resistance of the adsorbent layer during regeneration and the underground heat storage layer of waste hot air.
(4)熱交換器を使用せず、バーナーより発生した熱風
を吸着層へ直ちに送り込むことができる。(4) Hot air generated from a burner can be immediately sent to the adsorption layer without using a heat exchanger.
(5)熱ガスの温度調整はエジェクター等により過剰空
気を導入し、再生適正篇度(500’C)にすることが
簡単にできる。(5) The temperature of the hot gas can be easily adjusted by introducing excess air using an ejector or the like to bring it to a temperature suitable for regeneration (500'C).
(6) Co、の発生源として兼用することができる
以上のように大きな特長を有し、大型の燃焼炉や熱交換
器を必要きし、熱風の吐出圧力の低い4當のバーナーは
再生熱源には使用できない次に第1〜第4の発明に関す
る実施例を説明するに、@1〜第4の発明の実施例は共
通するにつき図面に依拠して一括説明する。(1)は温
室、(2)は温室(1)内の高温空気用ピッ)、(31
は該ピ熱により再生できる吸着剤、例えばアルミナゲル
、7リカゲル、活性炭等を単独または混合の状態きなっ
ている多面的吸着層、(7)は再生廃熱送風パイプ、a
りは再生熱風送風パイプ、(81,01は地下熱吸引パ
イプ、(9)は吹出兼吸引パイプ、(11)は再生用バ
ーナー、GIGま吸着用ブロア、03は高負荷撚焼炉付
高圧バーナー(再生能Co、発生fi ) 、(+41
は価焼空気兼再生用ブロア、6つは再生用空気吸込パル
プ、(16)は温室(1)内の吸着用吸込9気パルプ、
a′0は地下蓄熱空気に係わる吸着用吸込空気パルプ、
(+81は再生熱風廃棄パルプ、(11は地下蓄熱用
再生熱風給気パルプ、■)は再生熱風Co、供給パルプ
、C1)は温室(1)内のクーリングタワー、(22)
は該温室(1)外のクーリングタワー、りXま冷却、加
湿機、囚)は冷却機、(25)、(26)はポンプ、(
a)は温室(1)内の空気、(b)は吸着層入口、(c
)は吸着層出口、(d)はクーラー通過後の温陣−等の
計測部、(e)はクーりングタワー通過後の温度等の唱
測部、(f)は吸着層入口、ト1、伽1、←りは共に水
温計測部、(27)〜C36)までのものは、本件出願
人の出願に係る昭和55年特許願第62953号の散部
に関する構成部材を表示したものである。以下順次説明
すると、 (27)は円筒型−焼室、(2R)は外筒、
■)は内張り部、(30)は絞り部、(31)は案内翼
、C32)は空気入口、(33)はバーナーノズル、0
4)は燃料入口、(35)は燃焼用空気入口、(36)
はブロアー、(40)〜(至)1才でのものは、本願の
第1、第4の発明に係る液体郷料を使用した場合の吸着
装置(イ)に関するものである。以下111次説明する
と、(40)は廻転式送風管、(41)は送風管例転モ
ーター、(42)は除澤用送風機、(43)は除湿m空
気人口、(44)は再牛用送風機、(45)は水冷クー
ラー、(46Xま加湿器、(47Nま調整空気出口、(
48)は除湿空気用ダンパー、(49)は再生空気用ダ
ンパー、(50)は再生排気出口である。(6) Can be used as a source of Co Next, embodiments related to the first to fourth inventions will be described. Since the embodiments of the first to fourth inventions are common, they will be collectively explained with reference to the drawings. (1) is a greenhouse, (2) is a hot air pipe in the greenhouse (1), (31
(7) is a multifaceted adsorption layer containing an adsorbent that can be regenerated by the heat, such as alumina gel, 7-lica gel, activated carbon, etc., alone or in a mixed state; (7) is a regenerated waste heat blowing pipe;
(81 and 01 are underground heat suction pipes, (9) are blow-off and suction pipes, (11) are regeneration burners, GIG adsorption blowers, and 03 are high-pressure burners with high-load twisting furnaces. (Regeneration capacity Co, generation fi), (+41
Blower for burning air and regeneration, 6 air suction pulp for regeneration, (16) 9 air suction pulp for adsorption in greenhouse (1),
a′0 is suction air pulp for adsorption related to underground heat storage air;
(+81 is recycled hot air waste pulp, (11 is recycled hot air supply pulp for underground heat storage, ■) is recycled hot air Co, supply pulp, C1) is the cooling tower in the greenhouse (1), (22)
is the cooling tower outside the greenhouse (1);
a) is the air inside the greenhouse (1), (b) is the entrance of the adsorption layer, (c)
) is the adsorption bed outlet, (d) is the measurement part for temperature etc. after passing through the cooler, (e) is the measurement part for temperature etc. after passing through the cooling tower, (f) is the adsorption bed inlet, 1 and ← are both water temperature measuring parts, and (27) to C36) are the constituent members related to the scattered part of Patent Application No. 62953 filed in 1982 by the present applicant. To explain in order below, (27) is a cylindrical baking chamber, (2R) is an outer cylinder,
■) is the lining part, (30) is the constriction part, (31) is the guide vane, C32) is the air inlet, (33) is the burner nozzle, 0
4) is the fuel inlet, (35) is the combustion air inlet, (36)
(40) to (to) 1 year old relate to an adsorption device (a) when using the liquid material according to the first and fourth inventions of the present application. To explain in the following 111 steps, (40) is a rotary blower pipe, (41) is a blower pipe rotation motor, (42) is a blower for removing sawdust, (43) is a dehumidifying m air population, and (44) is for re-cow use. Air blower, (45) is a water cooler, (46X humidifier, (47N) adjustable air outlet, (
48) is a damper for dehumidified air, (49) is a damper for regenerated air, and (50) is a regenerated exhaust outlet.
