JPH094879A - Method and apparatus for controlling temperature and humidity in constant temperature / humidity space - Google Patents

Method and apparatus for controlling temperature and humidity in constant temperature / humidity space

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Publication number
JPH094879A
JPH094879A JP15438095A JP15438095A JPH094879A JP H094879 A JPH094879 A JP H094879A JP 15438095 A JP15438095 A JP 15438095A JP 15438095 A JP15438095 A JP 15438095A JP H094879 A JPH094879 A JP H094879A
Authority
JP
Japan
Prior art keywords
temperature
reheater
evaporator
humidity
heat
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP15438095A
Other languages
Japanese (ja)
Inventor
Yasuo Nokura
康夫 野倉
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hitachi Astemo Ltd
Original Assignee
Nissin Kogyo Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nissin Kogyo Co Ltd filed Critical Nissin Kogyo Co Ltd
Priority to JP15438095A priority Critical patent/JPH094879A/en
Publication of JPH094879A publication Critical patent/JPH094879A/en
Pending legal-status Critical Current

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Abstract

(57)【要約】 【目的】 温湿度制御装置の蒸発器を冷媒直接膨張式、
予熱器および再熱器を電熱式とし、外気温度が変化して
も、再熱器吐き出し空気温度を一定とする。 【目的】 圧縮機9、凝縮器10、膨張弁11、蒸発器
2を順に流れ、再び圧縮機に戻る冷媒直接膨張式空気冷
却装置の蒸発器における空気系統上下流にそれぞれ熱源
を電気エネルギーとした予熱器1および再熱器4を配置
し、再熱器下流に加湿器18を設備して温湿度を一定に
する温湿度制御装置の蒸発器の空気系統下流における蒸
発器と再熱器との間に蓄熱器3を設け、再熱器の発熱部
を構成する熱保有量以上の熱容量を蓄熱部38に保持せ
しめる。
(57) [Abstract] [Purpose] The evaporator of the temperature and humidity controller is a direct expansion type of refrigerant,
The preheater and reheater are of the electric heating type, and the reheater discharge air temperature is constant even if the outside air temperature changes. [Objective] Electrical energy is used as a heat source upstream and downstream of the air system in the evaporator of the refrigerant direct expansion type air cooling device which flows through the compressor 9, the condenser 10, the expansion valve 11, and the evaporator 2 in order and returns to the compressor again. The preheater 1 and the reheater 4 are arranged, and the humidifier 18 is installed downstream of the reheater to keep the temperature and humidity constant. A heat storage device 3 is provided between the heat storage device 38 and the heat storage device 38 so that the heat storage device 38 holds a heat capacity equal to or more than the amount of heat held in the heat generation part of the reheater.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、電熱式の予熱器および
再熱器で空気を加熱し、冷媒直接膨張式冷却装置で空気
を冷却し、取り入れ空気温湿度の変動により恒温・恒湿
空間の温湿度が変化しないように一定に保持する恒温・
恒湿空間の温湿度制御方法およびその装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention uses an electric heating type preheater and a reheater to heat air and a refrigerant direct expansion type cooling device to cool the air. Constant temperature to keep constant so that the temperature and humidity of the
The present invention relates to a temperature and humidity control method and apparatus for a constant humidity space.

【0002】詳しくは、宇宙開発ロケットの各種制御装
置を設備した空間(フェアリング)の温湿度を冷媒直接
膨張式空気冷却装置と熱源が電気エネルギーの予熱器、
再熱器を用いて制御する恒温・恒湿空間の温湿度制御方
法およびその装置に関する。
[0002] More specifically, the temperature and humidity of a space (fairing) equipped with various control devices of a space rocket are controlled by a refrigerant direct expansion type air cooling device and a heat source of a preheater of electric energy,
The present invention relates to a temperature and humidity control method and device for a constant temperature / constant humidity space that is controlled using a reheater.

【0003】[0003]

【従来の技術】従来、宇宙開発ロケットの各種制御装置
を設備した空間(フェアリング)等は恒温かつ恒湿にす
る必要がある。そして、これら恒温・恒湿空間の温度
は、20℃±0.2〜0.5℃で、相対湿度は、30〜
50%RHの範囲で一定に保持することが要求されてい
る。
2. Description of the Related Art Conventionally, a space (fairing) or the like equipped with various control devices for a space rocket has to be kept at a constant temperature and a constant humidity. And, the temperature of these constant temperature / constant humidity spaces is 20 ° C. ± 0.2 to 0.5 ° C., and the relative humidity is 30 to
It is required to keep constant in the range of 50% RH.

【0004】宇宙開発ロケットに関する恒温・恒湿空間
は、100%新鮮外気を取り入れ、空気系統の上流から
予熱器、蒸発器、再熱器、加湿器の順に並べた温湿度制
御装置により温湿度管理をした再熱器吐き出し空気をフ
ェアリングへ供給している。また、この蒸発器には、冷
媒による直接膨張式のものや、冷温水による熱交換器を
採用したものがあり、再熱器には、電気ヒータを用いた
ものや、温水による熱交換器を採用したものがある。
The constant temperature / humidity space for the space development rocket takes in 100% fresh outside air, and controls the temperature and humidity by a temperature / humidity control device in which a preheater, an evaporator, a reheater and a humidifier are arranged in this order from the upstream of the air system. The reheater discharged air is supplied to the fairing. Some of these evaporators use a direct expansion type using a refrigerant, and some use a heat exchanger using cold / hot water.The reheater uses an electric heater and a heat exchanger using hot water. Some have been adopted.

