JP2019002605A - Open air processing unit - Google Patents

Open air processing unit Download PDF

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JP2019002605A
JP2019002605A JP2017115814A JP2017115814A JP2019002605A JP 2019002605 A JP2019002605 A JP 2019002605A JP 2017115814 A JP2017115814 A JP 2017115814A JP 2017115814 A JP2017115814 A JP 2017115814A JP 2019002605 A JP2019002605 A JP 2019002605A
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wet purification
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outside air
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松本 健
Takeshi Matsumoto
健 松本
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Takenaka Komuten Co Ltd
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Abstract

To provide a technology which can feed open air in an appropriate state to an air supply target space while keeping removal ability of impurities suitable and saving water in an open air processing unit removing impurities from the open air by passing the open air flowing air supply course and fed to the air supply target space to a water membrane of a wet process cleanup unit arranged in the air supply course.SOLUTION: Multiple wet process cleanup units 10 arranged in a row in air supply air course 1 are comprised. Ventilation number adjust means 33 which can adjust number of the wet process cleanup units 10 in ventilation state that open air OA passes in the multiple wet process cleanup units 10, and supply water state adjust means 34 which can adjust a supply water state in each of multiple wet process cleanup units 10.SELECTED DRAWING: Figure 1

Description

本発明は、給気対象空間に供給される外気が給気ファンの送風力により通流する給気風路と、前記給気風路に配置され、所定の設定給水量以上の給水により形成した水膜に外気を通過させて、当該外気から不純物を除去する湿式浄化部とを備えた外気処理装置に関する。   The present invention provides an air supply passage through which outside air supplied to an air supply target space flows by a blowing force of an air supply fan, and a water film formed by water supply that is disposed in the supply air passage and has a predetermined supply water amount or more. The present invention relates to an outside air processing apparatus including a wet purification unit that allows outside air to pass through and removes impurities from the outside air.

従来、給気風路を通流して給気対象空間に供給される外気を、当該給気風路に配置された湿式浄化部の水膜に通過させて、当該外気から化学物質や塵埃等の不純物を除去するように構成された外気処理装置が知られている(例えば、特許文献1を参照。)。
かかる外気処理装置の湿式浄化部は、多孔質セラミック等からなる通気性のエレメント等からなる水膜形成部を有し、そのエレメントの上部に水を散水することで、当該エレメントの表面に水膜を形成する。そして、その水膜に外気を接触させることで、当該外気に含まれている不純物を水膜に吸収させる形態で除去することができる。
Conventionally, the outside air supplied to the supply target space through the supply air passage is passed through the water film of the wet purification section disposed in the supply air passage, and impurities such as chemical substances and dust are removed from the outside air. There is known an outside air processing apparatus configured to be removed (see, for example, Patent Document 1).
The wet purification part of such an outside air treatment apparatus has a water film forming part made of a breathable element made of porous ceramic or the like, and water is sprinkled on the upper part of the element so that a water film is formed on the surface of the element. Form. Then, by bringing outside water into contact with the water film, impurities contained in the outside air can be removed in a form of being absorbed by the water film.

特開2002−95924号公報JP 2002-95924 A

上記のような湿式浄化部を備えた外気処理装置では、節水を図る目的で湿式浄化部での給水量を所定の設定給水量よりも低下させると、エレメントの表面において不純物除去に必要な水膜が適切に形成されない箇所が生じ、結果、不純物の除去能力が急激に悪化する虞がある。従って、所望の不純物の除去能力を発揮するために、外気が通過する湿式浄化部での給水量を常時設定給水量以上に設定する必要があり、給水量を絞って節水を図ることは困難であった。   In the outside air treatment apparatus having the wet purification unit as described above, when the water supply amount in the wet purification unit is lowered below a predetermined set water supply amount for the purpose of saving water, a water film necessary for removing impurities on the surface of the element However, there is a possibility that a portion where the impurity is not properly formed is generated, and as a result, the ability of removing impurities is rapidly deteriorated. Therefore, in order to exert the desired impurity removal capability, it is necessary to set the water supply amount in the wet purification section through which the outside air passes constantly to be equal to or higher than the set water supply amount, and it is difficult to conserve water by reducing the water supply amount. there were.

この実情に鑑み、本発明の主たる課題は、給気風路を通流して給気対象空間に供給される外気を、当該給気風路に配置された湿式浄化部の水膜に通過させて、当該外気から不純物を除去する外気処理装置において、不純物の除去能力を維持しながら、節水を図り、適切な状態の外気を給気対象空間に供給することができる技術を提供する点にある。   In view of this situation, the main problem of the present invention is that the outside air flowing through the supply air passage and supplied to the supply target space is passed through the water film of the wet purification unit disposed in the supply air passage, In the outside air processing apparatus that removes impurities from outside air, it is to provide a technique that can save water and supply outside air in an appropriate state to the air supply target space while maintaining the ability to remove impurities.

本発明の第1特徴構成は、給気対象空間に供給される外気が給気ファンの送風力により通流する給気風路と、
前記給気風路に配置され、所定の設定給水量以上の給水により形成した水膜に外気を通過させて、当該外気から不純物を除去する湿式浄化部とを備えた外気処理装置であって、
前記給気風路において並列配置された複数の前記湿式浄化部を備えると共に、
当該複数の湿式浄化部のうちの外気が通過する通風状態とされる湿式浄化部の数を調整可能な通風数調整手段と、
前記複数の湿式浄化部の夫々における給水状態を調整可能な給水状態調整手段とを備えた点にある。
A first characteristic configuration of the present invention is an air supply air passage through which outside air supplied to the air supply target space flows by the air blowing force of the air supply fan,
An outside air treatment device including a wet purification unit that is disposed in the air supply air passage and allows the outside air to pass through a water film formed by supplying water of a predetermined set amount or more and removes impurities from the outside air,
With a plurality of the wet purification units arranged in parallel in the air supply air passage,
Ventilation number adjusting means capable of adjusting the number of wet purification sections that are in a ventilation state through which outside air passes among the plurality of wet purification sections;
The water supply state adjusting means is capable of adjusting the water supply state in each of the plurality of wet purification sections.