次に第1の発明の作用につき説明すると、本発明の前提
となる地中熱交換式温室(1)の構造は通常透明のプラ
スチックやガラス等により二重構造になっており、温室
(1)の内壁の温間と外気温IWとの関係は、外気が一
5℃の吉永で、+3℃稈度である。従って、内壁に接触
している温室(1)内の空気はり、P、3″Cであり、
室内の温度が15℃きすれば、RH40’1以下に除湿
するこ々により結露を防止するこ吉がで去る。又植物体
への結露は、温室(1)内の相対湿彦を80チ以下にす
ることにより防Iトすることができる。実験によれば、
第1図の1.通り、1ooom’の温室・:蒼
(1)に対し、吸着剤500 KFを使用した装置を運
転し、夜間1回の再生を行うことにより10〜12時間
の除湿を行ったところ、この環境を維持し、温室(1)
内壁及び植物体への結露を完全に貼I卜することができ
た。この具体例は第1図のとおりである。Next, to explain the operation of the first invention, the structure of the underground heat exchange type greenhouse (1), which is the premise of the present invention, is usually a double structure made of transparent plastic, glass, etc. The relationship between the warmth of the inner wall and the outside temperature IW is +3°C in Yoshinaga where the outside air is -5°C. Therefore, the air beam in the greenhouse (1) in contact with the inner wall is P, 3″C,
If the indoor temperature rises to 15°C, dehumidification will occur to prevent condensation by reducing the humidity to below RH40'1. Further, dew condensation on plants can be prevented by reducing the relative humidity in the greenhouse (1) to 80 degrees or less. According to experiments,
1 in Figure 1. When we dehumidified the greenhouse for 10 to 12 hours by operating a device using 500 KF of adsorbent and regenerating it once at night in a 100m greenhouse (1), we found that this environment Maintain and Greenhouse (1)
It was possible to completely prevent dew condensation from forming on the inner walls and plants. A specific example of this is shown in FIG.
第2の発明については、地中蓄熱パイプ(7)を有孔に
し、パイプ(7)外周辺に水分吸1夕兼蓄熱材即ち膠質
上、斜方沸石等を活性化した物質で1すさ100 u以
上の層(5)を作り、パイプの孔(9)を通じてこの1
−中へ蓄熱すべき、日中の温風及び吸着剤の再生廃熱及
びパイプ内の凝縮水分を送り込む仕組である。従来行わ
れている日中の温室(1)内の温風を送り込むパイプは
、地F水の浸入や熱の流出が多いため(吸水材がないた
め)パイプを有孔にすることがで粂なかった。本発明に
よれば、パイプ内に水の凝縮はなく、地F水の浸入を防
止し、水の流動による熱の移動もなくなり、従来のよう
にパイプ内の対流伝熱しか利用で舟なかったものを、本
発明では吸収兼蓄熱材より直接用=”” i’出tcと
、87き、ヵ7、熱効率が相当増加し、大きな特長を有
しているものである。本発明で特にこの吸収兼蓄熱材を
採用した理由は、吸収量が多く、吸水に当り人眼の凝縮
熱及びぬらし熱(heat of wetting )
9出すことにあるが、物性的にも、土壌や従来使用し
ている栗石と比べ比熱が^く熱伝導率が低いことで、即
ち吸水による潜熱の利用ができると4Vに、蓄熱量が多
く、熱の拡散が少く、断熱効果があり、強大な吸水力に
より、地F水や、凝縮水分を吸収して、それ等の流動に
よる熱の移動を防止し、地温を上昇させると共に、本発
明の湿分吸着装置(6)の負担を軽くする等の理由によ
るものである。その物性は第1表の通りである。Regarding the second invention, the underground heat storage pipe (7) is made perforated, and the outer periphery of the pipe (7) is filled with a moisture absorbing and heat storage material, that is, a substance made of colloid, chabazite, etc. Make a layer (5) of u or more, and pour this 1 through the hole (9) of the pipe.
- It is a system that sends warm air during the day, regenerated waste heat of the adsorbent, and condensed water in the pipes to be stored inside. The conventional pipes that send hot air into the greenhouse (1) during the daytime have a lot of infiltration of ground F water and the outflow of heat (because there is no water absorbing material), so it is not possible to make the pipes perforated. There wasn't. According to the present invention, there is no condensation of water inside the pipe, preventing the intrusion of groundwater, and there is no movement of heat due to the flow of water, instead of using only convection heat transfer inside the pipe as in the past. However, in the present invention, the thermal efficiency is significantly increased by direct use of the heat absorbing and heat storage material. The reason why this absorbent and heat storage material is particularly adopted in the present invention is that it has a large absorption amount, and when it absorbs water, it absorbs the condensation heat and heat of wetting of the human eye.
9, in terms of physical properties, it has a specific heat capacity and low thermal conductivity compared to soil and the conventionally used chestnut stone, which means that if the latent heat from water absorption can be used, it can store a large amount of heat at 4V. , has little heat diffusion, has a heat insulating effect, and has a strong water absorption power that absorbs ground F water and condensed water, prevents heat transfer due to flow, and raises ground temperature. This is for reasons such as reducing the burden on the moisture adsorption device (6). Its physical properties are shown in Table 1.