【0005】そして、この温湿度制御装置による温湿度
の管理方法は、外気温度がフェアリング内温度より高い
場合には、蒸発器で先ず外気を目的とする所定の温度よ
り低く冷却し、その後この低く冷却された空気を再熱器
で加熱して温湿度を管理する。また、外気温度がフェア
リング内温度より低い場合には、予熱器で加熱した後、
さらに再熱器で加熱し、蒸気式または水噴霧式の加湿器
を作動させて再熱器吐き出し空気の温湿度を管理してい
る。
According to the method of controlling temperature and humidity by this temperature and humidity control device, when the outside air temperature is higher than the inside temperature of the fairing, the outside air is first cooled to a temperature lower than the target temperature, and then this temperature is reduced. Temperature and humidity are controlled by heating low-cooled air with a reheater. If the outside air temperature is lower than the fairing temperature, after heating with a preheater,
Furthermore, the temperature and humidity of the air discharged from the reheater are controlled by heating with a reheater and operating a steam or water spray type humidifier.

【0006】[0006]

【発明が解決しようとする課題】従来の温湿度制御装置
の空気系統では、外気の取り入れ側から予熱器、蒸発
器、再熱器、加湿器の順にそれぞれの間の気密を保って
並べ、空気を出口側へ流し、吐き出し空気の温湿度が一
定の値となるように制御している。
In the air system of the conventional temperature / humidity control device, the preheater, the evaporator, the reheater, and the humidifier are arranged in this order from the outside air intake side while maintaining airtightness between them. To the outlet side, and the temperature and humidity of the discharged air are controlled to have a constant value.

【0007】この内、蒸発器を冷温水、再熱器を温水の
熱交換器にしたものでは、恒温・恒湿装置の他に冷温水
設備や温水製造装置等が必要で、設備スペースが大き
く、高価となり、熱容量の大きな温湿度制御装置にしか
適さないという問題点があった。
Among these, in the one in which the evaporator is cold / hot water and the reheater is a hot water heat exchanger, a cold / hot water facility, a hot water producing device, etc. are required in addition to the constant temperature / humidity device, and the equipment space is large. However, there is a problem that it becomes expensive and is suitable only for a temperature / humidity control device having a large heat capacity.

【0008】また、蒸発器を冷媒による直接膨張式と
し、再熱器を電熱ヒータとして取り入れ空気をそれぞれ
冷却したり、加熱するものは、比較的小容量のものに適
し、設備スペースも小さく、かつ安価に製造できる利点
がある。しかし、外気を100%取り入れて出口よりの
吐き出し空気を一定温度に維持し、目的空間に供給する
ため、外気温度が変化すると吐き出し空気温度が瞬時ま
たはしばらくの間、制御ゾーンから外れるという制御上
の問題点があった。
Further, the evaporator is a direct expansion type using a refrigerant, and the reheater is an electric heater for cooling and heating air respectively, which is suitable for a relatively small capacity and requires a small equipment space. There is an advantage that it can be manufactured at low cost. However, since 100% of the outside air is taken in and the exhaled air from the outlet is maintained at a constant temperature and supplied to the target space, when the outside air temperature changes, the exhaled air temperature will be out of the control zone instantaneously or for a while. There was a problem.

【0009】即ち、外気温度が低く変化した場合は、再
熱器吐き出し温度を一定に保つために、蒸発器の作動を
急きょ停止し、予熱器と再熱器とを作動させて取り入れ
空気を加熱する方向に温湿度制御装置を切り換える。こ
の際、再熱器の制御を半導体リレー(SSR)などの制
御精度が優れた制御機器を用いて制御をしても、再熱器
が保有している熱容量のため、再熱器吐き出し空気温度
は短時間の間、急上昇し、再び制御ゾーンに戻る現象が
起きるという問題点があった。
That is, when the outside air temperature changes low, the operation of the evaporator is suddenly stopped and the preheater and the reheater are operated in order to heat the intake air in order to keep the discharge temperature of the reheater constant. Switch the temperature and humidity control device in the direction to At this time, even if the control of the reheater is performed by using a control device such as a semiconductor relay (SSR) having excellent control accuracy, the heat capacity of the reheater causes the reheater discharge air temperature to change. However, there is a problem in that the phenomenon of a rapid rise for a short time and a return to the control zone occurs again.

【0010】さらに、外気温度が高く変化した場合は、
再熱器吐き出し温度を一定に保つために、予熱器の作動
を停止し、蒸発器と再熱器を作動させ再熱器吐き出し温
度を一定に保持する。しかし、これら作動を切り換えた
瞬間に、前記外気温度が低く変化した場合とは逆に、再
熱器吐き出し空気温度が短時間の間、急降下し、再び制
御ゾーンに戻る現象が起きるという制御上の問題点があ
った。
Further, when the outside air temperature changes highly,
In order to keep the reheater discharge temperature constant, the operation of the preheater is stopped and the evaporator and the reheater are operated to keep the reheater discharge temperature constant. However, on the contrary to the case where the outside air temperature changes low at the moment of switching between these operations, the phenomenon that the reheater discharge air temperature suddenly drops for a short time and returns to the control zone again occurs. There was a problem.

【0011】本発明は、温湿度制御装置の蒸発器を冷媒
直接膨張式とし、予熱器および再熱器を電熱式とし、外
気温度が変化しても、再熱器吐き出し空気温度が制御ゾ
ーン内にある恒温・恒湿空間の温湿度制御方法およびそ
の装置を提供することを目的とする。
According to the present invention, the evaporator of the temperature / humidity control device is of the refrigerant direct expansion type, and the preheater and the reheater are of the electric heating type, and even if the outside air temperature changes, the reheater discharge air temperature is within the control zone. It is an object of the present invention to provide a temperature and humidity control method and device for a constant temperature and constant humidity space.