本構成によれば、給気風路において複数の湿式浄化部を並列配置すると共に、上記通風数調整手段を備えるので、通風状態とされる湿式浄化部の数を調整することができる。更に、上記給水状態調整手段を備えるので、夫々の湿式浄化部での給水量を調整することができる。そして、上記通風数調整手段により通風状態とされている湿式浄化部においては、上記給水状態調整手段により給水量を設定給水量に維持して、不純物の除去能力を維持することができる。一方、上記通風数調整手段により非通風状態とされている湿式浄化部においては、上記給水状態調整手段により給水量を設定給水量よりも少ない量に変更する又は給水を停止する形態で減少させて、節水を図ることができる。更に、給気風路に設けられた給気ファンの送風量が減少した場合において、その外気が通過する水膜の面積や水量を減少させれば、給気対象空間に供給される外気の温度や湿度が、水の影響を受けて変動することを抑制することができる。
従って、本発明により、不純物の除去能力を維持しながら、節水を図り、適切な状態の外気を給気対象空間に供給することができる外気処理装置を提供することができる。
According to this configuration, since the plurality of wet purification units are arranged in parallel in the supply air passage and the ventilation number adjusting means is provided, the number of wet purification units in the ventilation state can be adjusted. Furthermore, since the said water supply state adjustment means is provided, the amount of water supply in each wet purification part can be adjusted. And in the wet purification part made into the ventilation | gas_flowing state by the said ventilation number adjustment means, the water supply amount can be maintained by the said water supply state adjustment means to a setting water supply amount, and the removal capability of an impurity can be maintained. On the other hand, in the wet purification section that is not ventilated by the ventilation number adjusting means, the water supply amount is changed to a smaller amount than the set water supply amount by the water supply state adjusting means, or the water supply is reduced in a form of stopping. , Can save water. Furthermore, when the air flow rate of the air supply fan provided in the air supply air passage is reduced, if the area of the water film and the amount of water that the outside air passes through are reduced, the temperature of the outside air supplied to the air supply target space, It can suppress that humidity changes under the influence of water.
Therefore, according to the present invention, it is possible to provide an outside air processing apparatus capable of saving water and supplying outside air in an appropriate state to the air supply target space while maintaining the ability to remove impurities.

本発明の第2特徴構成は、前記給気ファンの送風量の減少に伴って、前記通風数調整手段を制御して、前記通風状態とされる湿式浄化部の数を減少させると共に、前記給水状態調整手段を制御して、前記複数の湿式浄化部のうちの外気が通過しない非通風状態とされる湿式浄化部での給水量を前記設定給水量よりも減少させる節水制御手段を備えた点にある。   According to a second characteristic configuration of the present invention, the number of wet purification units that are in the ventilation state is reduced by controlling the ventilation number adjusting means in accordance with a decrease in the amount of air blown from the supply fan, and the water supply A point is provided with water-saving control means for controlling the state adjusting means to reduce the water supply amount in the wet purification section that is in a non-ventilated state through which the outside air does not pass among the plurality of wet purification sections, than the set water supply amount. It is in.

本構成によれば、上記節水制御手段を備えるので、給気ファンの送風量が減少した場合には、通風状態とされる湿式浄化部の数が自動的に減少すると共に、非通風状態とされた湿式浄化部での給水量が自動的に減少して、効率良く節水を実施することができる。更に、給気ファンの送風量が減少した場合には、それに伴って、その外気が通過する水膜の面積や水量が自動的に減少するので、当該外気の温度や湿度が水の影響を受けて変動するのを効率良く抑制することができる。   According to this configuration, since the water-saving control means is provided, when the amount of air supplied from the air supply fan is reduced, the number of wet purification units that are in the ventilation state is automatically reduced and the ventilation state is not set. In addition, the amount of water supplied in the wet purification unit is automatically reduced, and water can be saved efficiently. Further, when the air supply fan's air flow decreases, the area and water volume of the water film through which the outside air passes automatically decreases, so the temperature and humidity of the outside air are affected by the water. Can be efficiently suppressed.

本発明の第3特徴構成は、前記節水制御手段が、前記非通風状態とされている湿式浄化部での外気の通過を開始するにあたり、当該非通風状態とされている湿式浄化部での給水量を前記設定給水量とした状態で外気の通過を開始する通風開始処理を実行する点にある。   According to a third characteristic configuration of the present invention, when the water-saving control means starts passage of outside air in the non-ventilated wet purification unit, water supply in the non-ventilated wet purification unit It is in the point which performs the ventilation start process which starts the passage of external air in the state which made the quantity the said setting water supply amount.

本構成によれば、上記節水制御手段が上記通風開始処理を実行するので、非通風状態から通風状態に切り替えられる湿式浄化部において、外気の通過を開始するにあたり、外気が通過する当初から、十分な給水量により適切な水膜を形成して、不純物の除去能力を発揮させることができる。   According to this configuration, since the water-saving control unit performs the ventilation start process, in the wet purification unit that is switched from the non-ventilated state to the ventilated state, the start of the passage of the outside air is sufficient to start the passage of the outside air. An appropriate water film can be formed with a sufficient amount of water supply to exhibit the ability to remove impurities.

本発明の第4特徴構成は、前記節水制御手段が、前記複数の湿式浄化部の夫々における通風積算時間を均等化するように、前記非通風状態とする湿式浄化部を決定する通風積算時間均等化処理を実行する点にある。   According to a fourth characteristic configuration of the present invention, the water saving control means determines the wet purification unit to be in the non-ventilated state so as to equalize the ventilation integration time in each of the plurality of wet purification units. The point is to execute the digitization process.

本構成によれば、上記節水制御手段が上記通風積算時間均等化処理を実行するので、通風状態とされる湿式浄化部の数を減少させる場合でも、できるだけ通風積算時間が長い湿式浄化部を通風状態から非通風状態に切り替える形態で、非通風状態とする湿式浄化部を決定して、複数の湿式浄化部の夫々の通負積算時間を均等化することができる。よって、複数の湿式浄化部の夫々における水膜を形成するためのエレメント等の部品の劣化状態等を均等化して、長寿命化を図ることができる。   According to this configuration, since the water-saving control means performs the ventilation integration time equalization process, even when the number of wet purification units that are in the ventilation state is reduced, the ventilation unit has a long ventilation integration time as much as possible. By switching from the state to the non-ventilated state, it is possible to determine the wet purification unit to be in the non-ventilated state, and equalize the accumulated negative time of each of the plurality of wet purification units. Therefore, it is possible to equalize the deterioration state of components such as elements for forming a water film in each of the plurality of wet purification units, thereby extending the life.