第1表 保熱(蓄熱)材の比較
材料名 比 熱 熱伝導率 空気の流通 断熱性吸水
率栗石 0.22 0.7〜09 ヨ シ ナシナシ
通常日中の室内温度は30℃以上となり、この高温の空
気を地中へ蓄熱するのは、従来通りの方法であるが、本
発明では、こわと同時に吸着剤の加熱再生を行い、40
〜90℃の高温度の廃熱の大部分を地中へ送り込むこと
を特長とするが、通常の吸着除湿装置の場合は、この廃
軌をすべて外気中に廃棄するのであるが、本発明ではこ
れを地中に蓄熱し、夜間にこのエネルギーを利用するの
で、100.000〜160.000eal/da’、
y以十を有効に利用することができる。Table 1 Comparative material names for heat retention (thermal storage) materials Specific heat Thermal conductivity Air circulation Insulating water absorption rate Kurite 0.22 0.7~09 Yoshi Nashinashi The indoor temperature during the day is usually over 30℃, and this Storing heat from high-temperature air underground is a conventional method, but in the present invention, the adsorbent is heated and regenerated at the same time as the stiffening.
The feature is that most of the waste heat at a high temperature of ~90°C is sent underground, but in the case of normal adsorption dehumidification equipment, all of this abandoned track is disposed of into the outside air, but in the present invention, This heat is stored underground and this energy is used at night, so 100.000 to 160.000 eal/da',
y or more can be used effectively.
従って外気が一5℃以下の時は、従来の方法で −は
室内温度が8℃以上にならないため、暖房を′行わなけ
ればならない。本発明の方法によれば、第3図のように
この暖房は必要なく、また地中温度については、従来1
6℃N上Iこならなかったものを19°C〜22℃まで
上げることができる。従って長野系や北陸地方のように
外気温が低い所や、日照時間の短い所及び連続悪天候の
場合でも、従来8V稈度しか保温できなかった温室内の
温度を暖房機を使わな゛くても12′C以主にすること
ができるので、これ等の4[lJ方の農家に大きな希望
を与えるものである。この効果をもたらす原動力は新規
発明による蓄熱材の効W・であり、原理は吸水時の11
多縮軌及びぬらし熱によるもので、150〜800ca
l/吸水にりの潜熱による髭熱である。Therefore, when the outside temperature is below 15°C, the indoor temperature cannot rise above 8°C using conventional methods, so heating must be performed. According to the method of the present invention, this heating is not necessary as shown in Fig. 3, and the underground temperature is lower than the conventional one.
It is possible to raise the temperature above 6°C to 19°C to 22°C. Therefore, even in places like Nagano and Hokuriku regions where the outside temperature is low, the sunshine hours are short, or there is continuous bad weather, the temperature inside the greenhouse, which could only be maintained with an 8V culm, can be maintained without using a heater. Since it is also possible to make 12'C or less, it gives great hope to these 4[lJ farmers. The driving force behind this effect is the effect of the newly invented heat storage material W. The principle is 11 when water is absorbed.
150 to 800 ca due to multiple contractions and wetting heat
This is beard heat due to the latent heat of l/water absorption.
坑3の清明である1品室(1)内の畠ζ品抑制及び温度
1.、l整の作用について峠、明する。日中の温室(1
)内の適温、適湿は、20〜25℃、R1(60〜80
%とされているが、3月以降は35℃以上に過温され、
深川:も60 ’IA以下に下がることがある。しかる
に、本発明の吸着メカニズムを有効に活用するこ七によ
って、高温を抑制することができると共に、この7ステ
ムの環境船がすべて解決され、(7かもプロセスが−F
とな抄、環境FjM整がスムーズtこ行わわる。ところ
で、この高温抑制については、従来広のような方法が行
わわていたが、ぞのス・jν果は不完全であった。1. Product suppression and temperature in the 1 product room (1), which is clear in the hole 3. , Toge explains the effect of l adjustment. Greenhouse during the day (1
) The appropriate temperature and humidity are 20-25℃, R1 (60-80
%, but from March onwards, it has been overheated to over 35℃,
Fukagawa: It can also drop below 60'IA. However, by effectively utilizing the adsorption mechanism of the present invention, the high temperature can be suppressed, and all of these 7-stem environmental vessels can be solved (7 also the process can be -F
Tona-sho, the environment FjM adjustment is done smoothly. By the way, methods such as Hiro's have been used to suppress this high temperature, but the results were incomplete.
即ち、(1)換気に、よる方法、(2)細輯による方法
、(3)冷却…による方法の3う1″であhlこの中(
1)の方法によt7ば、温室(1)内のfgA度を外気
温度に対し、その5〜7 ”Cプラス相度の冷却、即ち
室内龜度35℃、外気25℃の時は、30〜32℃程度
の冷却が限度である。更に(2)の方法によれば、室内
の温度が過剰となり室内温度もマイナス2〜3C程度の
冷却、即ち外気温吐25“C1室内温度35′℃の時、
32〜33℃程度の冷却が限度で、高温の抑制にはなら
なかった。(7かるに、本発明の方法は第7図の如く換
気導入する外気を、水冷スフ九)で洗浄冷却し、湿度の
上昇した空気を多面的吸着#]6)内を通して、RH平
均30チ以下にし、この時吸着潜熱により10〜15℃
渦度上昇した空気を吸着1@出口にセットされた冷却機
c24)により第7図及び第2表の如く冷却すると共に
、エンタルピーを下げ、この低湿奔、低エンタルピーの
空気を温室(1)内または吸着装置にセットした加湿兼
クーリングタワー(21)の水滴中を通過させ、乾燥空
気の旺盛なる気化潜熱により、この時の外気の湿球温度
以下、例えば外気の誹・・椋温度が18℃、温室(1)
内温度が35℃の時、この方法によれば、尋人外気を第
7図及び第2衣の如く、15〜17℃まで下げることが
できるので、温室内を25℃以下にするこ七がでAる。In other words, (1) a method using ventilation, (2) a method using narrow ventilation, and (3) a method using cooling...