【0012】[0012]

【課題を解決するための手段】前記課題を達成するため
に、本発明の恒温・恒湿空間の温湿度制御方法として
は、圧縮機、凝縮器、膨張弁、蒸発器を順に流れ、再び
圧縮機に戻る冷媒直接膨張式空気冷却装置の蒸発器にお
ける空気系統上下流にそれぞれ熱源を電気エネルギーと
した予熱器および再熱器を配置する。そして、再熱器下
流に加湿器を設備して温湿度を一定にするようにした恒
温・恒湿空間において、前記蒸発器の空気系統下流にお
ける再熱器の熱容量の過不足を蒸発器と再熱器との間の
蓄熱器により補うようになす。
In order to achieve the above-mentioned object, the method of controlling the temperature and humidity of the constant temperature / humidity space according to the present invention is to sequentially flow through a compressor, a condenser, an expansion valve and an evaporator, and then compress again. A preheater and a reheater using heat sources as electric energy are arranged upstream and downstream of the air system in the evaporator of the refrigerant direct expansion type air cooling device returning to the machine. Then, in a constant temperature / humidity space where a humidifier is installed downstream of the reheater to keep the temperature and humidity constant, excess and deficiency of the heat capacity of the reheater downstream of the air system of the evaporator is regenerated with the evaporator. It is designed to be supplemented by a heat storage device between the heat device and the heat storage device.

【0013】そして、本発明の恒温・恒湿空間の温湿度
制御装置としては、圧縮機、凝縮器、膨張弁、蒸発器を
順に流れ、再び圧縮機に戻る冷媒直接膨張式空気冷却装
置の蒸発器における空気系統上下流にそれぞれ熱源を電
気エネルギーとした予熱器および再熱器を配置する。そ
して、再熱器下流に加湿器を設備して温湿度を一定にす
るようにした恒温・恒湿空間において、前記蒸発器の空
気系統下流における蒸発器と再熱器との間に蓄熱器を設
ける。
As the temperature / humidity control device for the constant temperature / constant humidity space of the present invention, the evaporation of the refrigerant direct expansion type air cooling device which flows through the compressor, the condenser, the expansion valve and the evaporator in this order and returns to the compressor again. A preheater and a reheater using heat sources as electric energy are arranged upstream and downstream of the air system. And, in a constant temperature / humidity space in which a humidifier is installed downstream of the reheater to keep the temperature and humidity constant, a heat storage device is provided between the evaporator and the reheater downstream of the air system of the evaporator. Set up.

【0014】この再熱器の発熱部を構成する熱保有量以
上の熱容量をこの蓄熱器の蓄熱部に保持せしめる。
A heat storage capacity of the regenerator is made to hold a heat capacity equal to or more than the amount of heat held in the heat generating section of the reheater.

【0015】また、蓄熱器として、複数の管孔を穿設し
た管板を相対する面に固定した直方体状の枠組ケーシン
グを設け、複数のフィンを貫通して両端を開放した複数
の管をこれら管板間に介在せしめ、各管板の管孔よりそ
れぞれの管端を突出せしめて蓄熱部となす。
Further, as the heat storage unit, a rectangular parallelepiped frame casing having tube plates having a plurality of tube holes fixed to opposite surfaces is provided, and a plurality of tubes having both ends opened through a plurality of fins are provided. It is interposed between the tube plates, and each tube end is projected from the tube hole of each tube plate to form a heat storage part.

【0016】そして、再熱器の発熱部の熱保有量に応じ
てこれら管内を空とするか、またはこれら管内に液体を
注入して両管端をそれぞれ閉塞せしめ、これら管と直交
する空気の流路を構成せしめ、この空気の流路と前記管
板以外の枠組ケーシングに覆いを設ける。
Then, the tubes are emptied according to the amount of heat retained in the heat generating portion of the reheater, or liquid is injected into the tubes to close both ends of the tubes, and the air orthogonal to these tubes is removed. A flow path is formed, and a cover is provided on the air flow path and the frame casing other than the tube sheet.

【0017】[0017]

【作用】取り入れ空気温度は送風機5を通過することに
より、送風機軸動力エネルギー分だけ上昇する。この送
風機5は、再熱器4等の空気系統下流に設けることも可
能であるが、送風機5を通過した空気は軸動力エネルギ
ー分だけ上昇し、制御性の問題から制御の容易な予熱器
の空気系統上流に配置したものである。
The temperature of the intake air passes through the blower 5 and rises by the amount of the blower shaft power energy. This blower 5 can be provided downstream of the air system such as the reheater 4, but the air that has passed through the blower 5 rises by the amount of shaft power energy, and because of the problem of controllability, a preheater that is easy to control is used. It is located upstream of the air system.

【0018】また、宇宙開発ロケットのフェアリング8
へフレキシブルダクト7で送風するようにしたので、送
風機5の電動機動力はフレキシブルダクト7がないもの
に比べ約2倍程度大きくなる。
The space development rocket fairing 8
Since the flexible duct 7 is used to blow air, the motor power of the blower 5 is about twice as large as that without the flexible duct 7.

【0019】予熱器1は電熱式のもので、予熱器1の下
流に設備した温度調節器16により予熱器出口温度を1
8℃に保ち蒸発器2に導く。
The preheater 1 is of an electric heating type, and the temperature controller 16 installed downstream of the preheater 1 adjusts the preheater outlet temperature to 1
Keep at 8 ° C. and lead to evaporator 2.

【0020】この蒸発器2は、冷媒による直接膨張式で
あり、冷媒が蒸発器2、往復動圧縮機9、凝縮器10、
膨張弁11と順に循環して再び蒸発器2に戻る冷媒配管
12を有する。そして、吸入空気温度を一定の範囲で連
続して冷却するもので、空気温度を20℃より低い所定
の温度まで冷却する。
The evaporator 2 is a direct expansion type using a refrigerant, and the refrigerant is the evaporator 2, the reciprocating compressor 9, the condenser 10,
It has a refrigerant pipe 12 which circulates in sequence with the expansion valve 11 and returns to the evaporator 2 again. Then, the intake air temperature is continuously cooled within a certain range, and the air temperature is cooled to a predetermined temperature lower than 20 ° C.

