201101993 六、發明說明： 【發明所屬之技術領域】 本申請案，係主張2009年7曰】Λ τ’月10日於日本申诗夕口 本專利申請號2009- 163486之利M ° 〜益’弓丨用該申請荦内交 而適當併入於此說明書中。 肖系二円今 本發明係關於用於農作物之溫室 王秋增溫室用換齑护 置及溫室用空調系統。 至用換軋裝 【先前技術】 以往，已知在乙稀製溫室或塑膠製溫室等栽培蔬菜或 ::之溫室栽培。X ’近來在不受天候或氣溫變化影響之 %境下栽培植物之「植物工廠」t到矚目。植物工廠，係 -種為了創造出適於培育植物之環境，而較以往之溫室栽 培更嚴格管理室溫或照度之方法。 當如上所述在封閉之空間栽培植物，即會隨著植物進 仃光口作用使溫至内之二氧化碳濃度降低。因此須對溫室 内供應二氧化碳，以進行換氣。 S知之皿至中，例如已知有專利文獻丨所記載，開放 溫室之—部分錢行換氣之方法。此方法，會使導致疾病 或發霉之有害動植物進入溫室内。 專利文獻2 ’係揭示了一種可防止有害動植物侵入溫室 内同時進行換氣之換氣系統。 [專利文獻] [專利文獻1]日本特開2004— 350506號公報 201101993 [專利文獻2]日本特開2〇〇8— 2839〇8號公報 I發明内容】 [發明所欲解決之問題] 專利文獻2所記載之換氣系統，由於使用網眼尺寸為 0.1mm之外部氣體過渡器，因此雖能防止較〇 ι_大之有 害動植物之侵入，但無法防止數 i数/z m〜數十v m之微細 1.» — 士 7S7s 或病毒之侵入。 又，專利文獻2所記載之換氣系統，藉由換氣並無法 防止溫室内之環境受破壞。培育植物之_重要因素為濕 度。例如，當減變高，即會成為灰黴病等之原因，當濕 度變低，則會成為白粉病等之原因。因此，保持適當範圍 之濕度，與保持氣溫同樣重要。然而，專利文獻2中，完 全沒有考量到溫室内之濕度。 此外，專利文獻2中，記載有當外部氣體溫度較高時， 藉由增濕降低溫室内之溫度之方法1而，此發明係著重 於溫室内之溫度者，並未考量到濕度。曰本的氣候中，外 部氣體溫度升高之夏季其濕度雖亦增高，但專利文獻2中， 由=係在氣溫高之情形下提高濕度’因此會導致濕度更加 增高，而產生如上述之灰黴病等之問題。 因此，本發明係提供一種考量到溫室内之空氣環境而 能適當進行換氣之新溫室用換氣裝置及溫室用空調系統。 [解決問題之技術手段] 本發明之溫室用換氣裝置，其具備：風扇，用以從溫 6 201101993 室外部將空氣送入至溫室内；填充材，設於從溫室外部流 至溫室内之空氣之通路；吸濕性液體供應部，對前述填充 材供應亦具有殺菌效果之吸濕性液體；液槽，用以收容通 過前述填充材之前述吸濕性液體；以及再生機，用以使在 前述填充材與空氣氣液接觸而濃度變化之吸濕性液體再 生0 如上述，藉由在設於空氣之通路之填充材中，使自外 部榻取之空氣與具有殺菌效果之吸濕性液體氣液接觸，而 能將已進行殺菌及調濕之空氣供應至溫室内，因此能在保 持溫室内之環境之同時進行換氣。亦可使用殺菌力高之氣 化锂作為吸濕性液體。 本發明之溫室用換氣裝置中’前述填充材亦可設置成 阻塞空氣之通路。 藉由此構成’由於導入溫室内之空氣必定通過填充 材’而與吸濕性液體氣液接觸，因此能確實地將之淨化。 本發明之溫室用換氣裝置，亦可具備測定前述溫室内 之一氧化碳濃度之感測器；且換氣 供礼之進仃係使前述二氧化 石反淚度成為既定閾值以上。 2此構成，能藉由換氣將溫室内之二氧化碳濃度維 持於適當之值，促進植物之培育。 本發明之溫室用換氣裝置， 七从 ^ 亦可於溫室外部至前述填 充材之空氣之通路上具備防細過據器。 在設置溫室之環境中存在右 ^ 有多數的蟲。藉由本發明之 構成，能防止因蟲之侵入而、一 & ^染吸濕性液體，以謀求吸濕 201101993 性液體之長壽命。 本發明之溫室用換氣裝署★ 充材之空氣之通路上具：:塵置器亦可於溫室外部至前述塌 在設置溫室之環境中 構成’能防止因砂塵污染 之長壽命。 有可能產生砂塵。藉由本發明之 吸濕性液體’以謀求吸濕性液體 本發明之溫室用換痛奘番 興軋裝置，其亦可為，前述再生機旦 備：筐體，具有擷取空氣# 生機具 礼之擷取口與排出空氣之排氣口. 吸濕性液體供應部，係供廄姓 ’ 你供應待再生之吸濕性液體；填充 為使從前述吸濕性液體供應部供應之吸濕性液體盘空氣氣 液接觸而使吸濕性液體暫時滯㈣；以及於前述掏取口至 前述填充材之空氣之通路上與前述填充材至前述排氣口之 空氣之通路上具備防蟲用過濾器。 在設置溫室之環境中存在有多數的蟲。藉由在填充材 至擷取口側具備防蟲用過濾器，能防止因蟲之侵入而污染 吸濕性液體，以謀求吸濕性液體之長壽命。又，藉由在排 氣口側亦設置防蟲用過濾器，而可在再生機之運轉停止時 亦防止蟲之侵入。 本發明之溫室用空調系統，具備：上述溫室用換氣裝 置；以及設置於前述溫室内之内部氣體燃燒式之加熱裝置。 由於藉由溫室用換氣裝置將空氣擷取至溫室内，因此 能藉由能量效率良好之内部氣體燃燒式之加熱裝置，提升 溫室内之溫度。 本發明之溫室用空調系統，具備：上述溫室用換氣裝 8 201101993 置；以及設置於前述溫室内之利用地下水或自來水之冷卻 裝置。 由於藉由皿至用換氣裝置調整溫室内之濕度，因此不 需要冋冷卻食b力，gp能實現使用地下水或自來水之成本低 之冷卻。 [發明之效果] 本發明’藉由具有殺菌效果之吸濕性液體處理自外部 棟取之空氣’而能在保持溫室内之環境之同時進行換氣。 【實施方式】 以下’參照圖式說明本發明之實施形態之溫室用空調 系統70。圖1係顯示溫室用空調系統7〇之整體構成之圖。 適用至用空調系統之溫室Η，例如係乙烯製溫201101993 VI. Description of the invention: [Technical field to which the invention pertains] This application claims that in 2009, 7 曰 Λ τ ' on the 10th of the 10th in Japan, the application of the patent application number 2009- 163486, M ° ~ benefits ' The bow is properly incorporated into this specification by this application. Xiao Department II This invention relates to a greenhouse for crops. Wang Qiu Zeng has a greenhouse protection system and a greenhouse air conditioning system. For the purpose of re-rolling, the prior art is known to be cultivated in a greenhouse such as an ethylene greenhouse or a plastic greenhouse or a greenhouse of ::. X ’ recently “plant factory” that cultivates plants without being affected by weather or temperature changes. Plant factories are methods that are more stringent in managing room temperature or illuminance than in previous greenhouse cultivation in order to create an environment suitable for cultivating plants. When the plants are cultivated in a closed space as described above, the concentration of carbon dioxide in the warmth is lowered as the plants are exposed to the light. Therefore, carbon dioxide must be supplied to the greenhouse for ventilation. S knows that the dish is in the middle, for example, it is known that there is a method of opening a greenhouse - part of the money to ventilate. This method can cause harmful plants and animals that cause disease or mold to enter the greenhouse. Patent Document 2' discloses a ventilation system that prevents harmful plants and animals from entering the greenhouse while performing ventilation. [Patent Document 1] Japanese Laid-Open Patent Publication No. 2004-350506 No. 201101993 [Patent Document 2] Japanese Patent Laid-Open Publication No. Hei. No. Hei. No. 8-2839 No. 8 SUMMARY OF INVENTION [Problems to be Solved by the Invention] Patent Literature In the ventilation system described in 2, since the external gas transition device having a mesh size of 0.1 mm is used, it is possible to prevent the intrusion of harmful plants and animals larger than 〇ι_, but it is not possible to prevent the number i/zm to tens of volts. Micro 1.» — Invasion of the 7S7s or virus. Further, the ventilation system described in Patent Document 2 cannot prevent the environment in the greenhouse from being damaged by ventilation. The important factor in cultivating plants is humidity. For example, when the reduction is high, it causes gray mold and the like, and when the humidity is low, it becomes a cause of powdery mildew and the like. Therefore, maintaining the proper range of humidity is as important as maintaining temperature. However, in Patent Document 2, the humidity in the greenhouse is not considered at all. Further, Patent Document 2 describes a method 1 for lowering the temperature in a greenhouse by humidification when the temperature of the outside air is high. This invention focuses on the temperature in the greenhouse, and does not consider humidity. In the climate of Sakamoto, the humidity in the summer when the temperature of the outside air rises is also increased. However, in Patent Document 2, the humidity is increased by the temperature in the case of high temperature, so that the humidity is further increased, and the ash as described above is generated. Problems such as mildew. Accordingly, the present invention provides a new greenhouse ventilating device and a greenhouse air conditioning system which can appropriately perform ventilation in consideration of an air environment in a greenhouse. [Technical means for solving the problem] The ventilation device for a greenhouse according to the present invention includes: a fan for feeding air into the greenhouse from the outdoor portion of the temperature 6 201101993; and a filler material disposed outside the greenhouse to the greenhouse a passage for air; a hygroscopic liquid supply portion, a hygroscopic liquid having a sterilizing effect on the filler; a liquid tank for accommodating the hygroscopic liquid passing through the filler; and a regenerator for The hygroscopic liquid is regenerated in contact with the air gas and liquid in contact with the air. As described above, the air taken from the outside and the hygroscopicity with the sterilizing effect are made in the filler provided in the passage of the air. The liquid gas-liquid contact can supply the air that has been sterilized and conditioned to the greenhouse, so that the air can be ventilated while maintaining the environment in the greenhouse. It is also possible to use a vaporized lithium having a high sterilizing power as a hygroscopic liquid. In the greenhouse ventilating device of the present invention, the aforementioned filler may be provided as a passage for blocking air. According to this configuration, since the air introduced into the greenhouse must pass through the filler, it is in contact with the hygroscopic liquid, so that it can be reliably purified. The greenhouse ventilating device of the present invention may further comprise a sensor for measuring a concentration of carbon monoxide in the greenhouse; and the ventilating device is such that the diathratic tearing degree is equal to or higher than a predetermined threshold. 