According to the method of 1), the fgA degree in the greenhouse (1) is 5 to 7"C relative to the outside air temperature, that is, when the indoor air temperature is 35°C and the outside air temperature is 25°C, the fgA degree in the greenhouse (1) is 30°C. The limit is cooling to about ~32°C.Furthermore, according to method (2), the indoor temperature becomes excessive and the indoor temperature is also cooled to about -2~3°C, that is, the outside air temperature is 25'C, the indoor temperature is 35'C. time,
Cooling was limited to about 32 to 33°C, and high temperatures were not suppressed. (7) As shown in Fig. 7, the method of the present invention cleans and cools the outside air introduced for ventilation with a water-cooled suction cup (9), and passes the air with increased humidity through a multifaceted adsorption chamber (6) with an average RH of 30. 10 to 15℃ due to the latent heat of adsorption.
The air with increased vorticity is cooled by adsorption 1@cooler c24) set at the outlet as shown in Figure 7 and Table 2, and the enthalpy is lowered, and this low-humidity, low-enthalpy air is transferred into the greenhouse (1). Alternatively, the water is passed through the water droplets of the humidifying/cooling tower (21) set in the adsorption device, and due to the vigorous latent heat of vaporization of the dry air, the temperature of the outside air at this time is below the wet bulb temperature, for example, the temperature of the outside air is 18℃, Greenhouse (1)
When the internal temperature is 35℃, this method allows the outside air to be lowered to 15-17℃ as shown in Figure 7 and No. 2. So Aru.
また、(の跣@鍼した水は廃棄せす゛、外部に川に設備
し7たクーリングタワー(羽)によね冷却し、て循環し
て使用するので、従来性われている、このトbのhθ;
と比べ、消費水量が大巾に節約できる。また外部のグー
リングタワーc23)の水の冷却力は、外気の湿球偏度
より若干商い帽り即ち第7図及び第2奴の如く外気湿球
渦m″15〜17℃の時、17〜191Cまで冷却する
ことができる。またこの時の浮塵の調整はヒュミディス
タットにより最適の環境に鯛整する。また、従来の細鮪
冷却方法では、温室(1)内のllが高くなりやすく、
そ謬黛化潜熱の利用はでをt+′いr、この志木発明C
才、温室(1)内の湿度に関係なく低渭度の空気を加渭
するので、高度の気化熱を利用できるため、利用効果が
大きい。In addition, the acupuncture water is not disposed of, but is cooled by a cooling tower (wings) installed outside the river, and then used for circulation. ;
Compared to this, water consumption can be significantly reduced. In addition, the cooling power of the water in the external Gooling Tower (c23) is slightly higher than the wet bulb polarity of the outside air, that is, when the outside air wet bulb vortex m'' is 15 to 17 degrees Celsius, as shown in Figure 7 and Figure 2, 17 It is possible to cool the sea bream to ~191C.Furthermore, the airborne dust at this time is adjusted to the optimum environment using a humidistat.Furthermore, with the conventional cooling method for thin tuna, the ll in the greenhouse (1) tends to become high. ,
The latent heat of oxidation can be utilized in this Shiki invention C.
In addition, since air at a low temperature is added regardless of the humidity inside the greenhouse (1), a high degree of heat of vaporization can be utilized, resulting in a large utilization effect.
第2表
外気温度 25℃60% D25°c wis℃11
ハウス内空気 35CRH4o% 118b吸着層
入口 25℃ 195% #17ce、着層出口
44℃ #20%’17dクーラー通過後 zg
c # 50% 1148′水温 22℃ −
bI # 25℃
c’# 20℃ −第4の発明の
装置の作用について説明すると、本発明に関する被吸着
物質の吸着能力を比較すると第13〜15図のとおりで
ある。これらの図の如く、合成ゼオライト、アルミナゲ
ルが本発明に適し、実験の結果も他の吸着剤より強力で
あることが判明した。即ち本発明に関する被吸着物質で
ある湿分、Co、% NJsホルムアルデヒド、ノ・ロ
ゲン系殺菌剤等の低分圧のカスに対して強力な吸着力を
有している。また、細菌やカビ類に対する吸着能力につ
いては、水分活性(Aw)に関係する吸着、脱水作用で
あり、細菌、カビ類のAWo、9〜0.78 に対し、
吸着剤は、Awo、 05〜02であり、吸着された害
菌類は、脱水状態になり死滅する。また、吸着されなお
生^残った害菌類はs >I’ll常サイクル的に行わ
れる吸St剤の加熱内生の時の120〜200 ℃の温
度により完全殺菌される。活性炭のように^分圧のガス
吸着を特長とする吸着剤は湿分、CO。Table 2 Outside air temperature 25°C 60% D25°c wis°C11
Air inside the house 35CRH4o% 118b Adsorption layer inlet 25℃ 195% #17ce, deposition layer outlet 44℃ #20%'17d After passing through cooler zg
c # 50% 1148'Water temperature 22°C - bI # 25°C c'# 20°C - To explain the operation of the device of the fourth invention, the adsorption capacity of the adsorbed substance according to the present invention is compared as shown in Figures 13 to 15. That's right. As shown in these figures, synthetic zeolite and alumina gel are suitable for the present invention, and experimental results have shown that they are stronger than other adsorbents. That is, it has a strong adsorption power to the adsorbed substances related to the present invention, such as moisture, Co, %NJs formaldehyde, and sludge with low partial pressure, such as nitrogen-based disinfectants. In addition, the adsorption ability for bacteria and molds is due to adsorption and dehydration effects related to water activity (Aw), and the AWo of bacteria and molds is 9 to 0.78.