【0021】取り入れ空気温度が一定の範囲内で低下す
ると、往復動圧縮機9は段階的に容量制御(稼働してい
る気筒数を減少)することにより、蒸発器2内の冷媒蒸
発温度を計画した温度に維持する。そして、蒸発器出口
空気温度を取り入れ空気13の温度の如何にかかわら
ず、常に一定に維持するようにする。
When the intake air temperature falls within a certain range, the reciprocating compressor 9 gradually controls the capacity (decreases the number of operating cylinders) to plan the refrigerant evaporation temperature in the evaporator 2. Maintained at the specified temperature. Then, the evaporator outlet air temperature is always kept constant regardless of the temperature of the intake air 13.

【0022】再熱器4は蒸発器2で20℃より低い所定
の温度まで冷却された空気温度を20℃まで加熱し、相
対湿度を30〜50%RHにする。
The reheater 4 heats the temperature of the air cooled to a predetermined temperature lower than 20 ° C. in the evaporator 2 to 20 ° C., and sets the relative humidity to 30 to 50% RH.

【0023】このように、予熱器1により加熱し、蒸発
器2で冷却し、再び再熱器4で加熱するのは、再熱器4
の吐き出し時の湿度を30〜50%RHにするための手
段である。
As described above, the heating by the preheater 1, the cooling by the evaporator 2, and the heating by the reheater 4 again are performed by the reheater 4
Is a means for controlling the humidity at the time of exhalation of 30 to 50% RH.

【0024】目的とする宇宙開発ロケットのフェアリン
グ8に供給する20℃、30〜50%RHの空気の絶対
湿度は大気圧(760mmHg)下では約0.0046〜
0.0077kg/kg(DRY AIR)であり、再
熱器4の吐き出し空気はこの範囲内の絶対湿度でなけれ
ばならない。つまり、蒸発器2の出口空気は4〜11℃
で約95%RHの範囲に制御する必要がある。
The absolute humidity of air at 20 ° C. and 30 to 50% RH supplied to the fairing 8 of the target space development rocket is about 0.0046 to under atmospheric pressure (760 mmHg).
0.0077 kg / kg (DRY AIR), and the air discharged from the reheater 4 must have an absolute humidity within this range. That is, the outlet air of the evaporator 2 is 4 to 11 ° C.
It is necessary to control in the range of about 95% RH.

【0025】この制御においては、予熱器1は、予熱器
1の下流に設備した温度調節器16により予熱器出口空
気温度すなわち蒸発器入口空気温度を18℃に予熱して
いる。また、送風機5の吸込口51近辺に温度スイッチ
15を設け、取入れ空気13の空気温度が9℃またはそ
れ以下になると、往復動圧縮機9を停止せしめ、蒸発器
2の冷却作用を停止する。そして、再熱器4および加湿
器18を作動させて再熱器吐き出し空気温度を20℃、
同湿度を30〜50%RHにする。
In this control, the preheater 1 preheats the preheater outlet air temperature, that is, the evaporator inlet air temperature to 18 ° C. by the temperature controller 16 installed downstream of the preheater 1. Further, the temperature switch 15 is provided near the suction port 51 of the blower 5, and when the air temperature of the intake air 13 becomes 9 ° C. or lower, the reciprocating compressor 9 is stopped and the cooling action of the evaporator 2 is stopped. Then, the reheater 4 and the humidifier 18 are operated to change the reheater discharge air temperature to 20 ° C.,
The humidity is set to 30 to 50% RH.

【0026】また、取り入れ空気13の温度が11℃ま
たはこれ以上になると、温度スイッチ15で往復動圧縮
機9を作動させる。これにより、蒸発器2が作動して、
蒸発器2の冷却作用により、蒸発器2の出口空気温度を
9℃に冷却制御する。
When the temperature of the intake air 13 becomes 11 ° C. or higher, the temperature switch 15 operates the reciprocating compressor 9. As a result, the evaporator 2 operates,
Due to the cooling action of the evaporator 2, the outlet air temperature of the evaporator 2 is controlled to be 9 ° C.

【0027】よって、この蒸発器2では送風機5よりの
取り入れ空気13の温度が一定の範囲で連続して冷却さ
れ、この空気温度が20℃より低い所定の温度まで冷却
される。
Therefore, in the evaporator 2, the temperature of the intake air 13 from the blower 5 is continuously cooled within a fixed range, and the air temperature is cooled to a predetermined temperature lower than 20 ° C.

【0028】取り入れ空気13の温度が一定の範囲内で
低下すると、往復動圧縮機9の吸入側に設けた吸入圧力
検出器19により往復動圧縮機9は稼働している気筒数
を減少して容量制御を行う。このことにより、蒸発器2
内の冷媒蒸発温度を計画した温度に維持し、蒸発器出口
温度を取り入れ空気温度の如何にかかわらず、常に一定
に保持することができる。これは、再熱器4での吐き出
し時の相対湿度を30〜50%RHにするための手段で
ある。
When the temperature of the intake air 13 drops within a certain range, the suction pressure detector 19 provided on the suction side of the reciprocating compressor 9 reduces the number of operating cylinders of the reciprocating compressor 9. Perform capacity control. As a result, the evaporator 2
It is possible to maintain the refrigerant vaporization temperature in the inside at a planned temperature and always keep the evaporator outlet temperature constant regardless of the intake air temperature. This is a means for adjusting the relative humidity at the time of discharge in the reheater 4 to 30 to 50% RH.

【0029】取り入れ空気温度が夏期等の35℃の高い
ところから約10℃まで低下する間は、往復動圧縮機9
の容量制御によりこの圧縮機9上流に設備した吸入圧力
検出器19で冷媒蒸発圧力を常に計画値になるようにす
る。そして、蒸発器出口空気温度を9℃に維持する。
The reciprocating compressor 9 is used while the intake air temperature decreases from a high temperature of 35 ° C. in summer to about 10 ° C.
The suction pressure detector 19 installed upstream of the compressor 9 keeps the refrigerant evaporation pressure at the planned value by the capacity control of the above. Then, the evaporator outlet air temperature is maintained at 9 ° C.