本発明の第5特徴構成は、前記複数の湿式浄化部の夫々が、前記水膜が形成される水膜形成部と、当該水膜への外気の通過を断続可能な通風断続部と、当該水膜への給水状態を調整可能な給水部とを有して構成された湿式浄化モジュールとして構成され、
前記通風数調整手段が、前記複数の湿式浄化モジュールの夫々が有する通風断続部で構成され、
前記給水状態調整手段が、前記複数の湿式浄化モジュールの夫々が有する給水部で構成されている点にある。
According to a fifth feature of the present invention, each of the plurality of wet purification sections includes a water film forming section in which the water film is formed, a ventilation intermittent section capable of interrupting passage of outside air to the water film, It is configured as a wet purification module configured to have a water supply unit capable of adjusting the water supply state to the water film,
The ventilation number adjusting means is constituted by a ventilation intermittent portion that each of the plurality of wet purification modules has,
The water supply state adjusting means is constituted by a water supply unit included in each of the plurality of wet purification modules.

本構成によれば、複数の湿式浄化部の夫々が湿式浄化モジュールとして構成されているので、湿式浄化モジュールの複数を給気風路に並列配置するだけで、これら湿式浄化モジュールの夫々が有する通風断続部を通風数調整手段として機能させ、これら湿式浄化モジュールの夫々が有する給水部を給水状態調整手段として機能させることができる。   According to this configuration, each of the plurality of wet purification modules is configured as a wet purification module, and therefore, by simply arranging a plurality of wet purification modules in parallel in the air supply air passage, each of these wet purification modules has an intermittent ventilation. It is possible to allow the water supply section of each of these wet purification modules to function as a water supply state adjusting means.

外気処理装置の概略構成図Schematic configuration diagram of outside air processing equipment 図1に示す外気処理装置に設けられた湿式浄化モジュールの概略構成図Schematic block diagram of the wet purification module provided in the outside air processing apparatus shown in FIG. 図1に示す外気処理装置に設けられた制御装置の概略構成図Schematic configuration diagram of a control device provided in the outside air processing device shown in FIG.

本発明の実施形態について図面に基づいて説明する。
図1に示すように、本実施形態の外気処理装置は、給気ファン2が配置された給気風路1を備える。そして、給気ファン2の送風力により、外気OAが給気風路1に導入され、当該導入された外気OAが給気風路1の内部を通流し、当該通流した外気OAが給気SAとして、屋内等の給気対象空間に供給される。
Embodiments of the present invention will be described with reference to the drawings.
As shown in FIG. 1, the outside air processing apparatus of this embodiment includes an air supply air passage 1 in which an air supply fan 2 is arranged. Then, the outside air OA is introduced into the supply air passage 1 by the air blowing force of the supply fan 2, the introduced outside air OA flows through the inside of the supply air passage 1, and the outside air OA thus flowed is used as the supply air SA. , And supplied to an air supply target space such as indoors.

給気風路1には、水膜に外気OAを通過させて当該外気から化学物質や塵埃等の不純物を除去する湿式浄化モジュール10(湿式浄化部の一例)が配置されている。更に、給気風路1には、内部を通流する外気OAを、外部から供給される冷水や温水等との熱交換により冷却又は加熱するための複数の熱交換器3,4,5が配置されている。この熱交換器3,4,5としては、予熱用熱交換器3、冷却用熱交換器4、再熱用熱交換器5等が、上流側から順に配置されている。上記湿式浄化モジュール10は、冷却用熱交換器4と再熱用熱交換器5との間の領域に配置されている。
即ち、給気風路1に導入された外気OAは、予熱用熱交換器3、冷却用熱交換器4、湿式浄化モジュール10、再熱用熱交換器5を順に通過した後に、給気SAとして給気対象空間に供給される。
A wet purification module 10 (an example of a wet purification unit) that removes impurities such as chemical substances and dust from the outside air by allowing the outside air OA to pass through the water film is disposed in the supply air passage 1. In addition, a plurality of heat exchangers 3, 4, 5 are disposed in the supply air passage 1 for cooling or heating the outside air OA flowing through the inside by heat exchange with cold water or hot water supplied from the outside. Has been. As the heat exchangers 3, 4, and 5, a preheating heat exchanger 3, a cooling heat exchanger 4, a reheating heat exchanger 5, and the like are sequentially arranged from the upstream side. The wet purification module 10 is disposed in a region between the cooling heat exchanger 4 and the reheating heat exchanger 5.
That is, the outside air OA introduced into the supply air passage 1 passes through the heat exchanger 3 for preheating, the heat exchanger 4 for cooling, the wet purification module 10 and the heat exchanger 5 for reheating in this order, and is then supplied as an air supply SA. It is supplied to the air supply target space.

例えば、外気OAの温度が高い夏季等においては、給気風路1に導入された外気OAは、冷却用熱交換器4において冷却された後に、湿式浄化モジュール10を通過して、不純物の除去が行われる。そして、このように冷却された後に不純物が除去された外気OAが、給気SAとして給気対象空間に供給される。
一方、外気OAの温度が低い冬季等においては、給気風路1に導入された外気OAは、予熱用熱交換器3において加熱された後に、湿式浄化モジュール10を通過して、不純物の除去が行われる。そして、このように加熱された後に不純物が除去された外気OAが、再熱用熱交換器5において適宜加熱された上で、給気SAとして給気対象空間に供給される。
For example, in summer when the temperature of the outside air OA is high, the outside air OA introduced into the supply air passage 1 is cooled in the cooling heat exchanger 4 and then passes through the wet purification module 10 to remove impurities. Done. Then, the outside air OA from which impurities are removed after being cooled in this way is supplied to the air supply target space as the air supply SA.
On the other hand, in the winter season when the temperature of the outside air OA is low, the outside air OA introduced into the supply air passage 1 is heated in the preheating heat exchanger 3 and then passes through the wet purification module 10 to remove impurities. Done. The outside air OA from which impurities have been removed after being heated in this way is appropriately heated in the reheat heat exchanger 5 and then supplied to the supply target space as the supply air SA.

湿式浄化モジュール10は、図2に示すように、水膜が形成される水膜形成部15を有して構成されている。この水膜形成部15は、多孔質セラミック等からなる通気性のエレメント16と、そのエレメント16の上端部に水を散水する散水管17と、そのエレメント16の下端部から滴下する水を受けるドレンパン18とを有して構成されている。更に、湿式浄化モジュール10は、水膜形成部15に形成される水膜への外気OAの通過を断続可能な通風断続部11と、水膜形成部15に形成される水膜への給水状態を調整可能な給水弁20(給水部の一例)とを有して構成されている。   As shown in FIG. 2, the wet purification module 10 includes a water film forming unit 15 in which a water film is formed. The water film forming portion 15 includes a breathable element 16 made of a porous ceramic, a water spray pipe 17 for spraying water on the upper end portion of the element 16, and a drain pan that receives water dripped from the lower end portion of the element 16. 18. Further, the wet purification module 10 includes a ventilation intermittent portion 11 capable of intermittently passing the outside air OA to the water film formed in the water film forming portion 15, and a water supply state to the water film formed in the water film forming portion 15. And a water supply valve 20 (an example of a water supply unit) that can be adjusted.