2 This composition can promote the cultivation of plants by maintaining the carbon dioxide concentration in the greenhouse at an appropriate value by ventilation. In the greenhouse ventilating device of the present invention, the anti-fine filter can be provided on the passage of the outside of the greenhouse to the air of the filler. There is a right majority of insects in the environment where the greenhouse is set up. According to the constitution of the present invention, it is possible to prevent the inhalation of insects, and to absorb the hygroscopic liquid in order to obtain a long life of the hygroscopic 201101993 liquid. The greenhouse ventilation device of the present invention has the following steps: The dust trap can also be constructed outside the greenhouse to the aforementioned environment in which the greenhouse is disposed to prevent the long life from being contaminated by sand dust. It is possible to generate sand dust. The moisture absorbing liquid of the present invention is used for the hygroscopic liquid of the present invention, and the regenerative machine can be used for the above-mentioned regenerative machine: the casing has the air intake. The mouthpiece and the exhaust port for discharging air. The hygroscopic liquid supply unit is for the surname of 'they are supplied with the hygroscopic liquid to be regenerated; and is filled for the hygroscopicity supplied from the aforementioned hygroscopic liquid supply part. The liquid tray is in gas-liquid contact to temporarily stagnate the hygroscopic liquid (4); and the insect-repellent filter is provided on the passage of the air inlet to the air of the filler and the air passage of the filler to the exhaust port. Device. There are many insects in the environment where the greenhouse is set up. By providing an insect-repellent filter on the side of the filler to the suction port, it is possible to prevent contamination of the hygroscopic liquid by the intrusion of insects, thereby achieving a long life of the hygroscopic liquid. Further, by providing an insect-proof filter on the side of the exhaust port, it is possible to prevent the intrusion of insects when the operation of the regenerator is stopped. An air conditioning system for a greenhouse according to the present invention includes: the ventilation device for a greenhouse; and an internal gas combustion type heating device provided in the greenhouse. Since the air is pumped into the greenhouse by the greenhouse ventilator, the temperature in the temperature chamber can be raised by the energy efficient internal gas combustion type heating device. The greenhouse air-conditioning system of the present invention comprises: the above-mentioned greenhouse ventilator 8 201101993; and a cooling device using groundwater or tap water provided in the greenhouse. Since the humidity in the greenhouse is adjusted by the dish to the ventilator, it is not necessary to cool the b-force, and the gp can achieve low cost of cooling using ground water or tap water. [Effects of the Invention] In the present invention, the air taken from the outside is treated by the hygroscopic liquid having a sterilizing effect, and the air can be ventilated while maintaining the environment in the greenhouse. [Embodiment] Hereinafter, a greenhouse air-conditioning system 70 according to an embodiment of the present invention will be described with reference to the drawings. Fig. 1 is a view showing the overall configuration of a greenhouse air conditioning system. Suitable for use in greenhouses with air conditioning systems, such as ethylene temperature
至塑膠製溫室，提供用以培育植物Ρ之環境。於溫室H 内設有栽培用之照明71。藉由熱電複合發電機72所發出之 電力供應至栽於用$日 戰枵用之照明71。此外，本說明書中，雖將空 調系統之設置對象稱為「溫室」，但本發明之溫室用空調 系統70亦可適用於被稱為「植物工廠」之設施。 -至用空調系統70具有用以將外部之空氣擷取至溫室 H内之酿至換氣裝置（以下稱為「換氣裝置」）丨。溫室Η内 :空氣從未圖示之排氣口排出。排氣口僅在藉由換氣裝置丨 氣之操取時開放’在換氣裝置1未作動時則關閉。 Hi小，藉由換氣裝置丨對空氣之供應心，形成從 内在溫…之氣流。藉此能防止來自排氣口之微 9 201101993 細生物等之侵入。此外，為了防止較大之蟲之侵入，最好 係於排氣口設置防蟲用過濾器。 換氣裝置1係調整從外部擷取 化後供應至溫室η内4㈣… 之，愚度並加以淨 孤至HR。在熱電複合發電機72產生之廢埶供 應至換氣裝置i。溫室用办哨备铋川砬山 …供 電機72… 由利用熱電複合發 電機之廢熱，課求能量利用效率之提升。 風器 空調系統7〇係於溫室H内具有内部氣體燃燒溫 —、“Ρ用送風機74。内部氣體燃燒溫風器η係燃 燒’皿至Η内之氧以生成溫風之裝置。内部氣體燃燒溫風器 73亦具有作為碳酸氣體施用器之功能。在溫室Η内之二氧 化碳濃度降低時，可藉由内部氣體燃燒溫風器73施用二氧 化碳。 一孔 冷卻用送風機74，係藉由地下水或自 而生^風。本實施形態中，由於歸藉由換氣裝;;擷 取工乳時調整其濕度（潛熱），因此即使無法藉由冷卻使室溫 關降低至某程度，亦能使溫室Η内之熱能降低。因此， 藉由利用地下水哎自夾氽+ 4站、人Α 八次目采水之和緩冷部，能創造出適於培育 植物Ρ之環境。 圖2係顯示溫室用空調系統7〇所使用之換氣裝置i之 詳細構成之圖。換氣裝i 1具有處理從溫室Η外部榻取之 空氣並導入溫室Η内之處理機10。處理機10藉由使擷取之 空氣與吸濕性液體L氣液接觸，來調整濕度。本實施形態 中，係使用氣化鋰（LiCl)作為吸濕性液體 圖3A係顯示氣化鋰之粉塵除去率之圖，圖3b係顯示 10 201101993 氣化鐘之殺菌力之圖。如 ^ ^ ^ < 圖3A所不，氣化鋰能大致100% 地除去粒徑5以m以上之#庙 π ^ 々塵。，圖3Β係顯示滅除供測 成菌種所需之時間與燶声 又之圖。例如，在大腸菌之情形， 藉由暴露於20%以上之澧疮，备儿〜 又之氯化經1 〇分鐘以上即可滅 菌。本實施形態之換氣F罟 孔裝置1，由於係使用27〜30%程度之 濃度之氣化鋰’因此可發揮高殺菌效果。 ,如上述，氯化鐘具有高粉塵除去作用、殺菌力，因此 卜P掏取之工氣’藉由與氯化鐘氣液接觸而被淨化。此 Φ為吸濕H液體L並不限於氣化經，亦可使用食鹽水 專具f潮解性之鹽之溶液、或甘油、乙二醇、丙二醇等吸 ·、、i·生回之夕70醇、或其他具有吸濕性、殺菌力、粉塵除去 力之廉價液體。 換氣裝置1具有再生機4G，其可進行用於處理機1〇之 處理之吸/,#、性液體L之再生。此處，所謂吸濕性液體L之 再生’係指藉由進行調濕使濃度已變化之吸濕性液體l回 復成調濕處理前之狀態。例如，除濕處理，係藉由冷卻溶 '農度咼之及濕性液體L，並使空氣通過經冷卻之吸濕性液 體L，而藉由吸濕性液體L吸收空氣中之水分。藉由此處 雖及濕丨生液體L之溶液濃度會變低，但溶液濃度低之 吸濕性液體L無法進行充分之除濕。藉由從溶液濃度變低 之吸濕性液體L使水分脫離之再生處理，而回復成溶液濃 度高之吸濕性液體L。在增濕處理之情形，相反地，由於吸 濕1±液體L之溶液濃度變高，因此藉由使吸濕性液體Ε吸 收水分之再生處理，而回復成溶液濃度低之吸濕性液體L。 201101993 圖2中，雖顯示對一台虛 處理機10連接一台再生機40 之例，但例如於複數個溫室讯 V, 刀別a又有處理機10時，亦可 係對複數台處理機10連接一台再生機仂之構成。 處理機1〇與再生機4〇係藉由第1吸濕液管路61及第 2吸濕液管路62連接。第1吸濕液管路61係用以從處理機 1 0在再生機40運送吸渴性液體τ _ , 「欣體L之管路，第2吸濕液管路 62係用以從再生機4〇往處理機】Λ、笛、¥ 蜒機10運送吸濕性液體L·之管 路。藉由使用第1吸濕液管路61、第 弟2及濕液管路62，使 吸濕性液體L在處理機1G與再生機4Q之間循環，而能將 在處理機H)使用之吸濕性液體L在再生機Μ再生，返回 至處理機10。 [處理機] 其次說明處理機1G之構成。處理機1()具備筐體u， 該筐體U收容有用以進行空氣與吸濕性液體l之氣液接觸 之填充材14與對填充材！4滴下吸濕+ 同r及屈性液體L之吸濕液供 應部1 5。從吸濕性液體L滴下之吸温柯你μ 「&及屈性液體L係通過填充 材14而缓慢地流落。因此，吸濕性液辦τ 7热庄及體L暫時滯留於填充 材。於筐體11下部具有用以貯留通過填充材 液體L之液槽16。 14之吸濕性 於筐體11形成有用以擷取空氣之擷取口 12與用以排 出空氣之排氣口 13。於操取口 12安裝右]5大Lrl 女衮有防止砂或塵埃侵入 管體11内之慮塵器18與防止通過渡塵器虫 ° t蟲之侵入之 防蟲用過濾器19。於排氣口 13設有用以將從外部擷取之* 氣送入溫室Η内之風扇17。