The adsorbent is Awo, 05-02, and the adsorbed harmful bacteria become dehydrated and die. In addition, the harmful fungi that remain alive after being adsorbed are completely sterilized by the temperature of 120 to 200° C. during the heating process of the St absorbing agent, which is carried out in a regular cycle. Adsorbents like activated carbon, which are characterized by their ability to adsorb gases at partial pressures, absorb moisture and CO.
等極性ガスの吸着には適さないが、薬剤ガスや悪臭ガス
の吸着除去には活性炭の方が強力である。各吸着剤の1
時性を活がし、混合状態の吸着剤を使用するこ七が、本
発明の装置の特長であり、こ11を特に多面的吸着層(
剤)と称する所以である。Activated carbon is not suitable for adsorbing homopolar gases, but it is more powerful for adsorbing and removing drug gases and malodorous gases. 1 of each adsorbent
The feature of the device of the present invention is that it takes advantage of time and uses adsorbents in a mixed state.
This is why it is called ``agent''.
1’r 1.第4の発明につき、昭和55年特許願第6
2953号の[高負荷jド□:型、・、、燃焼炉付高圧
バーナー」を使用して実験を行った結果及び電力との比
較は次のとおりである。1'r 1. Regarding the fourth invention, patent application No. 6 of 1982
The results of an experiment using No. 2953 [High-load j-do□: type..., high-pressure burner with combustion furnace] and comparison with electric power are as follows.
本発明 電、力を使用した時
1、温室規模 1000ゴ 右同じ2
、吸着剤敏 500Rり
3、除PJ量 60[/
41再生エネルギー 4800 Kcad4
1.5、再生時間 1時間
6、内生熱源 灯 油 電力200V7
、エネルギー消費@ 61/Hr 60
KW/Hr8、消費金額 480、ゾT(r
1.200.ゾHr9、co、 の発生 でき
る できない以上の如く、本発明の灯油使用
の方法が、勝っておるばかりでなく、現在のエネルギー
事情では本発明の灯油方式を採用するしか道はないので
ある。This invention When electricity and power are used 1, Greenhouse scale 1000 Go Same as right 2
, Adsorbent density 500R3, PJ removal amount 60/41 Renewable energy 4800 Kcad4
1.5, Regeneration time 1 hour 6, Endogenous heat source Kerosene Electric power 200V7
, Energy consumption @ 61/Hr 60
KW/Hr8, consumption amount 480, ZoT(r
1.200. Generation of Hr9, co, Possible Impossible As described above, the method of using kerosene of the present invention is not only superior, but also the method of using kerosene of the present invention is the only option under the current energy situation.
第1の発明の9fi+、、果を説明すると、第1の発明
においては、加熱によシ簡単tこ再生で永る吸着剤(ア
ルミナゲル、7リカゲル、活性炭等)を充填した多目的
吸着層゛に、温室内または室外の空気を通ル゛Aさせ、
第1及び第2図のようにCO2゜湿分等を吸着除去する
と共に、必要に応じて吸着物質である湿分、COl等を
温室内に放出させ、さらに植物が0(1,を必費としt
21“い夜間には、温室内のco、 p昨を小さなし、
00.を十分に必要とする日中にCO,濃度を高くす
ると七ができるようになしたので、環境上自然に近い状
綿か、または七41以上のすぐねた環境を作り出すこと
がで粂るに至り、才だ霊宇内で栽培中の農作物の葉、茎
、果実等に対する結露を防止し、呼吸作用の低下をも未
然に防止すると共に、細菌やカビ類の活性化による疫病
をも解消せしめる等の利点を有している。To explain the 9fi+ effect of the first invention, in the first invention, there is a multi-purpose adsorption layer filled with an adsorbent (alumina gel, 7 lyca gel, activated carbon, etc.) that can be easily heated and regenerated for a long time. to pass air inside or outside the greenhouse,
As shown in Figures 1 and 2, CO2 and moisture are adsorbed and removed, and adsorbed substances such as moisture and CO1 are released into the greenhouse as needed. Toshit
21. At night, the greenhouse was heated to a small size,
00. By increasing the concentration of CO during the day when sufficient CO2 is required, it is possible to create a slender environment that is close to natural in terms of the environment, or a wet environment of 741 or more. Finally, it prevents dew condensation on the leaves, stems, fruits, etc. of crops being cultivated in Saida Reiu, prevents the decline in respiratory function, and eliminates epidemics caused by the activation of bacteria and fungi. It has the following advantages.
印、2の発明の効果につき説明すると、本発明の場合、
ttv、−F蓄熱用送風パイプに多数の穴または吹出口
を付け、かつパイプの外側に天然産膠質土、斜方沸石等
の層を杉成し、またはパイプを使用し、ないときは、塊
状の吸収材層を設け、蓄熱すべき温風を該層中へ導入し
、吸収材の強大な吸水力を利用して蓄熱時に生ずる凝縮
水分及び地下水等を吸収させて地下蓄熱1丁4 s)Z
風パイプ内への水の浸入を防止させると共に、蓄熱層内
の空気の流動を良好となし、蓄熱効果屑ひ熱交換効果を
アップさせたすく嘗また利点を有している。To explain the effect of the invention marked 2, in the case of the present invention,
ttv, -F A heat storage blowing pipe has many holes or outlets, and a layer of natural colloid, chabazite, etc. is formed on the outside of the pipe, or if the pipe is not used, it is made of lumpy A layer of absorbent material is provided, warm air to be stored is introduced into the layer, and the absorbent material's strong water absorption power is used to absorb condensed water and groundwater that occur during heat storage, resulting in underground heat storage (1 to 4 seconds). Z
It has the advantage of preventing water from entering the wind pipe, improving the flow of air within the heat storage layer, and improving the heat storage effect and waste heat exchange effect.