湿式浄化モジュール10では、散水管17からエレメント16の上端部に水が散水されることで、エレメント16全体に水が供給され、当該エレメント16の表面に水膜が形成される。そして、エレメント16を通過する外気OAが、当該エレメント16の表面に形成された水膜と接触することで、当該外気OAに含まれている不純物が水膜に吸収される形態で除去されることになる。また、不純物を吸収した水は、エレメント16の下端部から滴下してドレンパン18に受けられ、最終的にはドレン水DWとして外部に排出されることになる。   In the wet purification module 10, water is sprinkled from the sprinkling pipe 17 to the upper end portion of the element 16, whereby water is supplied to the entire element 16 and a water film is formed on the surface of the element 16. Then, when the outside air OA passing through the element 16 comes into contact with the water film formed on the surface of the element 16, impurities contained in the outside air OA are removed in a form that is absorbed by the water film. become. Further, the water that has absorbed the impurities is dropped from the lower end portion of the element 16 and received by the drain pan 18, and is finally discharged to the outside as the drain water DW.

湿式浄化モジュール10は、水膜形成部15として、外気OAの流れ方向に沿って上流側に配置された前段側水膜形成部15aと、外気OAの流れ方向に沿って前段側水膜形成部15aよりも下流側に配置された後段側水膜形成部15bとを備えた2段式に構成されている。そして、後段側水膜形成部15bの散水管17bには、開放された給水弁20を介して水道管から供給された給水SWが供給される。一方、前段側水膜形成部15aの散水管17aには、上記給水弁20の開放と連動して作動された給水ポンプ19を介して後段側水膜形成部15bのドレンパン18bに貯留する貯留水が供給される。尚、本実施形態とは逆に、給水SWを前段側水膜形成部15aに供給し、前段側水膜形成部15aのドレンパン18aに貯留する貯留水を後段側水膜形成部15bに供給するように構成しても構わない。   The wet purification module 10 includes, as the water film forming unit 15, a front-side water film forming unit 15 a disposed upstream in the flow direction of the outside air OA, and a pre-stage side water film forming unit along the flow direction of the outside air OA. It is configured in a two-stage system including a rear-stage water film forming portion 15b disposed downstream of 15a. Then, the water supply SW supplied from the water pipe through the opened water supply valve 20 is supplied to the water spray pipe 17b of the rear-stage water film forming unit 15b. On the other hand, in the water spray pipe 17a of the front-stage water film forming section 15a, the stored water stored in the drain pan 18b of the rear-stage water film forming section 15b via the water supply pump 19 operated in conjunction with the opening of the water supply valve 20 is provided. Is supplied. Contrary to this embodiment, the water supply SW is supplied to the front-stage water film forming section 15a, and the stored water stored in the drain pan 18a of the front-stage water film forming section 15a is supplied to the rear-stage water film forming section 15b. You may comprise as follows.

湿式浄化モジュール10では、給水弁20を開放すると共に給水ポンプ19を作動させることで、水膜形成部15に所定の設定給水量以上の水を供給する通常給水状態となる。一方、給水弁20を遮断すると共に給水ポンプ19を停止させることで、水膜形成部15への水の供給を停止する給水停止状態となる。ここで、上記設定給水量は、水膜形成部15における外気OAからの不純物の除去能力を好適なものに維持するのに必要な最小給水量又はそれ以上の給水量として設定されている。
また、給水弁20の開度調整を行うことで、それと連動して給水ポンプ19の出力調整が行われて、夫々の水膜形成部15a,15bへの給水量を調整可能に構成されている。
In the wet purification module 10, the water supply valve 20 is opened and the water supply pump 19 is operated to enter a normal water supply state in which the water film forming unit 15 is supplied with water of a predetermined set amount or more. On the other hand, by shutting off the water supply valve 20 and stopping the water supply pump 19, a water supply stop state is reached in which the supply of water to the water film forming unit 15 is stopped. Here, the set water supply amount is set as a minimum water supply amount or a water supply amount equal to or higher than the minimum water supply amount necessary for maintaining the ability of removing impurities from the outside air OA in the water film forming unit 15 to be suitable.
Further, by adjusting the opening degree of the water supply valve 20, the output adjustment of the water supply pump 19 is performed in conjunction with it, and the water supply amount to each of the water film forming portions 15a and 15b can be adjusted. .

そして、通常給水状態では、開放状態とされた給水弁20から供給された給水SWが、後段側水膜形成部15bのエレメント16bに供給され、当該エレメント16bの表面に水膜を形成することになる。一方、エレメント16bからドレンパン18bに滴下した水が、作動状態とされた給水ポンプ19により汲み上げられて前段側水膜形成部15aのエレメント16aに供給され、当該エレメント16aの表面に水膜を形成することになる。更に、エレメント16aからドレンパン18aに滴下した水がドレン水DWとして外部に排出される。
尚、本実施形態では、湿式浄化モジュール10を2段式に構成しているが、本発明はこの構成に限定されるものではなく、1段式又は3段式以上に構成しても構わない。また、本実施形態では、一方の水膜形成部15bのドレン水(ドレンパン18bの貯留水)を他方の水膜形成部15aの給水として利用するように構成しているが、本発明はこの構成に限定されるものではなく、夫々の水膜形成部に対して、ドレン水を利用せず、各別に給水を行っても構わない。
In the normal water supply state, the water supply SW supplied from the open water supply valve 20 is supplied to the element 16b of the rear water film forming portion 15b, and a water film is formed on the surface of the element 16b. Become. On the other hand, water dripped from the element 16b to the drain pan 18b is pumped up by the water supply pump 19 in the activated state and supplied to the element 16a of the front water film forming portion 15a, thereby forming a water film on the surface of the element 16a. It will be. Further, water dripped from the element 16a to the drain pan 18a is discharged to the outside as drain water DW.
In this embodiment, the wet purification module 10 is configured in a two-stage type, but the present invention is not limited to this configuration, and may be configured in a one-stage type or a three-stage type or more. . In the present embodiment, the drain water of one water film forming unit 15b (the water stored in the drain pan 18b) is configured to be used as water supply for the other water film forming unit 15a. It is not limited to this, and each water film forming unit may be supplied with water separately without using drain water.