藉由此風扇17之旋轉，從溫; 12 201101993 Η外部將空氣擷取至筐體11内，通過圖2之箭頭所示路徑 送入溫室Η内。換氣裝置1之換氣量、亦即風扇17之轉數 係藉由控制部66控制。又’於排氣口 13亦安裝有防蟲用 過濾器20。 如圖2所示，填充材14由於設置在空氣所通過之通路 上，因此從擷取口 12擷取之空氣通過填充材14。如前所述， 由於吸濕性液體L滯留於填充材14，因此在吸濕性液體L 與通過填充材14之空氣之間進行水分之收授，而進行除濕 或增濕。又，藉由氣化鋰之粉塵除去作用及殺菌作用使通 過填充材14之空氣被淨化。填充材14如圖2所示設置成 :塞空氣之通路’於筐體η之内面與填充材14間無間隙。 疋以’導入至溫室Η内之空氣確實地通過填充材14。 處理機1〇具有用以將液槽16内之吸濕性液體L供應 至吸濕液供應部15之管21。於管2丨忠 %官21女裝有泵22，用以汲 取液槽16内之吸濕性液體L。 於此管21設有教粟夕笛t虹 為一一 ，、、、戈30之第1熱交換器31，藉由第i ‘、，、交換器3 1加熱或冷卻 控制從處理機10之吸㈣ 第1熱交換器31係To the plastic greenhouse, providing an environment for cultivating plant mites. A lighting 71 for cultivation is provided in the greenhouse H. The power generated by the thermoelectric composite generator 72 is supplied to the illumination 71 used for the $1 war. Further, in the present specification, the object of the air conditioning system is referred to as a "greenhouse", but the greenhouse air conditioning system 70 of the present invention can also be applied to a facility called a "plant factory". The air conditioning system 70 has a brewing device (hereinafter referred to as "ventilating device") for extracting the outside air into the greenhouse H. Inside the greenhouse: Air is discharged from the exhaust port not shown. The exhaust port is only opened when the ventilator is operated by the ventilator, and is turned off when the ventilator 1 is not actuated. Hi is small, through the ventilation device 丨 to the supply of air, forming a flow from the inner temperature. Thereby, it is possible to prevent intrusion of fine creatures and the like from the exhaust port. In addition, in order to prevent intrusion of larger insects, it is preferable to provide a pest control filter at the exhaust port. The ventilator 1 is adjusted to be supplied to the greenhouse η 4 (4) from the outside, and is fooled and netted to HR. The waste generated by the thermoelectric composite generator 72 is supplied to the ventilator i. The greenhouse is used for the whistle and the 砬 砬 ... ... ...... ...... ...... ...... ...... ...... ...... ...... ...... ...... ...... ...... ...... ...... ...... ...... ...... ...... ...... ...... ...... ...... ...... ...... ...... ...... The air conditioner system 7 is equipped with an internal gas combustion temperature in the greenhouse H, "the air blower 74 is used. The internal gas combustion air heater η is a device that burns the oxygen in the bowl to generate a warm air. Internal gas combustion The air heater 73 also functions as a carbon dioxide gas applicator. When the concentration of carbon dioxide in the greenhouse is lowered, carbon dioxide can be applied by the internal gas combustion air heater 73. The one-hole cooling blower 74 is grounded or self-contained. In the present embodiment, since the humidity is adjusted (latent heat) when the working milk is taken, the greenhouse can be adjusted to a certain degree by cooling. The heat energy in the raft is reduced. Therefore, by using the groundwater 哎 氽 氽 + 4 stations, the Α 八 目 目 目 目 缓 缓 , , , , , 能 能 能 能 能 能 能 能 能 能 能 能 能 。 。 。 。 。 。 。 。 。 。 The detailed configuration of the ventilation device i used in the system 7. The ventilation device i 1 has a processor 10 for processing the air taken from the outside of the greenhouse and introduced into the greenhouse. The processor 10 is made to be taken. Air and hygroscopicity In the present embodiment, the vaporized lithium (LiCl) is used as the hygroscopic liquid. Fig. 3A shows the dust removal rate of the vaporized lithium, and Fig. 3b shows the 10 201101993 gasification. The figure of the bactericidal force of the clock. For example, ^ ^ ^ < Figure 3A does not, gasification of lithium can roughly remove 100% of the particle size of 5 m π ^ 々 dust. Figure 3 Β shows the elimination of the test The time required for the bacteria to form and the snoring. For example, in the case of coliforms, by exposure to more than 20% of acne, the preparation of chlorination can be sterilized for more than 1 minute. The ventilating F boring device 1 of the form has a high sterilizing effect because it uses a vaporized lithium of a concentration of 27 to 30%. As described above, the chlorinated clock has a high dust removing effect and a sterilizing power, so The process gas extracted by P is purified by contact with the chlorinated clock gas. This Φ is the moisture absorption. The liquid L is not limited to the vaporization process, and a salt solution of the deliquescent salt of the salt water may be used. Or glycerin, ethylene glycol, propylene glycol, etc., i, raw back 70 alcohol, or other hygroscopicity, bactericidal power The ventilating device 1 has a regenerator 4G which can perform the regeneration of the suction/, #, liquid L for the treatment of the processor 1 . Here, the regeneration of the hygroscopic liquid L ' means that the hygroscopic liquid 1 whose concentration has been changed is returned to the state before the humidity control treatment by performing humidity control. For example, the dehumidification treatment is performed by cooling the 'potency' and the wet liquid L, and The air passes through the cooled hygroscopic liquid L, and the moisture in the air is absorbed by the hygroscopic liquid L. Here, the concentration of the solution of the wet liquid L is lowered, but the solution concentration is low. The liquid L cannot be sufficiently dehumidified, and the moisture is removed from the hygroscopic liquid L having a reduced solution concentration, and the hygroscopic liquid L having a high solution concentration is returned. In the case of the humidification treatment, conversely, since the concentration of the solution of the moisture absorption 1±liquid L becomes high, the hygroscopic liquid L having a low solution concentration is returned by the regeneration treatment of the moisture absorption liquid Ε absorption water. . 201101993 In FIG. 2, although an example is shown in which a regenerator 40 is connected to a virtual processor 10, for example, in a plurality of greenhouses V, when the processor 10 has a processor 10, it can also be used for a plurality of processors. 10 is connected to a regenerator. The processor 1 and the regenerator 4 are connected by a first moisture absorption line 61 and a second moisture absorption line 62. The first moisture absorption liquid line 61 is for transporting the thirsty liquid τ _ from the processor 10 to the regenerator 40, and the second moisture absorption line 62 is used for the regeneration machine. 