【0030】また、取り入れ空気温度が冬期等の−1℃
の低いときには、蒸発器2は作動せず、温度調節器16
により予熱器1を作動させ、加熱作用により加熱し、そ
の空気温度を18℃に予熱する。そして、再熱器4およ
び加湿器18を作動させて、再熱器4の吐き出し空気1
4の温度を20℃、同湿度を30〜50%RHにする。
In addition, the temperature of the intake air is -1 ° C in winter and the like.
When the temperature is low, the evaporator 2 does not operate and the temperature controller 16
The preheater 1 is actuated by the above to heat by the heating action, and the air temperature thereof is preheated to 18 ° C. Then, the reheater 4 and the humidifier 18 are operated to discharge the air 1 discharged from the reheater 4.
The temperature of 4 is 20 ° C. and the humidity is 30 to 50% RH.

【0031】前記蒸発器出口における9℃の空気温度を
再熱器4の出口で20℃になるように温度調節器17に
より再熱器4を制御する。
The reheater 4 is controlled by the temperature controller 17 so that the air temperature of 9 ° C. at the evaporator outlet becomes 20 ° C. at the outlet of the reheater 4.

【0032】こうして、温度制御幅は20℃±0.2〜
0.5℃で、取り入れ空気温度によって予熱器1と蒸発
器2と再熱器4および加湿器18を作動させ、どのよう
な場合でも再熱器4の吐き出し空気温度20℃、湿度3
0〜50%RHを得る。
In this way, the temperature control width is 20 ° C. ± 0.2 to
At 0.5 ° C., the preheater 1, the evaporator 2, the reheater 4 and the humidifier 18 are operated according to the intake air temperature, and the discharge air temperature of the reheater 4 is 20 ° C. and the humidity is 3 in any case.
0 to 50% RH is obtained.

【0033】しかし、取り入れ空気温度が9℃以下に低
下したとき、蒸発器2の作動が停止し、冷却作用がなく
なるので、再熱器4の吐き出し空気温度は瞬時的に急上
昇する。また、この逆に、取り入れ空気温度が11℃以
上に上昇したとき、蒸発器2が作動して冷却作用が始ま
るので、再熱器4の吐き出し空気温度が瞬時的に急降下
する。
However, when the intake air temperature falls below 9 ° C., the operation of the evaporator 2 is stopped and the cooling action is lost, so the discharge air temperature of the reheater 4 instantaneously rises rapidly. On the contrary, when the intake air temperature rises to 11 ° C. or higher, the evaporator 2 operates and the cooling action starts, so that the discharge air temperature of the reheater 4 suddenly drops suddenly.

【0034】このため、蒸発器2と再熱器4との間に再
熱器4の電熱ヒータの発熱部が保有し得る熱保有量以上
の熱容量を蓄えた蓄熱部38を有する蓄熱器3を設け
る。これより、取り入れ空気温度が9℃以下に低下した
際の再熱器4の吐き出し空気温度の瞬時的上昇と、取り
入れ空気温度が11℃以上に上昇した際の再熱器4の吐
き出し空気温度の瞬時的降下をその吸熱と放熱によって
微少に押え得る。
Therefore, between the evaporator 2 and the reheater 4, the regenerator 3 having the regenerator 4 having the heat storage portion 38 having a heat capacity equal to or more than that of the heat generating portion of the electric heater of the reheater 4 can be retained. Set up. From this, the instantaneous increase in the discharge air temperature of the reheater 4 when the intake air temperature falls below 9 ° C and the discharge air temperature of the reheater 4 when the intake air temperature rises above 11 ° C A momentary drop can be suppressed to a minute by its heat absorption and heat dissipation.

【0035】こうして、計画した外気温度の範囲におい
て、外気温度がどのように変化しても、蓄熱器3は再熱
器4の熱容量の過不足を補うから、再熱器4の吐き出し
空気温度が20℃、相対湿度が30〜50%RHの範囲
で一定に保持できる。
Thus, no matter how the outside air temperature changes within the planned range of the outside air temperature, the regenerator 3 compensates for the excess or deficiency of the heat capacity of the reheater 4, so that the temperature of the air discharged from the reheater 4 is increased. It can be kept constant at 20 ° C. and relative humidity of 30 to 50% RH.

【0036】[0036]

【実施例】以下に、本発明の恒温・恒湿空間の温湿度制
御方法およびその装置の実施の一例を示した添付図面に
基づいて詳細に説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A temperature / humidity control method for a constant temperature / humidity space and an apparatus therefor according to the present invention will be described below in detail with reference to the accompanying drawings.

【0037】図1は蒸発器として冷媒による直接膨張式
空気冷却装置と、予熱器、再熱器に電熱ヒータを用いた
本発明の宇宙開発ロケットのフェアリング等の恒温・恒
湿空間の温湿度制御装置を示すものである。図2は本発
明の蓄熱器を示し、図3は再熱器吐き出し空気温度の変
動が改善されたことを示す本発明の温湿度制御装置の取
り入れ空気温度と送風機、蒸発器、再熱器における出口
温度の時間に対する変動状態の冷却時の線図である。
FIG. 1 shows the temperature and humidity of a constant temperature / constant humidity space such as a fairing of a space rocket of the present invention, which uses a direct expansion type air cooling device using a refrigerant as an evaporator and an electric heater as a preheater and a reheater. It shows a control device. FIG. 2 shows the heat storage device of the present invention, and FIG. 3 shows that the fluctuation of the air temperature of the reheater discharge is improved, and the intake air temperature of the temperature and humidity control device of the present invention and the blower, the evaporator, and the reheater. It is a diagram at the time of cooling of the variation state of the outlet temperature with respect to time.