第3の発明の効果につき説明すると、本発明においては
、第1の発明において使用した多目的吸着層を介して温
室内の湿分及び有害物ηをrJN1層除去し、この吸清
熱により高温となった空気を水冷クーラーで冷却し7、
目1g9気のエンタルピーをFけ、下げられた低温度、
低下/タルビーの空気を加瀞器または細n発生V匝の水
滴中を通過させることにより、低湿度の空気の旺盛なる
気化熱より空気の温度を下げるので、市販温にすること
ができた。また、この裂開で使用する地下水は膨大なも
ので、地下水の少い所では使用することが不可能であり
、その上室内空気の湿度が商くて気化熱の利用ができな
いため、この効果は地下水の温度即ち顕熱のみの利用で
あったが、本発明は室内の湿態に関係なく、吸屓層によ
り除湿され超低湿度の空気を水滴に接触させるため、そ
の気化潜熱により空気の湿度が更に下がり、その上外部
に設ドしたクーリングタワーを通じて冷却循環させるの
で、消費水酸が非常に少縦である。本発明の装置の運転
実施例は第2表及び第7図の通りである。To explain the effect of the third invention, in the present invention, the moisture and harmful substances η in the greenhouse are removed by one layer of rJN through the multipurpose adsorption layer used in the first invention, and the heat absorption causes the temperature to rise. Cool the air with a water cooler7.
Fake the enthalpy of 1g9 qi, lower the temperature,
By passing the air in the lowering/Talby through the water droplets in the heat exchanger or the V-shaped container, the temperature of the air was lowered by the intense heat of vaporization of the low-humidity air, so the temperature could be brought to market. In addition, the amount of groundwater used in this cracking process is enormous, and it is impossible to use it in places where there is little groundwater.Moreover, the humidity of the indoor air is too high, making it impossible to utilize the heat of vaporization. In contrast, the present invention utilizes only the temperature of groundwater, that is, sensible heat, but the present invention brings ultra-low-humidity air, which has been dehumidified by a suction layer, into contact with water droplets, regardless of the humidity inside the room. Humidity is further reduced, and since cooling is circulated through a cooling tower installed outside, the amount of hydroxyl consumed is very small. Examples of operation of the apparatus of the present invention are shown in Table 2 and FIG.
第4の発明の効果については、上記第1の発明において
使用する多面的吸着層により害菌類を集菌吸着させ、吸
着した盲菌類は、従来性われているミクロフィルターl
こより濾過するのと!!4り、数10cm、厚さ以上に
充填された粒状の吸着剤層を害菌を含んだ空気が抵抗し
て通過するので、濾過とはその仕組が全く異なり、吸着
により完全に除去されると共に、吸着後の害菌は、吸着
剤の害菌よりの脱[原作用により死滅し、そゎ1以上、
。吸着斉IJIPi内(7) ”1.1対71カ85チ
以下、あるため、この環境では害菌が当然死滅し、また
吸着剤の再生が200℃以上の加熱により行われて吸着
された害菌がここで焼殺され、以上の三工程lこよって
殺菌が行われるものである。Regarding the effect of the fourth invention, harmful fungi are collected and adsorbed by the multifaceted adsorption layer used in the first invention, and the adsorbed blind fungi are removed by the conventional microfilter.
It's better to filter it! ! The mechanism is completely different from filtration, as the air containing harmful bacteria passes through a granular adsorbent layer filled with several tens of centimeters in thickness or more, with resistance, and is completely removed by adsorption. , the harmful bacteria after adsorption are killed by the original action of the adsorbent, and more than 1,
. Adsorption ratio within IJIPi (7) ``1.1 to 71 to 85 or less, so harmful bacteria will naturally die in this environment, and the adsorbent will be regenerated by heating above 200 degrees Celsius, reducing the amount of adsorbed harmful bacteria. Bacteria are burned to death here, and sterilization is accomplished through the above three steps.