4 〇 处理 Λ Λ Λ 笛 笛 笛 笛 笛 笛 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送 运送The liquid L is circulated between the processor 1G and the regenerator 4Q, and the hygroscopic liquid L used in the processor H) can be regenerated in the regenerator and returned to the processor 10. [Processor] Next, the processor will be described. The structure of 1G. The processor 1 () is provided with a casing u, and the casing U accommodates a filler 14 for bringing air and liquid in contact with the moisture-absorbing liquid 1 and a moisture absorption + the same for the filler material 4; The moisture-absorbing liquid supply portion of the depressing liquid L is 15. The temperature-absorbing liquid from the hygroscopic liquid L is "sampling" and "the refractive liquid L is slowly flowed through the filler material 14. Therefore, the hygroscopic liquid The τ 7 hot slab and the body L are temporarily retained in the filler. The lower portion of the casing 11 has a liquid tank 16 for storing the liquid L passing through the filler. 14 The hygroscopicity of the casing 11 is useful for taking up the space. The port 12 and the exhaust port 13 for exhausting air are installed. The right port 5 is mounted on the right port. The 5 large Lrl girl has a dust filter 18 for preventing sand or dust from entering the pipe body 11 and preventing the passage of the dust collector. a pest-insulating filter 19 for invading insects. The exhaust port 13 is provided with a fan 17 for feeding the gas extracted from the outside into the greenhouse, whereby the fan 17 is rotated and heated; 12 201101993 The air is taken into the casing 11 and sent to the greenhouse through the path indicated by the arrow in Fig. 2. The amount of ventilation of the ventilator 1, that is, the number of revolutions of the fan 17, is controlled by the control unit 66. Controlling. Further, an insect-proof filter 20 is also installed at the exhaust port 13. As shown in Fig. 2, since the filler 14 is disposed on the passage through which the air passes, the air drawn from the extraction port 12 is filled. As described above, since the hygroscopic liquid L stays in the filler 14, the moisture is absorbed between the hygroscopic liquid L and the air passing through the filler 14 to perform dehumidification or humidification. The air passing through the filler material 14 is purified by the dust removing action and the sterilizing action of the vaporized lithium. 2 is arranged such that the passage of the air passage has no gap between the inner surface of the casing η and the filler 14. The air introduced into the greenhouse is surely passed through the filler 14. The processor 1 has The hygroscopic liquid L in the liquid tank 16 is supplied to the tube 21 of the moisture absorption liquid supply portion 15. The tube 2 has a pump 22 for sucking the hygroscopic liquid L in the liquid tank 16. The tube 21 is provided with a first heat exchanger 31 for teaching the celestial flutes to be one, one, and 30, and is controlled from the processor 10 by the heating or cooling of the i', the exchanger 31. Suction (4) 1st heat exchanger 31
之溫产。H ϋ "，、’供應部I5供應之吸濕性液體L 之皿度。疋加熱或冷卻 將空氣增濕或除满。亦即在卢體L，取決於是藉由處理機 係為了冑口及m P在處理機1〇進行增濕處理時， 保馮了使及濕性液體L 吁 濕性液體L。相反祕 刀放出至空氣_而加熱吸 了使空氣中之水分容^處理機1G進行除濕處理時，係為 性液體L。 地吸收至吸濕性液體L而冷卻吸濕 13 201101993 用以將液槽1 6内之明、、爲吣_ 円之及濕性液體L運送至再 第1吸濕液管路61，#㈣一 A ^ 係經由二向閥23連接於用以從液槽 16汲取吸濕性液體l之營2丨。_ a bb 1 ^ 之僧 —向閥2 3係控制運送至虚 理機10之吸濕液供應部15之 廷至處 及燕性液體L之罝與通過第1 吸濕液管路61運送至真4地4Λ 圮至再生機40之吸濕性液體L之量。太 實施形態中之三向閥23，. i里不 阀23係將（對吸濕液供應部15運送之 吸濕性液體L之量）：軍详5击1她 '再生機40之吸濕性液體L之 量）控制成從8 : 2成為9 : 1之比率。 於第1吸濕液管路6丨雜·古楚+ u 峪61 a又有第2熱交換器32，用以冷卻 或加熱供應至再生機40之吸濕性液體卜第2熱交換器32 係控制供應至再生機40之吸濕性液體L之溫度。第^熱交 換器3!與第2熱交換器32構成熱泵3〇,熱在第！熱：換 器31與第2熱交換器32之間移動。 此處說明熱泵30之構成。熱泵30具備第i熱交換器 3 1、第2熱交換器32、壓縮機33、膨脹閥34、以及連結此 等之冷煤管35。熱泵30藉由使冷煤之流動逆轉，而能：第 1熱交換器31發揮蒸發器或冷凝器之功能。第2熱交換器 32係進行與第1熱交換器3丨相反之處理。 [再生機] 其次說明再生機40。再生機40係使從處_ 1〇送來 之吸濕性液體L與空氣氣液接觸，而再生吸濕性液體l。再 生機40具備筐體41，該筐體4丨係收容用以進行空氣與吸 濕性液體L之氣液接觸之填充材44與對填充材44滴下吸 濕性液體L之吸濕液供應部45。又，於筐體41下部具有用 14 201101993 L之液槽46。 以貯留通過填充材44之吸濕性液體 吸濕液供應部45具有用以將通過第1吸濕液管路61 送來之吸濕性液體L供應至填充材44之吸濕液供應部仏 與將從液槽46沒取之吸濕性液體L供應至填充材44之吸 濕液供應部45b »設於第1吸濕液管路6丨之熱泵3〇之第2 熱交換器32是加熱或冷卻吸濕性液體L，取決於再生機 是將吸濕性液體L濃縮或稀釋。亦即，在再生機4g進行吸 濕性液體L之濃縮時’係為了使吸濕性液體L所含之水分 放出至空氣中而加熱吸濕性液體L。相反地，在再生機4〇 稀釋吸濕性液體L時，係為了使空氣中之水分容易地吸收 至吸濕性液體L而冷卻吸濕性液體l。 於筐體41形成有用以擷取空氣之擷取口 42與用以排 =空氣之排氣口 43。於擷取口 42安裝有防止砂或塵埃侵入 筐體41内之濾塵器56與防止通過濾塵器56之蟲之侵入之 防蟲用過渡器5 7 〇 於排氣口 43設有用以從筐體41内排出空氣之風扇 7藉由此風扇47之旋轉，筐體41内之空氣排出至外部， 而筐體41内相對筐體41外部成為負壓，因此空氣係通過 擷取口 42流入筐體41内。又，於排氣口 43亦安裝有防蟲 用過濾器5 8。藉此，在風扇47停止時，亦可防止蟲從排氣 口 43侵入筐體41内。 圖2中’箭頭係顯示空氣之流動。如圖2所示，從擷 取口 42棟取之空氣係通過填充材44。由於吸濕性液體[滯 留於填充材44，因此係在吸濕性液體l與空氣之間進行水 15 201101993 分之收授。藉此再生吸濕性液體L。 再生機40具有用以將液槽46内之吸濕性液體l供應 至第1吸濕液管路61之管49。液槽46内之吸濕性液體l 藉由泵5 0被汲取至第1吸濕液管路6卜吸濕性液體L通過 第2熱交換器32再度供應至再生機4〇。 再生機40具有用以將液槽46之吸濕性液體l供應至 吸濕液供應部45b之供應管5卜於供應管51安裝有泵52， 用以汲取液槽46内之吸濕性液體l。又，於該管5丨設有加 熱源53。此加熱源係利用熱電複合發電機72之廢熱加熱流 動於管5 1之吸濕性液體l。 加熱源53’除了第2熱交換器32之溫度控制外，欲使 溫度上升時，係加熱從液槽46汲取之吸濕性液體L。經加 熱之吸濕性液體L從吸濕液供應部45b滴下至填充材44， 而在填充材44氣液接觸。通過填充材44之吸濕性液體l 進入液槽46。如上述地使吸濕性液體L循環，再生機4〇即 進行吸濕性液體L之再生處理。 再生機具有對液槽46進行供水之供水管54。於供 水f 54上設有閥55，藉由閥55進行供水之控制。 液槽46之吸濕性液體L係通過第2吸濕液管路“返 回至處理機10^從再生機4〇返回至處理機1〇之吸濕性液 體L之量藉由閥63被調整。本實施形態中之閥63係將返 回至處理機ίο之吸濕性液體L之量控制成液槽46内之吸 濕性液體L之液面高度成為一定。 換氣裝I 1具有在第i吸濕液管路61與第2吸濕液管 16 201101993 路62之間進行熱交換之熱交換器64。此熱交換器64係減 低"il動於第1吸濕液管路61之吸濕性液體l與流動於第2 吸濕液管路62之吸濕性液體L之溫度差，有助於熱泵30 之汲取溫度差之減低。以上，詳細說明了換氣裝置1之構 成。 [溫室用空調系統之動作] 其次’說明本實施形態之溫室用空調系統7〇之動作。 溫室用空調系統70係藉由測定二氧化碳濃度之感測器65 測定溫室Η内之二氧化碳濃度。換氣裝置1係藉由控制部 66將換氣量調整成溫室Η内之二氧化碳濃度保持既定之閾 值。例如，在二氧化碳濃度低於既定之閾值之情形下開始 換氣，進行換氣直至與外部之二氧化碳濃度相等為止。又， (1)在植物不進行光合作用之夜間，（2)在多數個作業人員位 於溫室内時，（3)在使内部氣體燃燒溫風器73作動時等，溫 室Η内之二氧化碳濃度變大時，於二氧化碳濃度高於既定 之閾值之情形下開始換氣，進行換氣直至與外部之二氧化 碳濃度相等為止。 首先，說明外部氣體之濕度較溫室Η内高時之換氣動 作。此情形下，換氣裝置丨係先將外部氣體除濕至與溫室Η 内之濕度相同程度為止後，供應至溫室Η内。 換氣裝f 1係使熱泵30之第1熱交換器3】發揮蒸發 器之功能’使第2熱交換器32發揮冷凝器之功能。於處理 機10之液槽16先收容溶液濃度高之吸濕性液體乙。 處理機H)係從液槽16沒取溶液漠度高之吸濕性液體 17 201101993 L ’並以發揮蒸發器功能之第1熱交換器3 1將吸濕性液體l 冷卻後供應至吸濕液供應部1 5。吸濕液供應部1 5係將吸濕 性液體L低下至填充材14❶被滴下之吸濕性液體l和緩地 通過填充材14返回至液槽16。 處理機10藉由與上述動作同時地使設於排氣口 13之 風扇17旋轉’將空氣擷取至篋體n内，並以填充材14進 行空氣與吸濕性液體L之氣液接觸後，將處理後之空氣通 過排氣口 13供應至溫室η内。由於在填充材14存在有溶 液濃度咼且低溫之吸濕性液體L，因此空氣中之水分藉由吸 濕性液體L而被吸收’經除濕之空氣被供應至溫室η内。 此外’由於在吸濕性液體L與空氣之間亦同時進行熱交換， 因此空氣係被冷卻。 在處理機1 0持續進行除濕動作後，吸濕性液體L被稀 釋，而變得難以吸收空氣中之水分’導致除濕效率降低， 因此藉由再生機40使吸濕性液體L再生。換氣裝置1係將 處理機10之從液槽16吸出之吸濕性液體l中之一部分供 應至第1吸濕液管路61，並運送至再生機4〇 ^運送至再生 機40之吸漁性液體l之量藉由三向閥23受到調節。 於第1吸濕液管路61之途中配設有發揮冷凝器功能之 第2熱交換器32 ’運送至再生機40之吸濕性液體l係藉由 第2熱交換器32而被加熱。再生機40進行從第丨吸濕液 管路61供應之溶液濃度變低之吸濕性液體[之再生處理。 具體而言，吸濕液供應部45a，係將經第2熱交換器32加 熱之及/愚性液體L滴下至填充材44。被滴下之吸濕性液體 18 201101993 L通過填充材44而進入液槽46。 再生機40在與上述動作同時地藉由設於排出口 43之 風扇47從筐體41内排出空氣。藉此，空氣係通過操取口 42流入筐體41内。流入之空氣在填充材44與吸濕性液體 L氣液接觸後，從排出口 43排出。藉由空氣與吸濕性液體 L接觸，水分從高溫之吸濕性液體L脫離而釋放至空氣中， 使吸濕性液體L之濃度變高。通過填充材44之吸濕性液體 L進入液槽46。 液槽46内之吸濕性液體L之一部分藉由泵52被汲取， 通過供應管5 1供應至吸濕液供應部45b。此時，加熱源53 係加熱吸濕性液體L。藉此，成為吸濕性液體L之水分更加 谷易被放出之狀態，再生機4〇能進行良好效率之濃縮處理。 又，液槽46内之吸濕性液體L之一部分供應至第丨吸 =’、液g路61。被供應至第1吸濕液管路61之吸濕性液體l 係被第2熱交換器32加熱而再度被供應至吸濕液供應部 如上述，藉由吸濕性液體L在填充材44與液槽之 間循環，使吸濕性液體L之濃度徐徐地變高。