【0038】本発明の温湿度制御装置は、後述の予熱器
1、蒸発器2、蓄熱器3および再熱器4の順に空気系統
の上流側から各器をケーシング6でそれぞれ気密に連結
し、それぞれの外面に防熱壁を施したものである。
The temperature / humidity control device of the present invention comprises a preheater 1, an evaporator 2, a regenerator 3 and a reheater 4, which will be described later, which are airtightly connected to each other by a casing 6 from the upstream side of the air system. Each outer surface has a heat shield wall.

【0039】予熱器1は、送風機5の吐出側にケーシン
グ6を介して気密に連結したもので、予熱器出口空気温
度、すなわち蒸発器入口空気温度を18℃に制御する電
熱式のものである。これは、予熱器1の下流に設けた温
度調節器16により予熱器1の出口での加熱量を制御し
て、蒸発器入口空気温度を18℃に予熱する。
The preheater 1 is air-tightly connected to the discharge side of the blower 5 via the casing 6, and is of an electric heating type for controlling the preheater outlet air temperature, that is, the evaporator inlet air temperature to 18 ° C. . This is to control the heating amount at the outlet of the preheater 1 by a temperature controller 16 provided downstream of the preheater 1 to preheat the evaporator inlet air temperature to 18 ° C.

【0040】そして、外気温度が18℃より高い場合に
は、予熱器1は作動せず、送風機5を通過した空気は予
熱器1を素通りして蒸発器2に至る。
When the outside air temperature is higher than 18 ° C., the preheater 1 does not operate, and the air passing through the blower 5 passes through the preheater 1 and reaches the evaporator 2.

【0041】蒸発器2は、予熱器1の空気系統下流にケ
ーシング6により気密に連結したもので、冷媒による直
接膨張式であり、冷媒系として蒸発器2、往復動圧縮機
9、凝縮器10および膨張弁11を順に冷媒配管12で
連結したものである。そして、送風機5の吸込口51の
近辺に温度スイッチ15を設け、この温度スイッチ15
と往復動圧縮機9を結線し、取り入れ空気13の温度を
検知せしめ、その温度により往復動圧縮機9を停止させ
たり、始動させたりする。すなわち、その温度が低下し
て温度スイッチ15における設定温度の9℃になると往
復動圧縮機9を停止し、その温度が上昇して同設定温度
の11℃になると往復動圧縮機9を始動するようにした
ものである。
The evaporator 2 is air-tightly connected to the preheater 1 at the downstream side of the air system by a casing 6, and is of a direct expansion type using a refrigerant, and the evaporator 2, the reciprocating compressor 9, and the condenser 10 are used as the refrigerant system. The expansion valve 11 and the expansion valve 11 are sequentially connected by the refrigerant pipe 12. The temperature switch 15 is provided near the suction port 51 of the blower 5, and the temperature switch 15
And the reciprocating compressor 9 are connected to detect the temperature of the intake air 13, and the reciprocating compressor 9 is stopped or started depending on the temperature. That is, the reciprocating compressor 9 is stopped when the temperature decreases to the set temperature of 9 ° C. in the temperature switch 15, and the reciprocating compressor 9 is started when the temperature rises to the same set temperature of 11 ° C. It was done like this.

【0042】蓄熱器3は、蒸発器2の空気系統下流のケ
ーシング6に気密に連結し、後述の再熱器4との間にも
ケーシング6を介して気密に連結し、再熱器4の発熱部
の電熱ヒータが保有し得る熱保有量以上の熱容量を蓄え
た蓄熱部38を有する。蓄熱器3は、図2に示すような
直方体状枠組ケーシング31の相対する面に複数の管孔
を有する管板32を固定したものである。そして、多数
のフィン34を貫通し、両端を開放した複数の管33を
これら管板32間に介在し、これらの管33の管端35
をこれら管板32の複数の管孔より突出し、複数の管3
3の両管端を閉塞して蓄熱部38とする。
The heat accumulator 3 is airtightly connected to the casing 6 downstream of the evaporator 2 from the air system, and is also airtightly connected to the reheater 4 described later through the casing 6 so as to connect the reheater 4 with the reheater 4. It has a heat storage unit 38 that stores a heat capacity that is equal to or larger than the amount of heat that the electric heater of the heat generating unit can hold. The heat storage device 3 is configured by fixing a tube plate 32 having a plurality of tube holes to opposite surfaces of a rectangular parallelepiped frame casing 31 as shown in FIG. Then, a plurality of tubes 33 penetrating a large number of fins 34 and open at both ends are interposed between these tube plates 32, and tube ends 35 of these tubes 33 are provided.
Through the plurality of tube holes of the tube plate 32,
Both pipe ends of 3 are closed to form a heat storage unit 38.

【0043】これら複数の管33と直交する直方体状枠
組ケーシング31の相対する面を空気流路面37とし、
これら相対する管板32と空気流路面37を除く直方体
状枠組ケーシング31の面に覆い36を施したものであ
る。
The opposing surfaces of the rectangular parallelepiped frame casing 31 orthogonal to the plurality of tubes 33 are the air flow passage surfaces 37,
A cover 36 is provided on the surfaces of the rectangular parallelepiped frame casing 31 excluding the tube plate 32 and the air flow path surface 37 which face each other.

【0044】また、この蓄熱器3は複数の管33に多数
のフィン34を設けたもので、後述の再熱器4の発熱部
を構成する個々の材料の比熱と個々の材料の重量の積の
総和で示される熱保有量以上の熱容量を保持せしめたも
のである。さらに、後述の再熱器4の熱容量が大きい場
合は、前記両端を閉塞した複数の管33の管端35を開
き、この管端35から内部に比重の大きな液体、例えば
食塩水などを注入し、その管端35を閉塞する。こうし
て、蓄熱器3の熱容量を増加し得るようにしたものであ
る。
The heat accumulator 3 is provided with a large number of fins 34 on a plurality of tubes 33, and the product of the specific heat of each material and the weight of each material constituting the heat generating portion of the reheater 4 described later. It has a heat capacity equal to or greater than the heat holding amount shown by the sum of. Further, when the heat capacity of the reheater 4 described later is large, the pipe ends 35 of the plurality of pipes 33 whose both ends are closed are opened, and a liquid having a large specific gravity, such as saline, is injected into the inside from the pipe ends 35. , Its tube end 35 is closed. In this way, the heat capacity of the heat storage device 3 can be increased.