本実施形態において、外気OAの通過を断続可能な通風断続部11は、公知の電動式ダンパとして構成されている。具体的には、水膜形成部15に通じる枠体13と、当該枠体13内に配置された複数のフラップ12と、それら複数のフラップ12の回転角度を変更可能な電動アクチュエータ14とを備える。そして、電動アクチュエータ14により複数のフラップ12の回転角度を変更することで、開放状態と遮断状態とが切り替わり、枠体13内での外気OAの通過を断続可能となる。即ち、通風断続部11を開放状態とすると、水膜形成部15を外気OAが通過する通風状態となり、通風断続部11を遮断状態とすると、水膜形成部15を外気OAが通過しない非通風状態となる。
尚、本実施形態では、通風断続部11を電動式ダンパとして構成しているが、本発明はこの構成に限定されるものではなく、電動式シャッターや電動式バタフライ弁等のような他の構成を採用して、外気OAの通過を断続可能としても構わない。
In this embodiment, the ventilation intermittent part 11 which can interrupt the passage of outside air OA is comprised as a well-known electric damper. Specifically, a frame body 13 that communicates with the water film forming unit 15, a plurality of flaps 12 disposed in the frame body 13, and an electric actuator 14 that can change the rotation angles of the plurality of flaps 12 are provided. . Then, by changing the rotation angle of the plurality of flaps 12 by the electric actuator 14, the open state and the cut-off state are switched, and the passage of the outside air OA in the frame body 13 can be interrupted. That is, when the ventilation intermittent part 11 is opened, the outside air OA passes through the water film forming part 15, and when the ventilation intermittent part 11 is shut off, the outside air OA does not pass through the water film forming part 15. It becomes a state.
In the present embodiment, the ventilation intermittent portion 11 is configured as an electric damper, but the present invention is not limited to this configuration, and other configurations such as an electric shutter, an electric butterfly valve, and the like. And the passage of the outside air OA can be interrupted.

図1に示すように、外気処理装置の給気風路1には、3つの湿式浄化モジュール10が並列状態で配置されている。即ち、給気風路1の横断方向の中央部には、第2湿式浄化モジュール10Bが配置され、その両側方側の夫々には、第1湿式浄化モジュール10A及び第3湿式浄化モジュール10Cが配置されている。   As shown in FIG. 1, three wet purification modules 10 are arranged in parallel in the supply air path 1 of the outside air processing apparatus. That is, the second wet purification module 10B is disposed in the central portion in the transverse direction of the supply air passage 1, and the first wet purification module 10A and the third wet purification module 10C are disposed on both sides thereof. ing.

上記3つの湿式浄化モジュール10A,10B,10Cの夫々に設けられた通風断続部11が、水膜形成部15を外気OAが通過する通風状態とされる湿式浄化モジュール10の数(以下、「通風数」と呼ぶ場合がある。)を調整可能な通風数調整手段33(図3参照)として機能する。
また、上記3つの湿式浄化モジュール10A,10B,10Cの夫々に設けられた給水弁20が、当該3つの湿式浄化モジュール10の夫々における給水量を調整可能な給水状態調整手段34(図3参照)として機能する。
尚、図1(a)〜(c)の各図において、遮断状態の給水弁20を黒塗りで表し、開放状態の給水弁20を白抜きで表している。
The number of the wet purification modules 10 (hereinafter referred to as “ventilation”) in which the ventilation intermittent portions 11 provided in each of the three wet purification modules 10A, 10B, and 10C are in a ventilation state in which the outside air OA passes through the water film forming portion 15. It may be referred to as “number”.) Functions as an adjustable ventilation number adjusting means 33 (see FIG. 3).
In addition, the water supply valve 20 provided in each of the three wet purification modules 10A, 10B, and 10C can adjust the water supply amount in each of the three wet purification modules 10 (see FIG. 3). Function as.
In addition, in each figure of Fig.1 (a)-(c), the water supply valve 20 of the interruption | blocking state is represented by black, and the water supply valve 20 of the open state is represented by white.

図3に示すように、外気処理装置には、運転を制御する制御装置30が設けられている。この制御装置30は、所定のプログラムを実行することにより、所定の空調制御を実行する空調制御手段31、及び、所定の節水制御を実行する節水制御手段32として機能する。
以下、これら空調制御手段31及び節水制御手段32の詳細について、図1及び図3を参照して順に説明を加える。
As shown in FIG. 3, the outside air processing device is provided with a control device 30 that controls the operation. The control device 30 functions as an air conditioning control unit 31 that executes predetermined air conditioning control and a water saving control unit 32 that executes predetermined water saving control by executing a predetermined program.
Hereinafter, the details of the air conditioning control means 31 and the water saving control means 32 will be described in order with reference to FIGS. 1 and 3.

〔空調制御手段〕
空調制御手段31が実行する空調制御では、先ず、給気風路1から給気対象空間に供給される給気SAの温度や湿度、更には給気対象空間において発熱する人員の数や生産機器の稼働率等に基づいて空調負荷を算出する。そして、このように算出した空調負荷に基づいて、熱交換器3,4,5への熱媒体の供給量を制御すると共に、給気ファン2の送風量を制御する形態で、給気対象空間の温度及び湿度を所望の温度及び湿度に調整する。即ち、空調制御手段31は、空調負荷が小さくなるほど、熱交換器3,4,5への熱媒体の供給量を減少側に調整すると共に、給気ファン2の送風量を減少側に調整するように構成されている。
尚、本実施形態では、上記空調負荷の算出方法の一例を示したが、適宜変更しても構わない。
[Air conditioning control means]
In the air-conditioning control executed by the air-conditioning control means 31, first, the temperature and humidity of the supply air SA supplied from the supply air path 1 to the supply target space, and further the number of personnel generating heat in the supply target space and the production equipment The air conditioning load is calculated based on the operating rate. Then, based on the air conditioning load calculated in this way, the supply amount of the heat medium to the heat exchangers 3, 4, 5 is controlled, and the air supply amount of the supply fan 2 is controlled in the form of controlling the supply air space. The temperature and humidity are adjusted to the desired temperature and humidity. That is, the air conditioning control means 31 adjusts the supply amount of the heat medium to the heat exchangers 3, 4, 5 to the decreasing side and adjusts the air supply amount of the air supply fan 2 to the decreasing side as the air conditioning load decreases. It is configured as follows.
In the present embodiment, an example of the calculation method of the air conditioning load is shown, but it may be changed as appropriate.