Warm production. H ϋ ",, 'The degree of hygroscopic liquid L supplied by the supply unit I5.疋 Heating or cooling to humidify or deplete the air. That is, in the L-shaped body L, the moisturizing liquid L is moistened with the wet liquid L by the treatment machine for humidifying the treatment machine 1 for the mouthwash and m P . On the other hand, when the secret knife is released to the air _ while the heat is absorbed and the moisture in the air is processed by the processor 1G for dehumidification treatment, it is a liquid L. Absorbed to the hygroscopic liquid L and cooled to absorb moisture 13 201101993 for transporting the liquid tank 16 and the wet liquid L to the first moisture absorption liquid line 61, #(4) An A ^ is connected to the battalion 2 for drawing the hygroscopic liquid 1 from the liquid tank 16 via the two-way valve 23. _ a bb 1 ^ 向 向 向 向 向 向 向 向 向 向 向 向 向 向 向 向 向 向 向 向 向 向 向 向 向 向 向 向 向 向 向 向 向 向 向 僧 僧 僧 僧 僧 僧 僧 僧 僧 僧 僧 僧 僧The amount of the hygroscopic liquid L of the regenerative machine 40. In the three-way valve 23 of the embodiment, the valve 23 is not the valve (the amount of the hygroscopic liquid L transported to the moisture absorption liquid supply unit 15): the military 5 hits 1 her 'regeneration machine 40 moisture absorption The amount of the liquid L is controlled to be a ratio of 9:1 to 9:1. In the first moisture absorption liquid line 6 丨 · Gu Chu + u 峪 61 a, there is a second heat exchanger 32 for cooling or heating the hygroscopic liquid supplied to the regenerator 40, the second heat exchanger 32 The temperature of the hygroscopic liquid L supplied to the regenerator 40 is controlled. The first heat exchanger 3! and the second heat exchanger 32 constitute a heat pump 3, and the heat is in the first! Heat: The converter 31 moves between the second heat exchanger 32. The configuration of the heat pump 30 will be described here. The heat pump 30 includes an i-th heat exchanger 3 1 , a second heat exchanger 32 , a compressor 33 , an expansion valve 34 , and a cold coal pipe 35 connected thereto. The heat pump 30 can reverse the flow of the cold coal, so that the first heat exchanger 31 functions as an evaporator or a condenser. The second heat exchanger 32 performs a process opposite to that of the first heat exchanger 3丨. [Recycling Machine] Next, the reproducing machine 40 will be described. The regenerative machine 40 regenerates the hygroscopic liquid 1 by bringing the hygroscopic liquid L sent from the _ 1 接触 into contact with the air gas and liquid. The regenerator 40 includes a casing 41 that houses a filler 44 for bringing air and liquid contact between the air and the hygroscopic liquid L, and a moisture supply portion for dropping the hygroscopic liquid L to the filler 44. 45. Further, a liquid tank 46 of 14 201101993 L is provided at the lower portion of the casing 41. The hygroscopic liquid moisture absorbing liquid supply portion 45 that has been stored and passed through the filler 44 has a moisture absorbing liquid supply portion for supplying the hygroscopic liquid L sent through the first moisture absorbing liquid line 61 to the filler 44. The moisture absorption liquid supply unit 45b that supplies the hygroscopic liquid L that is not taken from the liquid tank 46 to the filler 44 is disposed in the second heat exchanger 32 of the heat pump 3 that is disposed in the first moisture absorption line 6 The hygroscopic liquid L is heated or cooled, and the hygroscopic liquid L is concentrated or diluted depending on the regenerator. In other words, when the regenerator 4g concentrates the hygroscopic liquid L, the hygroscopic liquid L is heated in order to release the moisture contained in the hygroscopic liquid L into the air. On the other hand, when the regenerative machine 4 稀释 dilutes the hygroscopic liquid L, the hygroscopic liquid 1 is cooled in order to easily absorb the moisture in the air to the hygroscopic liquid L. The casing 41 is formed with a suction port 42 for drawing air and an exhaust port 43 for discharging air. A dust filter 56 for preventing sand or dust from entering the casing 41 and an insect-proof transition device for preventing intrusion of the insects passing through the dust filter 56 are attached to the extraction port 42. The exhaust port 43 is provided for the slave housing 43. The fan 7 that discharges air in the air 41 is rotated by the fan 47, and the air in the casing 41 is discharged to the outside, and the inside of the casing 41 becomes a negative pressure with respect to the outside of the casing 41, so that the air flows into the casing through the dip port 42. 41 inside. Further, an insect-proof filter 58 is attached to the exhaust port 43. Thereby, when the fan 47 is stopped, it is possible to prevent the insect from entering the casing 41 from the exhaust port 43. The arrow in Figure 2 shows the flow of air. As shown in Fig. 2, the air taken from the sluice port 42 passes through the filler 44. Since the hygroscopic liquid [stayed in the filler 44, it is subjected to water 15 201101993 between the hygroscopic liquid 1 and the air. Thereby, the hygroscopic liquid L is regenerated. The regenerator 40 has a tube 49 for supplying the hygroscopic liquid 1 in the liquid tank 46 to the first moisture absorption line 61. The hygroscopic liquid 1 in the liquid tank 46 is pumped to the first moisture absorption liquid line 6 by the pump 50, and the hygroscopic liquid L is again supplied to the regenerator 4 through the second heat exchanger 32. The regenerator 40 has a supply pipe 5 for supplying the hygroscopic liquid 1 of the liquid tank 46 to the moisture absorption liquid supply portion 45b. The supply pipe 51 is provided with a pump 52 for sucking the hygroscopic liquid in the liquid tank 46. l. Further, a heating source 53 is provided in the tube 5''. This heating source heats the hygroscopic liquid 1 flowing through the tube 51 by the waste heat of the thermoelectric composite generator 72. In addition to the temperature control of the second heat exchanger 32, the heating source 53' heats the hygroscopic liquid L drawn from the liquid tank 46 when the temperature is raised. The heated hygroscopic liquid L is dropped from the moisture-absorbing liquid supply portion 45b to the filler 44, and is brought into contact with the filler 44 in a gas-liquid state. The liquid phase 46 is introduced through the hygroscopic liquid l of the filler material 44. The hygroscopic liquid L is circulated as described above, and the regenerating machine 4 performs the regeneration treatment of the hygroscopic liquid L. The regenerator has a water supply pipe 54 that supplies water to the liquid tank 46. A valve 55 is provided on the water supply f 54 to