【0045】再熱器4は、蓄熱器3の空気系統下流にケ
ーシング6を介して気密に連結したものである。この再
熱器4の発熱部は発熱管の内部に電熱ヒータを介在して
構成した電熱式であり、発熱管の内部にはニクロム線を
配置し、その表面を酸化マグネシウム(MgO)で覆っ
て絶縁したものである。そして、蒸発器2で冷却した空
気を加熱し、再熱器4の吐き出し空気温度を20℃、相
対湿度が30〜50%HRになるようにする。
The reheater 4 is airtightly connected to the heat storage device 3 downstream of the air system via a casing 6. The heat generating portion of the reheater 4 is an electrothermal type in which an electric heater is provided inside the heat generating tube, and a nichrome wire is arranged inside the heat generating tube and its surface is covered with magnesium oxide (MgO). It is insulated. Then, the air cooled by the evaporator 2 is heated so that the temperature of the air discharged from the reheater 4 is 20 ° C. and the relative humidity is 30 to 50% HR.

【0046】フレキシブルダクト7は、基端を再熱器4
の空気系統下流にケーシング6を介して気密に連結した
もので、その先端を宇宙開発ロケットのフェアリング8
に気密に連結したものである。このフレキシブルダクト
7内に温度センサを設備した温度調節器17を設け、再
熱器4の発熱部の電熱ヒータと結線する。また、フレキ
シブルダクト7内に湿度スイッチ20を設け、再熱器4
の出口とフレキシブルダクト7間のケーシング6内に設
けた蒸気式または水噴霧式の加湿器18の電磁弁等18
1とを結線する。そして、温度調節器17と湿度スイッ
チ20は、フレキシブルダクト7内の温度が20℃±
0.2〜0.5℃を保ち、相対湿度が30〜50%HR
なるように、再熱器4および加湿器18を制御するもの
である。
The flexible duct 7 has a base end at the reheater 4
Is airtightly connected to the downstream of the air system of the spacecraft through a casing 6, and its tip is the fairing 8 of the space rocket.
It is connected airtightly. A temperature controller 17 equipped with a temperature sensor is provided in the flexible duct 7 and is connected to the electric heater of the heat generating portion of the reheater 4. Further, the humidity switch 20 is provided in the flexible duct 7 and the reheater 4
Solenoid valve of steam type or water spray type humidifier 18 and the like provided in the casing 6 between the outlet of the outlet and the flexible duct 18
Connect 1 and. The temperature inside the flexible duct 7 of the temperature controller 17 and the humidity switch 20 is 20 ° C. ±
Maintains 0.2-0.5 ° C, relative humidity 30-50% HR
Therefore, the reheater 4 and the humidifier 18 are controlled.

【0047】本発明装置を使用するに当たっては、取り
入れ空気(外気)の温度を温度スイッチ15で検出し、
この温度が11〜35℃の場合は、往復動圧縮機9を運
転して蒸発器2の出口空気温度を9℃まで冷却する。取
り入れ空気温度が11℃に近づくと、吸入圧力検出器1
9により往復動圧縮機9の稼働気筒数を減少して蒸発器
2の出口空気温度が9℃になるように蒸発温度を計画し
た温度に維持する。
In using the device of the present invention, the temperature of the intake air (outside air) is detected by the temperature switch 15,
When this temperature is 11 to 35 ° C, the reciprocating compressor 9 is operated to cool the outlet air temperature of the evaporator 2 to 9 ° C. When the intake air temperature approaches 11 ° C, the suction pressure detector 1
The number of operating cylinders of the reciprocating compressor 9 is reduced by 9 to maintain the evaporation temperature at the planned temperature so that the outlet air temperature of the evaporator 2 becomes 9 ° C.

【0048】また、取り入れ空気(外気)に関係なく予
熱器1を作動させ、蒸発器入口空気温度を18℃に制御
しているから、取り入れ空気温度が−1〜11℃のとき
にも予熱器1は作動しており、蒸発器入口空気温度を1
8℃に制御している。このとき、蒸発器2は冷却作用を
停止しているので、18℃に加熱された空気は、蒸発器
2を素通りして再熱器に至る。そして、これらの間に
も、再熱器4の吐き出し空気14の温度が20℃になる
ように温度調節器17によって再熱器4を制御するもの
である。
Further, since the preheater 1 is operated and the evaporator inlet air temperature is controlled to 18 ° C. regardless of the intake air (outside air), the preheater is also operated when the intake air temperature is −1 to 11 ° C. 1 is operating and the evaporator inlet air temperature is 1
The temperature is controlled at 8 ° C. At this time, since the evaporator 2 has stopped the cooling action, the air heated to 18 ° C. passes straight through the evaporator 2 and reaches the reheater. During this time, the reheater 4 is controlled by the temperature controller 17 so that the temperature of the discharge air 14 of the reheater 4 becomes 20 ° C.

【0049】また、この温度調節器17による制御は、
現実的にはフレキシブルダクト7には熱ロスがあるた
め、温度調節器17はフレキシブルダクト7の下流に設
け、この部分の温度を制御するようにしたものである。
The control by the temperature controller 17 is as follows.
In reality, since the flexible duct 7 has a heat loss, the temperature controller 17 is provided downstream of the flexible duct 7 to control the temperature of this portion.