第1図は本発明の地中蓄熱式温室暖房の環境調整装置に
おける第1の発明に関する温室内の相対湿庸比較図、第
2図は同県室内のCO1#度の比較図、第3図は同温室
内温度及び地下温度の比較図、第4.5図は第1の発明
における第1、第2実m例を示す図、第6図は第1.4
の発明において使用される高負荷小型燃焼炉付高圧粕炎
バーナーを示す図、@7図は@3の発明の実施の一例で
ある高温抑制を示す図、第8図は同温室内高温空気用地
下蓄熱工程を示す図、第8.9.10,11図は第2の
発明における実施例を示す図、第12図は第1.4の発
明において使用する液体燃料使用の揚台の吸着装置^“
を示す図、第13図は第1.4の発明において使用され
ている吸着剤のCO;の吸着率を示す図、第14図はN
H,の吸着率を示す図、第15図は水蒸気の吸着率を示
す図である。
(1)・・・栽培温室、(2)・・・温室内高温空気用
ビット、(3)・・・温室内高温空気用ファン、(3す
・・・蓄熱兼水分吸収材、(4)・・・土壌、(5)・
・・吸水兼蓄熱材層、(6)・・・多面的吸着層、(7
)・・・温室内高温空気送風パイプ兼用地下温風吸引パ
イプ、σ′)・・・再生熱風送風パイプ、(81、(1
1・・・地下熱脇側パイプ、(9)・・・吹出兼吸引パ
イプJOυ・・・再生用バーナー、u渇・・・吸着用プ
ロア、(1漕・・・高負荷燃焼炉付高圧バーナー、04
)・・・燃焼空気兼再生用プロア、(1つ・・・再生用
空気吸込パルプ、(陶、G7)・・・吸込空気バルブ、
rlm・・・再生熱風廃棄バルブ、(II・・・地下蓄
熱用再生熱風給気パルプ、(^ト・・再生熱風CO,供
給バルブ、(21)、C22)・・クーリングタワー、
(23)・・・冷却・、加湿機、 (241・・・冷却
機、(25)、(26)・・・ポンプ、(27)・円筒
型燃焼室、(m・・外筐、■)・・内張り部、G30)
・・・絞り部、 (31)・・・案内翼、G2)・空気
入口、G3)・・・バーナーノズル、G44)燃料人[
1、(35) 燃料用空気人口、(36)・・ブpア
ー、(401・・廻転式送風管、(41)・・・モータ
ー、 (42)・・・除湿用送風機、(43)・・・除
湿用空気人口、(44)・・・再生用送風機、 (45
)・・・水冷クーラー、(46)・・・加湿器、(47
)・・・調整空気出口、(48)・・除湿空気用ダンパ
ー、(49)・・・再生空気用夕/パー1乙))・・P
)生捕伝出口。
第1F4
B奇 問
酔 間
月日
第4図
第5図
第6図
第7図
第8図
第12図Figure 1 is a comparison diagram of the relative humidity in the greenhouse regarding the first invention of the underground heat storage type greenhouse heating environment control device of the present invention, Figure 2 is a comparison diagram of CO1# degree in the same prefecture room, Figure 3 Figure 4.5 is a diagram showing the first and second actual examples of the first invention, Figure 6 is Figure 1.4.
A diagram showing a high-pressure lees flame burner with a high-load small combustion furnace used in the invention of @3, Figure @7 is a diagram showing high temperature suppression which is an example of implementation of the invention of @3, and Figure 8 is a high-temperature flame burner for high-temperature air in the same greenhouse. A diagram showing the underground heat storage process, Figures 8.9, 10 and 11 are diagrams showing the embodiment of the second invention, and Figure 12 is an adsorption device using a lifting platform using liquid fuel used in the invention 1.4. ^“
Figure 13 is a diagram showing the CO adsorption rate of the adsorbent used in the invention of Article 1.4, Figure 14 is a diagram showing the adsorption rate of CO;
FIG. 15 is a diagram showing the adsorption rate of H, and FIG. 15 is a diagram showing the adsorption rate of water vapor. (1) Cultivation greenhouse, (2) Bit for high temperature air in the greenhouse, (3) Fan for high temperature air in the greenhouse, (3) Heat storage and moisture absorbing material, (4)・・・Soil, (5)・
・・Water absorption and heat storage material layer, (6) ・・Multilateral adsorption layer, (7
)...Underground hot air suction pipe that doubles as greenhouse high temperature air blowing pipe, σ')...Regenerated hot air blowing pipe, (81, (1
1...Underground heat side pipe, (9)...Blowout and suction pipe JOυ...Regeneration burner, u-drying...Adsorption proa, (1 row...High-pressure burner with high-load combustion furnace ,04
)...Proa for combustion air and regeneration, (1... air suction pulp for regeneration, (ceramic, G7)... suction air valve,
rlm... Regenerated hot air disposal valve, (II... Regenerated hot air supply pulp for underground heat storage, (^t... Regenerated hot air CO, supply valve, (21), C22)... Cooling tower,
(23)... Cooling, Humidifier, (241... Cooler, (25), (26)... Pump, (27) Cylindrical combustion chamber, (m... Outer casing, ■) ...Inner lining, G30)
... Throttle part, (31) ... Guide vane, G2)・Air inlet, G3) ... Burner nozzle, G44) Fuel man [
1, (35) Fuel air population, (36)... blower, (401... rotating air pipe, (41)... motor, (42)... dehumidification blower, (43)... ... Air population for dehumidification, (44) ... Regeneration blower, (45
)... Water cooler, (46)... Humidifier, (47
)...Adjusted air outlet, (48)...Damper for dehumidified air, (49)...Energy for regenerated air/Par 1))...P
) Raw capture exit. 1F4 B odd drunkenness Figure 4 Figure 5 Figure 6 Figure 7 Figure 8 Figure 12
Claims (4)
吸着創生としてアルミナゲル、合成ゼオライト、活性炭
等の単独または混合状態の吸着層に、除湿(吸着)用送
風と、再生(脱着)用熱風を交互に送風して、夜間の温
室内の除湿と、昼間の加湿及びCo、の補給を行うと共
に、除湿、加湿、再生の切換は室内にセットしたヒュミ
ディスタットと吸着剤の能力の減退を指示するサーモス
タットの設定温度で行い、再生のための熱源は昭和55
年特許出願第62953号の高負荷小型燃焼炉付高圧バ
ーナーを使用することを%1Mとする地中熱交換式温室
暖房の環境調整装置。(1) Air for dehumidification (adsorption) and hot air for regeneration (desorption) are applied to an adsorption layer of alumina gel, synthetic zeolite, activated carbon, etc. alone or in a mixed state as an adsorption layer installed on the ground or underground that can be regenerated by heating. In addition to dehumidifying the greenhouse at night and humidifying and replenishing Co during the day, switching between dehumidification, humidification, and regeneration prevents the capacity of the humidistat and adsorbent set indoors from decreasing. The temperature is set on the thermostat as instructed, and the heat source for regeneration is
An environmental control device for underground heat exchange type greenhouse heating using a high pressure burner with a high load small combustion furnace as disclosed in Patent Application No. 62953.