control the water supply by the valve 55. The hygroscopic liquid L of the liquid tank 46 is adjusted by the second moisture absorption liquid line "the amount of the hygroscopic liquid L returned to the processing machine 10 from the regenerator 4 to the processing machine 1" is adjusted by the valve 63. In the valve 63 of the present embodiment, the amount of the hygroscopic liquid L returned to the processor 355 is controlled so that the liquid level of the hygroscopic liquid L in the liquid tank 46 becomes constant. The ventilating device I 1 has a heat exchanger 64 for exchanging heat between the moisture absorption liquid line 61 and the second moisture absorption liquid pipe 16 201101993. The heat exchanger 64 is reduced by "il moving to the first moisture absorption liquid line 61. The temperature difference between the hygroscopic liquid 1 and the hygroscopic liquid L flowing through the second moisture absorption line 62 contributes to a reduction in the temperature difference of the heat pump 30. The configuration of the ventilator 1 will be described in detail. [Operation of Greenhouse Air Conditioning System] Next, the operation of the greenhouse air conditioning system 7 of the present embodiment will be described. The greenhouse air conditioning system 70 measures the carbon dioxide concentration in the greenhouse by the sensor 65 for measuring the carbon dioxide concentration. The device 1 adjusts the amount of ventilation to the concentration of carbon dioxide in the greenhouse by the control unit 66. Threshold value. For example, when the carbon dioxide concentration is lower than a predetermined threshold, ventilation is started, and ventilation is performed until the concentration of carbon dioxide is equal to the outside. Further, (1) at night when the plant does not perform photosynthesis, (2) When a plurality of workers are located in the greenhouse, (3) when the internal gas combustion air heater 73 is actuated, when the concentration of carbon dioxide in the greenhouse is increased, the ventilation is started when the carbon dioxide concentration is higher than a predetermined threshold. Ventilation is performed until the concentration of carbon dioxide is equal to the outside. First, the ventilation of the outside air is higher than that in the greenhouse. In this case, the ventilator first dehumidifies the outside air into the greenhouse. After the humidity is the same, it is supplied to the greenhouse. The ventilation unit f 1 causes the first heat exchanger 3 of the heat pump 30 to function as an evaporator. The second heat exchanger 32 functions as a condenser. The liquid tank 16 of the machine 10 first accommodates the hygroscopic liquid B having a high concentration of the solution. The processor H) does not take the hygroscopic liquid 17 201101993 L ' from the liquid tank 16 and has a high degree of solution inversion. The first heat exchanger 3 1 of the hair dryer function cools the hygroscopic liquid 1 and supplies it to the moisture absorption liquid supply unit 15. The moisture absorption liquid supply unit 15 lowers the hygroscopic liquid L until the filler 14 is dropped. The hygroscopic liquid 1 is gently returned to the liquid tank 16 through the filler 14. The processor 10 simultaneously rotates the fan 17 provided at the exhaust port 13 to extract the air into the body n by the above operation. After the air and liquid of the air and the hygroscopic liquid L are contacted by the filler 14, the treated air is supplied to the greenhouse η through the exhaust port 13. Since the solution 14 has a solution concentration and low temperature moisture absorption The liquid L is so that the moisture in the air is absorbed by the hygroscopic liquid L. The dehumidified air is supplied into the greenhouse η. Further, since the heat exchange is also performed between the hygroscopic liquid L and the air, the air is cooled. After the dehumidifying operation is continued by the processor 10, the hygroscopic liquid L is diluted, and it becomes difficult to absorb the moisture in the air. The dehumidification efficiency is lowered, so that the hygroscopic liquid L is regenerated by the regenerator 40. The ventilating device 1 supplies a part of the hygroscopic liquid 1 sucked from the liquid tank 16 of the processor 10 to the first moisture absorbing liquid line 61, and transports it to the regenerator 4 to be transported to the regenerator 40. The amount of the fishing liquid l is regulated by the three-way valve 23. The hygroscopic liquid 1 transported to the regenerator 40 by the second heat exchanger 32' which functions as a condenser in the middle of the first moisture absorption line 61 is heated by the second heat exchanger 32. The regenerator 40 performs a regeneration process of the hygroscopic liquid whose concentration of the solution supplied from the second moisture absorption liquid line 61 is lowered. Specifically, the moisture absorption liquid supply unit 45a drops the liquid/cool liquid L heated by the second heat exchanger 32 to the filler 44. The dripped hygroscopic liquid 18 201101993 L enters the liquid tank 46 through the filler 44. The regenerator 40 discharges air from the casing 41 by the fan 47 provided at the discharge port 43 simultaneously with the above operation. Thereby, the air flows into the casing 41 through the operation port 42. The inflowing air is discharged from the discharge port 43 after the filler 44 comes into contact with the moisture-absorbing liquid L. By the contact of the air with the hygroscopic liquid L, the moisture is released from the high-temperature hygroscopic liquid L and released into the air, so that the concentration of the hygroscopic liquid L becomes high. The hygroscopic liquid L passing through the filler 44 enters the liquid tank 46. A portion of the hygroscopic liquid L in the liquid tank 46 is taken up by the pump 52 and supplied to the moisture absorption liquid supply portion 45b through the supply pipe 51. At this time, the heat source 53 heats the hygroscopic liquid L. As a result, the moisture of the hygroscopic liquid L is more easily released, and the regenerator 4 can perform a concentration process with good efficiency. Further, a part of the hygroscopic liquid L in the liquid tank 46 is supplied to the first suction =' and the liquid g path 61. The hygroscopic liquid 1 supplied to the first moisture absorption liquid line 61 is heated by the second heat exchanger 32 and supplied again to the moisture absorption liquid supply portion as described above, and the hygroscopic liquid L is applied to the filler 44. Circulation with the liquid tank, the concentration of the hygroscopic liquid L is gradually increased.