〔節水制御手段〕
節水制御手段32は、所定の節水制御を実行すると共に、その節水制御において所定の通風開始処理及び通風積算時間均等化処理を実行するように構成されている。以下、これら節水制御、並びにその節水制御において実行される通風開始処理及び通風積算時間均等化処理の詳細について順に説明を加える。
[Water-saving control means]
The water saving control means 32 is configured to execute predetermined water saving control and to execute predetermined ventilation start processing and ventilation integration time equalization processing in the water saving control. Hereinafter, the details of the water saving control and the ventilation start processing and ventilation integration time equalization processing executed in the water saving control will be described in order.

(節水制御)
上記節水制御手段32が実行する節水制御では、上記空調制御により給気ファン2の送風量が減少された場合において、その減少に伴って、通風数調整手段33を制御すると共に、給水状態調整手段34を制御する。
具体的には、通風数調整手段33の制御では、開放状態である一部の通風断続部11を遮断する形態で、複数の湿式浄化モジュール10のうちの外気OAが通過する通風状態とされる湿式浄化モジュール10の数(通風数)を減少させる。更に、給水状態調整手段34の制御では、複数の湿式浄化モジュール10のうちの外気OAが通過しない非通風状態とされる湿式浄化モジュール10での給水量を設定給水量よりも減少させる。
(Water saving control)
In the water-saving control executed by the water-saving control means 32, when the air flow rate of the air supply fan 2 is reduced by the air-conditioning control, the air flow rate adjusting means 33 is controlled and the water supply state adjusting means is accompanied with the reduction. 34 is controlled.
Specifically, in the control of the ventilation rate adjusting means 33, the ventilation state through which the outside air OA of the plurality of wet purification modules 10 passes is set in a form in which some ventilation interruption / interconnection portions 11 in the open state are blocked. The number of wet cleaning modules 10 (the number of ventilation) is reduced. Further, in the control of the water supply state adjusting means 34, the water supply amount in the wet purification module 10 that is in a non-ventilated state through which the outside air OA does not pass among the plurality of wet purification modules 10 is reduced from the set water supply amount.

例えば、図1(c)に示すように、2つの第2及び第3湿式浄化モジュール10B,10Cが通風状態(外気OAが通過する状態)であり、且つ、これら第2及び第3湿式浄化モジュール10B,10Cが通常給水状態(設定給水量以上の給水が行われている状態)である場合を想定する。この状態において、上記空調制御により給気ファン2の送風量が減少された場合には、図1(a)に示すように、第2湿式浄化モジュール10Bは、通風状態且つ通常給水状態に維持される。一方、第3湿式浄化モジュール10Cは、通風断続部11及び給水弁20が制御されて、非通風状態(外気OAが遮断された状態)且つ給水停止状態(給水が停止された状態)に切り替えられる。即ち、通風数が自動的に2から1に減少されると共に、湿式浄化モジュール10全体への給水SWの給水量が自動的に減少されることになって、節水が図られることになる。
尚、本実施形態では、外気OAが通過しない非通風状態とされる湿式浄化モジュール10の給水量を減少させる形態の一例として、当該湿式浄化モジュール10への給水状態を給水停止状態とするように構成したが、給水停止状態とするのではなく、給水量を上記設定給水量よりも少ない所定の小給水量に設定する小流量給水状態とするように構成しても構わない。
For example, as shown in FIG. 1C, the two second and third wet purification modules 10B and 10C are in a ventilated state (a state in which the outside air OA passes), and these second and third wet purification modules. A case is assumed in which 10B and 10C are in a normal water supply state (a state where water supply is performed in excess of the set water supply amount). In this state, when the air blowing amount of the air supply fan 2 is reduced by the air conditioning control, the second wet purification module 10B is maintained in the ventilation state and the normal water supply state as shown in FIG. The On the other hand, the third wet purification module 10C is switched to a non-ventilated state (a state where the outside air OA is shut off) and a water supply stopped state (a state where the water supply is stopped) by controlling the ventilation intermittent portion 11 and the water supply valve 20. . That is, the number of ventilations is automatically reduced from 2 to 1, and the water supply amount of the water supply SW to the entire wet purification module 10 is automatically reduced, thereby saving water.
In this embodiment, as an example of a mode of reducing the amount of water supplied to the wet purification module 10 that is in a non-ventilated state through which the outside air OA does not pass, the water supply state to the wet purification module 10 is set to a water supply stop state. Although configured, the water supply stop state may not be set, but a small flow rate water supply state in which the water supply amount is set to a predetermined small water supply amount smaller than the set water supply amount may be set.

例えば、湿式浄化モジュール10を通過する外気OAは、冷却用熱交換器4により冷却されて、給水SWよりも低温となっている場合がある。この場合、給気ファン2の送風量が減少した際に、湿式浄化モジュール10において外気OAが接触する水膜の面積や水量が大きすぎると、当該外気OAが所望の温度又は湿度よりも昇温又は加湿されることが懸念される。
そこで、本実施形態の外気処理装置では、給気ファン2の送風量が減少した際に、通風数の減少に伴って、外気OAが接触する水膜の面積や水量を自動的に減少させるので、外気OAの昇温や加湿を抑制し、当該外気OAの温度や湿度を安定化させることができる。
For example, the outside air OA passing through the wet purification module 10 may be cooled by the cooling heat exchanger 4 and at a lower temperature than the feed water SW. In this case, when the air volume of the supply air fan 2 decreases and the area of the water film and the amount of water that the outside air OA contacts in the wet purification module 10 are too large, the outside air OA is heated to a temperature higher than a desired temperature or humidity. Or there is a concern of being humidified.
Therefore, in the outside air processing apparatus of the present embodiment, when the air flow rate of the air supply fan 2 is decreased, the area of the water film and the amount of water in contact with the outside air OA are automatically reduced as the ventilation number decreases. The temperature rise and humidification of the outside air OA can be suppressed, and the temperature and humidity of the outside air OA can be stabilized.