け、パイプの外側に天然産膠質上、沸石等の+mを作9
、またパイプを使用しない場合は塊状の天然産膠質上、
沸石等の層を作り、夜間の湿度の高い空気をこの層中を
循環させると共に、吸水によって起る凝縮熱により地中
の温度を上列させて、蓄熱効果及び熱交換効果を向上さ
せることを特徴とする湛宰の地中蓄熱装置。(2) A large number of holes or outlets are provided in the underground heat storage blower pipe, and +m of natural colloid, zeolite, etc. is made on the outside of the pipe9.
, and if you do not use a pipe, use a block of natural glue,
By creating a layer of zeolite, etc., and circulating the highly humid air at night through this layer, the condensation heat generated by water absorption raises the underground temperature, improving heat storage and heat exchange effects. A unique underground heat storage device.
と同じ吸着層を使用して、湿分及び有害物質をe、着除
去し一1吸着潜熱により温度が十昇した空気を、吸着層
の出口にセットした水冷クーラーで冷却し、空気のエン
タルピーを降下させ、この低洋度低エンタルピーの空気
を温室内にセットした加湿機または細霧発生装置の中を
通過させ、この気化熱により空気を冷却し、温室内の温
度及び温度を栽培上ベストの環境にコントロールするこ
とを特徴とする温室の環境調整装置。(3) As a method of suppressing high temperatures in a greenhouse during the day, the same adsorption layer as in item 1 is used to remove moisture and harmful substances, and to remove the air whose temperature has risen by 10 degrees due to the latent heat of adsorption. A water cooler set at the outlet of the adsorption layer cools the air to lower the enthalpy of the air, and this low-ocean, low-enthalpy air is passed through a humidifier or mist generator set in the greenhouse to reduce the heat of vaporization. A greenhouse environment adjustment device characterized by cooling the air and controlling the temperature inside the greenhouse to the best environment for cultivation.
る温室内の空気を循環】+(a過させて栽培上有害なる
物質例えばco、、NH,、ROHO1OH類、ハロゲ
ン系殺菌剤の残留ガス等を吸着除去し、栽培上ベストの
環境を連続して得る装置で、吸着剤の内生には昭和55
年特許顧第62953号の高負荷小型燃焼炉付高圧短炎
バーナーを使用し、CO,発生機を兼用させ、通常日中
に行う吸着剤の加熱再生時に、廃熱の一部を温室内に放
出して、加湿とCO,の補給を行い、大部分の廃熱を地
中へ蓄熱することを特徴とした温室暖房の蓄熱及び環境
調整装置。(4) Circulating the air in the greenhouse for underground heat exchange greenhouse heating using the same adsorption layer as in item 1] + (a) Substances harmful to cultivation such as CO, NH, ROHO1OH, halogen fungicides This is a device that adsorbs and removes residual gas, etc., and continuously provides the best environment for cultivation.
A high-pressure short-flame burner with a high-load small combustion furnace (Patent No. 62953) is used, and it doubles as a CO generator, and a part of the waste heat is transferred into the greenhouse during heating and regeneration of the adsorbent, which normally takes place during the day. A heat storage and environment conditioning device for greenhouse heating, characterized by releasing, humidifying and replenishing CO, and storing most of the waste heat underground.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57102370A JPS58220627A (en) | 1982-06-15 | 1982-06-15 | Environment control apparatus for heating underground heat exchange greenhouse |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57102370A JPS58220627A (en) | 1982-06-15 | 1982-06-15 | Environment control apparatus for heating underground heat exchange greenhouse |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58220627A true JPS58220627A (en) | 1983-12-22 |
Family
ID=14325568
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57102370A Pending JPS58220627A (en) | 1982-06-15 | 1982-06-15 | Environment control apparatus for heating underground heat exchange greenhouse |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58220627A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011179785A (en) * | 2010-03-03 | 2011-09-15 | Fuji Kagaku Kk | Temperature and humidity control device |
JP2019162084A (en) * | 2018-03-20 | 2019-09-26 | 国立大学法人九州大学 | Gas supplying apparatus and plant cultivation system |
KR20200034134A (en) * | 2018-09-21 | 2020-03-31 | 한국에너지기술연구원 | Energy Recovery Ventilator with Active Humidity Control and Method Thereof |
JP2020074758A (en) * | 2018-10-24 | 2020-05-21 | 国立研究開発法人産業技術総合研究所 | Dehumidification system for gardening facilities |
-
1982
- 1982-06-15 JP JP57102370A patent/JPS58220627A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011179785A (en) * | 2010-03-03 | 2011-09-15 | Fuji Kagaku Kk | Temperature and humidity control device |
JP2019162084A (en) * | 2018-03-20 | 2019-09-26 | 国立大学法人九州大学 | Gas supplying apparatus and plant cultivation system |
KR20200034134A (en) * | 2018-09-21 | 2020-03-31 | 한국에너지기술연구원 | Energy Recovery Ventilator with Active Humidity Control and Method Thereof |
JP2020074758A (en) * | 2018-10-24 | 2020-05-21 | 国立研究開発法人産業技術総合研究所 | Dehumidification system for gardening facilities |
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