H内之動作。 、生進仃再生處理之液槽46内之吸濕性液體L·通過第2 。吸濕性液體L在返回至處 藉由熱交換器64與流向再生機4〇之吸濕 交換，使溫度降低。以上，說明了使用溫 之換氣裝置1將經除濕之空氣供應至溫室 其次， 說明外部氣體之濕度較 溫室Η内低時之換氣動 19 201101993 作。此情形下，換氣裝置1係先將外部氣體增濕至與溫室H 内之/燕度相同程度為止後，供應至溫室Η内。 在以換氣裝置1使空氣增濕時’熱泵3〇係使第1熱交 換器3 1發揮冷凝器之功能，使第2熱交換器32發揮蒸發 器之功能。於處理機1〇之液槽16先收容溶液濃度低（含多 量水分）之吸濕性液體L。增濕處理之情形，基本上換氣裝 置1係進行與除濕處理相反之動作。 處理機10係將溶液濃度低之吸濕性液體L加熱並滴下 至填充材14，另一方面使擷取之空氣通過填充材14，藉此 從吸濕性液體L放出水分並使空氣增濕◊此外，亦同時在 吸濕性液體L與空氣之間進行熱交換，以加熱空氣。 在處理機10持續進行增濕動作後，由於吸濕性液體L 被濃縮’使放出至空氣中之水分變少，因此藉由再生機4〇 使吸濕性液體L再生。換氣裝置1係將處理機1〇之從液槽 16吸出之吸濕性液體L中之一部分供應至第1吸濕液管路 61 ’並運送至再生機40» 運送至再生機40之吸濕性液體L，藉由位於第1吸濕 液管路61之第2熱交換器3 2被冷卻。經冷卻之吸濕性液 體L供應至再生機40之吸濕液供應部45a。吸濕性供應部 45a將經冷卻之濃度高之吸濕性液體l滴下至填充材44， 另一方面使從外部擷取之空氣通過填充材44，藉此進行使 吸濕性液體L吸收水分之再生處理。通過填充材44之吸濕 性液體L進入液槽46。 液槽46内之吸濕性液體L之一部分藉由泵52被及取， 20 201101993 通過供應管5 1供應至吸濕液供應部45b。又，液槽46内之 吸濕性液體L之-部分供應至第i吸濕液管路61。被供應 至第1吸濕液管路61之吸濕性液體"系被第2熱交換器32 冷卻而再度被供應至吸濕液供應部45a。如上述，藉由吸濕The action inside H. The hygroscopic liquid L· in the liquid tank 46 for the regeneration treatment is passed through the second. The hygroscopic liquid L is returned to the moisture exchange by the heat exchanger 64 and the flow to the regenerator 4 to lower the temperature. In the above, the use of the warm ventilator 1 to supply the dehumidified air to the greenhouse is described. Next, it is indicated that the humidity of the external gas is lower than that in the greenhouse 19 19 201101993. In this case, the ventilator 1 is supplied to the greenhouse after the external air is humidified to the same extent as the swath in the greenhouse H. When the air is humidified by the ventilating device 1, the heat pump 3 causes the first heat exchanger 3 1 to function as a condenser, and the second heat exchanger 32 functions as an evaporator. The liquid tank 16 in the processor 1 first contains the hygroscopic liquid L having a low solution concentration (including a large amount of moisture). In the case of the humidification treatment, basically, the ventilation device 1 performs an operation opposite to the dehumidification treatment. The processor 10 heats and drops the hygroscopic liquid L having a low solution concentration to the filler 14 and, on the other hand, passes the extracted air through the filler 14, thereby releasing moisture from the hygroscopic liquid L and humidifying the air. In addition, heat exchange is also performed between the hygroscopic liquid L and the air to heat the air. After the processor 10 continues the humidification operation, since the hygroscopic liquid L is concentrated, the amount of water released into the air is reduced, so that the hygroscopic liquid L is regenerated by the regenerator 4 . The ventilating device 1 supplies a portion of the hygroscopic liquid L sucked from the liquid tank 16 by the processor 1 to the first moisture absorbing liquid line 61' and transports it to the regenerator 40» for transport to the regenerator 40. The wet liquid L is cooled by the second heat exchanger 32 located in the first moisture absorption line 61. The cooled hygroscopic liquid L is supplied to the moisture absorption liquid supply portion 45a of the regenerator 40. The hygroscopic supply unit 45a drops the hygroscopic liquid 1 having a high concentration of cooling to the filler 44, and on the other hand, the air extracted from the outside passes through the filler 44, whereby the hygroscopic liquid L absorbs moisture. Regeneration processing. The hygroscopic liquid L passing through the filler 44 enters the liquid tank 46. A portion of the hygroscopic liquid L in the liquid tank 46 is taken up by the pump 52, and 20 201101993 is supplied to the moisture absorption liquid supply portion 45b through the supply pipe 51. Further, a portion of the hygroscopic liquid L in the liquid tank 46 is supplied to the i-th moisture absorption liquid line 61. The hygroscopic liquid supplied to the first moisture absorption line 61 is cooled by the second heat exchanger 32 and supplied again to the moisture absorption liquid supply unit 45a. As described above, by moisture absorption
!生液體L在填充材44與液槽46之間循環，使吸濕性液體L 之》辰度徐徐地變低。 在進行吸濕性液體L之_再生時，亦可取代從外部 氣體往吸濕性㈣L操取水分之方式，直接供水至吸濕性 液體L’藉此來稀釋吸濕性液體再生機4〇係開啟供水 管54之閥55，對液槽46進行供水。 、、生進行再生處理之液槽46内之吸濕性液體l通過第2 吸濕液管路62返回至處理機1〇。以上，說明了使用溫室用 空調系統7 0之換溃裝署1 ύ» /- 換軋裒置1將經增濕之空氣供應至溫室η 之動作。 ，如上所述，由於從外部榻取之空氣在除濕時係與已冷 卻之吸濕性液冑L氣液接觸，在增濕時係與已加妖之❹ 性液體L氣液接觸，因此在與吸濕性液體㈣ 交換。亦即，拖裔壯苗.】At + 』7』進仃熱 、巩裝置“在調整從外部擷取之空氣之濕 :同時調整溫度。不過，換氣裝置1由於係以濕度為目 才示進行控制，因此右 為 之目標溫度不同之情形。在上述情形： _焊、、®1 1尔使用内部氟體 ::風器73或冷卻用送風機74將溫室 至目標溫度。 ，皿度調整 卜亦可根據吸濕性液體L之溶液溫度與外部氣體 21 201101993 之溫度之溫度差、擷取空氣之流量、吸濕性液冑l之供應 :等’預測伴隨換氣之溫室H内之溫度變化，以在產生顯 著之溫度變化前使用内部氣體燃燒溫風器73或冷卻用送風 機74進行溫度調整。以上，說明了實施形態之溫室用空調 系統70 » = ^本實施形態之溫室用空調系統由於在進行濕度調整 後將空氣供應至溫室H内，因此能在保持溫室Η内之濕度 之同時進行換氣。藉由如上述地保持溫室Η内之濕度即 可抑制疾病之產生，且能促進植物之培育。又，藉由將濕 度適當地保持’而能抑制結露。以往，在溫室頂面結露之 水落下而附著於植物，會成為變色等之原因，但藉由使用 本實施形態之溫室用空調系統70，即能解決此種問題。 本貫施形態之溫室用空調系統7 0藉由擷取濕度經調節 之空氣’而使溫室Η内之空氣所含之水分擴散。藉此，能 得到溫室Η内之空氣之溫度均一化之效果。圖4Α，係顯示 於溫室内測量在高度4m之位置測定之溫度及濕度後之結果 之圖，圖4 B，係顯示於溫室内測量在高度1 · 5 m之位置測定 之溫度及濕度後之結果之圖。圖4C係顯示作為參考之溫室 外之溫度及濕度之資料之圖。以往，會因自地面起之高度 使溫度不同，但可知藉由使用本實施形態之溫室用空調系 統70，在高度4m與高度1.5m之位置之溫度均一致（參照圖 4A，圖 4B)。 溫室用空調系統7〇之換氣裝置1由於進行與氣化鋰之 氣液接觸，因此能除去可能含於外部空氣之有害菌等，將 22 201101993 經淨化之空氣供應至溫室Η内。 溫室用S調系統7G由於具有進行換氣之構成，因此能 燃燒溫室Η内之氧，而能使用較外部氣體燃燒式能量效率 更佳之内部氣體燃燒溫風器73。藉此，可減低加熱成本， 抑制溫室Η栽培之運轉成本。 溫室用空調系統70，由於進行濕度（潛熱）之調整，因 此不需藉由冷卻使室溫（顯熱）降低至某程度，亦能以利用地 下水或自來水之冷卻用送風機74創造出適當之環境。藉 此，可減低冷卻成本，抑制溫室Η栽培之運轉成本。 以上，雖舉出實施形態詳細說明了本發明之溫室用空 調系統，但本發明並不限定於上述實施形態。 上述實施形態中，雖說明了使用熱泵3〇控制吸濕性液 體L之溫度之例，但並不一定要使用熱泵％。例如，當從 熱電複合發電機72取得充分溫度之廢熱時，亦可利用此來 加熱吸濕性液體L，或亦可利用地下水或自來水來冷卻吸濕 性液體L 〇 本發明’具有能保持溫室内之環境之同時進行換氣之 優異效果，而能適用於管理植物之培育環境之植物工廠等 之溫室。 【圖式簡單說明】 圖1係顯示溫室用空調系統之構成之圖。 圖2係顯示溫室用換氣裝置之構成之圖。 圖3 Α係顯示氣化鋰之粉塵除去率之圖。 23 201101993 圖3 B係顯示氣化链之殺菌力之圖。 圖4A係顯示溫室内之溫度及濕度之測量結果之圖。 圖4B係顯示溫室内之溫度及濕度之測量結果之圖。 圖4C係顯示溫室外之溫度及濕度之測量結果之圖。 