(通風開始処理)
上記節水制御において実行される通風開始処理では、非通風状態とされている湿式浄化モジュール10において、当該湿式浄化モジュール10での外気OAの通過を開始するにあたり、給水量を設定給水量とした状態で外気OAの通過を開始する。
具体的には、第3湿式浄化モジュール10Cにおいて、通風断続部11が遮断された非通風状態(図1(a)を参照)から通風断続部11が開放された通風状態(図1(c)を参照)に切り替えて、外気OAの通過を開始する場合を想定する。この場合において、節水制御手段32は、通風断続部11を開放する時点よりも前に、湿式浄化モジュール10への給水状態を給水停止状態から通常給水状態に切り替えて給水を再開して(図1(b)を参照)、給水量を設定給水量以上に復帰させる。すると、この第3湿式浄化モジュール10Cでは、外気OAが通過する当初から、十分な設定給水量以上の給水により適切な水膜が形成されて、所望の不純物の除去能力が発揮されることになる。
(Ventilation start processing)
In the ventilation start process executed in the water-saving control, in the wet purification module 10 that is in a non-ventilated state, a state in which the water supply amount is set to the set water supply amount when the passage of the outside air OA in the wet purification module 10 is started. The passage of outside air OA starts.
Specifically, in the third wet purification module 10C, the ventilation intermittent state 11 is opened from the non-ventilated state (see FIG. 1 (a)) where the ventilation intermittent portion 11 is blocked (see FIG. 1 (c)). )) And the passage of the outside air OA is assumed. In this case, the water-saving control means 32 restarts the water supply by switching the water supply state to the wet purification module 10 from the water supply stop state to the normal water supply state before the time when the ventilation intermittent part 11 is opened (FIG. 1). (Refer to (b)), the water supply amount is returned to the set water supply amount or more. Then, in the third wet purification module 10C, an appropriate water film is formed by supplying water of a sufficient set amount or more from the beginning when the outside air OA passes, and a desired impurity removal capability is exhibited. .

尚、給水弁20を給水停止状態から通常給水状態に切り替える給水タイミングについては、通風断続部11を開放する通風タイミングよりも前であれば良い。例えばエレメント16(図2を参照)全体に適切な水膜が形成された段階で通風が開始されるように、上記給水タイミングを設定することができる。また、非通風状態とされる湿式浄化モジュール10への給水状態が小流量給水状態である場合には、通風断続部11を開放する時点よりも前に、湿式浄化モジュール10への給水状態を小流量給水状態から通常給水状態に切り替えて給水量を設定給水量以上に復帰させるように構成することができる。更に、次に通風数が増加された場合に、非通風状態から通風状態に切り替えられる対象として決定された湿式浄化モジュール10については、予め給水量を設定給水量以上に維持しておくように構成しても構わない。   In addition, about the water supply timing which switches the water supply valve 20 from a water supply stop state to a normal water supply state, it should just be before the ventilation timing which opens the ventilation intermittent part 11. FIG. For example, the water supply timing can be set so that ventilation is started when an appropriate water film is formed on the entire element 16 (see FIG. 2). Further, when the water supply state to the wet purification module 10 that is set to the non-ventilated state is a small flow rate water supply state, the water supply state to the wet purification module 10 is reduced before the time when the ventilation intermittent portion 11 is opened. It can be configured to switch from the flow rate water supply state to the normal water supply state to return the water supply amount to the set water supply amount or more. Further, when the ventilation rate is increased next time, the wet purification module 10 determined as the target to be switched from the non-ventilated state to the ventilated state is configured to keep the water supply amount at or above the preset water supply amount in advance. It doesn't matter.

(通風積算時間均等化処理)
上記節水制御において実行される通風時間均等化処理では、夫々の湿式浄化モジュール10における通風積算時間を均等化するように、非通風状態とする湿式浄化モジュール10を決定する。
具体的には、節水制御手段32は、夫々の湿式浄化モジュール10において通風状態とされた積算時間である通風積算時間をタイマー(図示省略)等で計測する。そして、通風数を減少させる場合には、その時点において通風状態となっている湿式浄化モジュール10のうち、通風積算時間が最も長い湿式浄化モジュール10を非通風状態に切り替える。このことで、夫々の湿式浄化モジュール10における水膜を形成するためのエレメント16(図2を参照)等の部品の劣化状態等が均等化され、長寿命化が図られることになる。
(Ventilation integration time equalization process)
In the ventilation time equalization process executed in the water saving control, the wet purification modules 10 to be in the non-ventilated state are determined so as to equalize the ventilation integration time in each wet purification module 10.
Specifically, the water-saving control means 32 measures the ventilation integration time, which is the integration time in which the wet purification module 10 is in the ventilation state, with a timer (not shown) or the like. When the number of ventilations is reduced, among the wet purification modules 10 that are in the ventilation state at that time, the wet purification module 10 with the longest ventilation integration time is switched to the non-ventilation state. As a result, the deterioration state of components such as the element 16 (see FIG. 2) for forming a water film in each wet purification module 10 is equalized, and the service life is extended.

〔別実施形態〕
本発明の他の実施形態について説明する。尚、以下に説明する各実施形態の構成は、それぞれ単独で適用するものに限られず、他の実施形態の構成と組み合わせて適用することも可能である。
[Another embodiment]
Another embodiment of the present invention will be described. Note that the configuration of each embodiment described below is not limited to being applied alone, and may be applied in combination with the configuration of another embodiment.

(1)上記実施形態では、節水制御手段32を備え、給気ファン2の送風量の減少に伴って通風数調整手段33及び給水状態調整手段34を制御して、通風数の減少と非通風状態とされる湿式浄化モジュール10での給水量の減少とを自動的に行うように構成したが、これら通風数調整手段33及び給水状態調整手段34の操作を手動で実行するように構成しても構わない。 (1) In the above embodiment, the water-saving control unit 32 is provided, and the ventilation number adjusting unit 33 and the water supply state adjusting unit 34 are controlled in accordance with the decrease in the air flow rate of the air supply fan 2, thereby reducing the ventilation number and non-ventilation. Although the water supply amount in the wet purification module 10 to be in a state is automatically reduced, the operation of the ventilation rate adjusting means 33 and the water supply state adjusting means 34 is configured to be executed manually. It doesn't matter.

(2)上記実施形態では、給気ファン2の送風量が減少した場合に、湿式浄化モジュール10の通風数及び給水量を減少させるように構成したが、例えば給気SAの温度や湿度が高い場合に、給気ファン2の送風量を減少させることなく、湿式浄化モジュール10の通風数及び給水量を減少させるように構成しても構わない。この場合、湿式浄化モジュール10の通風数及び給水量の減少により、湿式浄化モジュール10において外気OAが接触する水膜の面積や水量が減少する。よって、湿式浄化モジュール10を通過した外気OAである給気SAの昇温や加湿を抑制することができ、当該給気SAの温度や湿度を安定化させることができる。 (2) In the said embodiment, when the ventilation volume of the air supply fan 2 decreased, it comprised so that the ventilation rate and water supply amount of the wet purification module 10 might be decreased, but the temperature and humidity of supply air SA are high, for example In this case, the air flow rate and the water supply amount of the wet purification module 10 may be reduced without reducing the air blowing amount of the air supply fan 2. In this case, the area of the water film and the amount of water in contact with the outside air OA in the wet purification module 10 are reduced due to the reduction in the number of ventilations and the amount of water supply of the wet purification module 10. Therefore, the temperature increase and humidification of the supply air SA that is the outside air OA that has passed through the wet purification module 10 can be suppressed, and the temperature and humidity of the supply air SA can be stabilized.