【主要元件符號說明】 1 溫室用換氣裝置 10 處理機 11 筐體 12 擷取口 13 排氣口 14 填充材 15 吸濕液供應部 16 液槽 17 風扇 18 滤塵Is 19 防蟲用過濾器 20 防蟲用過濾器 21 管 22 泵 23 三向閥 30 熱泵 31 第1熱交換器 32 第2熱交換器 24 201101993 33 壓縮機 34 膨脹閥 35 冷煤管 40 再生機 41 筐體 42 搁取口 43 排氣口 44 填充材 45, 45a, 45b 吸濕液供應部 46 液槽 47 風扇 49 管 50 泵 51 供應管 52 泵 53 加熱源 54 供水管 55 閥 56 濾塵器 57 防蟲用過濾器 58 防蟲用過濾器 61 第1吸濕液管 62 第2吸濕液管 63 閥 25 201101993 64 熱交換器 65 感測器 66 控制部 70 溫室用空調系統 71 照明 72 熱電複合發電機 73 内部氣體燃燒溫風器 74 冷卻用送風機 Η 溫室 L 吸濕性液體 26The raw liquid L circulates between the filler 44 and the liquid tank 46, and the degree of decay of the hygroscopic liquid L is gradually lowered. In the case of performing the regeneration of the hygroscopic liquid L, it is also possible to directly supply water to the hygroscopic liquid L' instead of the moisture from the external gas to the hygroscopic (4) L to dilute the hygroscopic liquid regenerating machine. The valve 55 of the water supply pipe 54 is opened to supply water to the liquid tank 46. The hygroscopic liquid l in the liquid tank 46 subjected to the regeneration treatment is returned to the processor 1 through the second moisture absorption liquid line 62. In the above, the operation of supplying the humidified air to the greenhouse η using the air conditioner system of the greenhouse for the replacement of the air conditioner system 1 ύ» /-. As described above, since the air taken from the outside is in contact with the cooled hygroscopic liquid 胄L during dehumidification, it is in contact with the dehumidified liquid L in the humidification, so that Exchange with hygroscopic liquid (4). That is, dragging the sages.] At + 』7』Into the heat, the Gong device "in the adjustment of the air from the outside to get wet: at the same time adjust the temperature. However, the ventilation device 1 is shown by the humidity Control is carried out, so the right is the target temperature difference. In the above situation: _ welding, ® 1 1 use internal fluorine:: air duct 73 or cooling blower 74 to the greenhouse to the target temperature. It is also possible to predict the temperature difference between the temperature of the solution of the hygroscopic liquid L and the temperature of the external gas 21 201101993, the flow rate of the extracted air, and the supply of the hygroscopic liquid :1: The temperature adjustment is performed using the internal gas combustion air heater 73 or the cooling blower 74 before a significant temperature change occurs. The greenhouse air conditioning system of the embodiment is described above. 70 » = ^ The greenhouse air conditioning system of the present embodiment After the humidity adjustment, the air is supplied to the greenhouse H, so that the humidity can be maintained while maintaining the humidity in the greenhouse. The humidity can be suppressed by maintaining the humidity in the greenhouse as described above. It is possible to promote the cultivation of plants. In addition, it is possible to suppress condensation by appropriately maintaining the humidity. In the past, the water deposited on the top surface of the greenhouse was attached to the plant, which caused discoloration and the like. The greenhouse air conditioning system 70 can solve such a problem. The greenhouse air conditioning system 70 of the present embodiment diffuses the moisture contained in the air in the greenhouse by extracting the humidity-conditioned air. The effect of uniformizing the temperature of the air in the greenhouse can be obtained. Figure 4Α shows the results of measuring the temperature and humidity measured at a height of 4 m in the greenhouse, and Figure 4 B shows the measurement in the greenhouse. A graph showing the results of temperature and humidity measured at a height of 1 · 5 m. Figure 4C is a graph showing the temperature and humidity of the temperature outside the reference. In the past, the temperature was different due to the height from the ground. However, it is understood that the temperature of the position of the height of 4 m and the height of 1.5 m is the same by using the greenhouse air-conditioning system 70 of the present embodiment (see FIG. 4A, FIG. 4B). The ventilation device 1 of the greenhouse air-conditioning system 7 Since it is in contact with the gas-liquid of the vaporized lithium, it is possible to remove the harmful bacteria that may be contained in the outside air, and supply the purified air of 22 201101993 to the greenhouse. The greenhouse S-conditioning system 7G has a composition for performing ventilation. Therefore, it is possible to burn the oxygen in the greenhouse, and it is possible to use the internal gas combustion air heater 73 which is more energy efficient than the external gas combustion type, thereby reducing the heating cost and suppressing the operating cost of the greenhouse cultivation. 70. Since the humidity (latent heat) is adjusted, it is not necessary to reduce the room temperature (sensible heat) to a certain extent by cooling, and it is also possible to create an appropriate environment by the cooling blower 74 using ground water or tap water. It can reduce the cooling cost and inhibit the operating cost of greenhouse cultivation. As described above, the greenhouse air conditioning system of the present invention has been described in detail with reference to the embodiments, but the present invention is not limited to the above embodiments. In the above embodiment, an example in which the temperature of the hygroscopic liquid L is controlled by the heat pump 3 is described, but the heat pump % is not necessarily used. For example, when the waste heat of sufficient temperature is obtained from the thermoelectric composite generator 72, the hygroscopic liquid L may be heated by this, or the groundwater or tap water may be used to cool the hygroscopic liquid L. The present invention has the ability to maintain the greenhouse. The environment in which the environment is tempered at the same time, and it can be applied to a greenhouse such as a plant factory that manages the cultivation environment of plants. BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a view showing the constitution of a greenhouse air conditioning system. Fig. 2 is a view showing the configuration of a greenhouse ventilator. Figure 3 shows the diagram of the dust removal rate of vaporized lithium. 23 201101993 Figure 3 B shows a diagram of the bactericidal power of the gasification chain. Fig. 4A is a graph showing measurement results of temperature and humidity in a greenhouse. Fig. 4B is a graph showing the measurement results of temperature and humidity in the greenhouse. Fig. 4C is a graph showing the measurement results of the temperature and humidity outside the temperature chamber. [Description of main components] 1 Greenhouse ventilator 10 Processor 11 Housing 12 Extraction port 13 Exhaust port 14 Filler 15 Moisture supply unit 16 Tank 17 Fan 18 Filter Is 19 Insect filter 20 Insect filter 21 Tube 22 Pump 23 Three-way valve 30 Heat pump 31 First heat exchanger 32 Second heat exchanger 24 201101993 33 Compressor 34 Expansion valve 35 Cold coal pipe 40 Regenerator 41 Housing 42 Shelf 43 Exhaust port 44 Filling material 45, 45a, 45b Moisture supply unit 46 Tank 47 Fan 49 Tube 50 Pump 51 Supply tube 52 Pump 53 Heat source 54 Water supply pipe 55 Valve 56 Filter 57 Insect filter 58 Insect filter 61 First moisture absorption tube 62 Second moisture absorption tube 63 Valve 25 201101993 64 Heat exchanger 65 Sensor 66 Control unit 70 Greenhouse air conditioning system 71 Illumination 72 Thermoelectric composite generator 73 Internal gas combustion temperature Air blower 74 Cooling blower Η Greenhouse L Hygroscopic liquid 26