(3)上記実施形態では、水膜形成部15、通風断続部11、給水弁20等を湿式浄化モジュール10としてモジュール化して外気処理装置に搭載する例を説明したが、これら各部位を個別の単体で外気処理装置に設けるように構成しても構わない。 (3) In the above embodiment, the example in which the water film forming unit 15, the ventilation intermittent unit 11, the water supply valve 20, and the like are modularized as the wet purification module 10 and mounted on the outside air processing apparatus has been described. You may comprise so that it may provide in an external air processing apparatus by itself.

(4)上記実施形態では、給気風路1に複数の湿式浄化部を並列状態で配置するにあたり、湿式浄化部としての湿式浄化モジュール10を3つ配置した例を示したが、湿式浄化部の数は複数であれば良く、例えば、2つ又は4つ以上の湿式浄化部を給気風路に並列状態で配置しても構わない。 (4) In the above embodiment, when arranging a plurality of wet purification units in the supply air passage 1 in parallel, an example in which three wet purification modules 10 as wet purification units are arranged is shown. The number may be plural, and for example, two or four or more wet purification units may be arranged in parallel with the supply air passage.

1 給気風路
2 給気ファン
10 湿式浄化モジュール(湿式浄化部)
11 通風断続部
15 水膜形成部
20 給水弁(給水部)
32 節水制御手段
33 通風数調整手段
34 給水状態調整手段
OA 外気
SW 給水
1 Supply Air Path 2 Supply Air Fan 10 Wet Purification Module (Wet Purification Unit)
11 Ventilation intermittent part 15 Water film formation part 20 Water supply valve (water supply part)
32 Water saving control means 33 Ventilation number adjustment means 34 Water supply state adjustment means OA Outside air SW Water supply

Claims (5)

給気対象空間に供給される外気が給気ファンの送風力により通流する給気風路と、
前記給気風路に配置され、所定の設定給水量以上の給水により形成した水膜に外気を通過させて、当該外気から不純物を除去する湿式浄化部とを備えた外気処理装置であって、
前記給気風路において並列配置された複数の前記湿式浄化部を備えると共に、
当該複数の湿式浄化部のうちの外気が通過する通風状態とされる湿式浄化部の数を調整可能な通風数調整手段と、
前記複数の湿式浄化部の夫々における給水状態を調整可能な給水状態調整手段とを備えた外気処理装置。
An air supply passage through which the outside air supplied to the air supply target space flows through the air supply fan;
An outside air treatment device including a wet purification unit that is disposed in the air supply air passage and allows the outside air to pass through a water film formed by supplying water of a predetermined set amount or more and removes impurities from the outside air,
With a plurality of the wet purification units arranged in parallel in the air supply air passage,
Ventilation number adjusting means capable of adjusting the number of wet purification sections that are in a ventilation state through which outside air passes among the plurality of wet purification sections;
An outside air processing apparatus comprising: a water supply state adjusting means capable of adjusting a water supply state in each of the plurality of wet purification units.
前記給気ファンの送風量の減少に伴って、前記通風数調整手段を制御して、前記通風状態とされる湿式浄化部の数を減少させると共に、前記給水状態調整手段を制御して、前記複数の湿式浄化部のうちの外気が通過しない非通風状態とされる湿式浄化部での給水量を前記設定給水量よりも減少させる節水制御手段を備えた請求項1に記載の外気処理装置。   Along with a decrease in the air flow rate of the air supply fan, the ventilation number adjusting means is controlled to reduce the number of wet purification sections to be in the ventilation state, and the water supply state adjusting means is controlled to The outside air processing apparatus according to claim 1, further comprising: a water-saving control unit configured to reduce a water supply amount in the wet purification unit that is in a non-ventilated state through which the outside air does not pass among the plurality of wet purification units, than the set water supply amount. 前記節水制御手段が、前記非通風状態とされている湿式浄化部での外気の通過を開始するにあたり、当該非通風状態とされている湿式浄化部での給水量を前記設定給水量とした状態で外気の通過を開始する通風開始処理を実行する請求項2に記載の外気処理装置。   When the water-saving control means starts the passage of outside air in the non-ventilated wet purification unit, the water supply amount in the non-ventilated wet purification unit is set to the set water supply amount The outside air processing apparatus according to claim 2, wherein ventilation start processing for starting passage of outside air is executed. 前記節水制御手段が、前記複数の湿式浄化部の夫々における通風積算時間を均等化するように、前記非通風状態とする湿式浄化部を決定する通風積算時間均等化処理を実行する請求項2又は3に記載の外気処理装置。   The water saving control means executes ventilation integrated time equalization processing for determining the wet purification unit to be in the non-ventilated state so as to equalize the ventilation integrated time in each of the plurality of wet purification units. 3. An outside air processing apparatus according to 3. 前記複数の湿式浄化部の夫々が、前記水膜が形成される水膜形成部と、当該水膜への外気の通過を断続可能な通風断続部と、当該水膜への給水状態を調整可能な給水部とを有して構成された湿式浄化モジュールとして構成され、
前記通風数調整手段が、前記複数の湿式浄化モジュールの夫々が有する通風断続部で構成され、
前記給水状態調整手段が、前記複数の湿式浄化モジュールの夫々が有する給水部で構成されている請求項1〜4の何れか1項に記載の外気処理装置。
Each of the plurality of wet purification units can adjust a water film forming unit in which the water film is formed, a ventilation intermittent part capable of interrupting passage of outside air to the water film, and a water supply state to the water film Configured as a wet purification module configured with a water supply unit,
The ventilation number adjusting means is constituted by a ventilation intermittent portion that each of the plurality of wet purification modules has,
The outside air processing apparatus according to any one of claims 1 to 4, wherein the water supply state adjusting means is configured by a water supply unit included in each of the plurality of wet purification modules.
JP2017115814A 2017-06-13 2017-06-13 Open air processing unit Pending JP2019002605A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110772905A (en) * 2019-11-16 2020-02-11 江苏九洲环保技术有限公司 Environment-friendly treatment cleaning device
CN112146193A (en) * 2019-06-28 2020-12-29 广东美的制冷设备有限公司 Air purification assembly, control method and device, air conditioner and storage medium

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112146193A (en) * 2019-06-28 2020-12-29 广东美的制冷设备有限公司 Air purification assembly, control method and device, air conditioner and storage medium
CN110772905A (en) * 2019-11-16 2020-02-11 江苏九洲环保技术有限公司 Environment-friendly treatment cleaning device

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