【0050】次に、本発明を使用することにより、再熱
器4における吐き出し空気14の温度の変動が改善され
る様子について詳説する。この変動が改善される様子を
示した取り入れ空気温度と送風機、蒸発器、再熱器の出
口温度の変動を、横軸を時間とし、縦軸を温度とした線
図である図3に基づいて説明する。
Next, the manner in which the temperature fluctuation of the discharge air 14 in the reheater 4 is improved by using the present invention will be described in detail. Based on FIG. 3, which is a diagram in which the horizontal axis represents time and the vertical axis represents temperature, the fluctuations of the intake air temperature and the outlet temperature of the blower, the evaporator, and the reheater, which show how this fluctuation is improved, are shown. explain.

【0051】本発明の蓄熱器3を装備していない場合に
は、図3の実線で示すように、取り入れ空気13の温度
1 が所定の温度T1-1 まで降下するまで、蒸発器2が
作動して再熱器4の出口空気温度T4 は一定値に制御さ
れている。
When the heat accumulator 3 of the present invention is not provided, as shown by the solid line in FIG. 3, the evaporator 2 is cooled until the temperature T 1 of the intake air 13 drops to a predetermined temperature T 1-1. Is activated and the outlet air temperature T 4 of the reheater 4 is controlled to a constant value.

【0052】時間t1 に取り入れ空気温度T1 がT1-1
になると、往復動圧縮機9は停止して蒸発器2の冷却作
用を停止する。すると、蒸発器2の出口温度T3 は急上
昇して送風機5の出口温度T2 に近づき、時間t2 に温
度T3-2 となり、送風機5の出口温度T2-2 と交わる。
At time t 1 , the intake air temperature T 1 is T 1-1.
Then, the reciprocating compressor 9 is stopped and the cooling action of the evaporator 2 is stopped. Then, the outlet temperature T 3 of the evaporator 2 rapidly rises and approaches the outlet temperature T 2 of the blower 5, reaches the temperature T 3-2 at time t 2 , and intersects with the outlet temperature T 2-2 of the blower 5.

【0053】再熱器4の出口空気温度T4 は時間t2
手前の時間t2'でピークとなる温度T4-2'に達する。や
がて、再熱器4は制御され、時間t3 で再熱器4の出口
空気温度T4-3 がT4 と等しくなり、一定値T4 に戻
る。
[0053] Outlet air temperature T 4 of reheater 4 reaches the 'temperature T 4-2 which is a peak in the' time t 2 before the time t 2. Eventually, reheater 4 is controlled, the outlet air temperature T 4-3 reheater 4 is equal to T 4 at time t 3, the flow returns to a constant value T 4.

【0054】ここで、本発明の蓄熱器3を装備した場合
は、二点鎖線で示すように、時間t 1 から吸熱を始め、
蒸発器2の出口温度T3 は緩やかに上昇し、時間t4
送風機5の出口温度T2-4 に交わる。この蒸発器2にお
ける出口温度T3 の緩やかな上昇のために、再熱器4の
出口空気温度T4 の急上昇はなくなり、再熱器4の出口
空気温度T4 の温度上昇は、時間t2 手前の時間t2"
おけるこの温度T4 より微小上昇した温度T4-2"のみと
なる。
Here, when the heat storage device 3 of the present invention is equipped
Is the time t as indicated by the chain double-dashed line. 1Start absorbing heat from
The outlet temperature T of the evaporator 2ThreeRises slowly and at time tFourso
Blower 5 outlet temperature T2-4Intersect with. In this evaporator 2
Outlet temperature TThreeDue to the gradual rise of
Outlet air temperature TFourNo more soaring, exit of reheater 4
Air temperature TFourTemperature rises at time t2Time t in front2 "To
This temperature T inFourTemperature T slightly increased4-2 "Only
Become.

【0055】この再熱器4における出口温度T4 の、時
間t1 におけるT4-1 からT4-2',T4-3 ,T4-2",T
4-1 で囲まれた面積は、再熱器4の制御時間遅れと、再
熱器4の有する熱容量を示すものである。
The outlet temperature T 4 of the reheater 4 at time t 1 from T 4-1 to T 4-2 ' , T 4-3 , T 4-2 " , T
The area surrounded by 4-1 shows the control time delay of the reheater 4 and the heat capacity of the reheater 4.

【0056】また、蒸発器2における出口温度T3 の、
時間t1 におけるT3-1 からT3-2,T3-4 ,T3-1
囲まれた面積は蓄熱器3の熱容量を示す。
Further, at the outlet temperature T 3 of the evaporator 2,
The area surrounded by T 3-1 to T 3-2 , T 3-4 , and T 3-1 at time t 1 indicates the heat capacity of the heat storage device 3.

【0057】このように、本発明の蓄熱器3を装備した
場合は、再熱器4における出口空気温度T4 の図3の実
線で示す再熱器4の有する熱容量分の変動をなくすこと
ができる。
As described above, when the regenerator 3 of the present invention is equipped, fluctuations in the outlet air temperature T 4 of the reheater 4 corresponding to the heat capacity of the reheater 4 shown by the solid line in FIG. 3 can be eliminated. it can.

【0058】[0058]

【発明の効果】本発明は、恒温・恒湿空間の蒸発器とし
て往復動圧縮機を用いた冷媒直接膨張式とし、予熱器お
よび再熱器を電熱式とし、この蒸発器と再熱器間に蓄熱
器を設けたから、従来の冷媒直接膨張式による欠点をな
くすことができる。
According to the present invention, a refrigerant direct expansion type using a reciprocating compressor is used as an evaporator in a constant temperature / constant humidity space, and a preheater and a reheater are of an electric heating type. Since the heat accumulator is provided in, the disadvantages of the conventional refrigerant direct expansion type can be eliminated.

【0059】すなわち、被冷却物である比熱の小さい空
気を冷却する場合、蒸発器を停止すると冷却作用がなく
なり、蒸発器の出口の空気温度は直ちに上昇する。次
に、再熱器によって加熱するとき、精度が高い温度制御
器を用いても再熱器の吐き出し空気温度が瞬時または一
時的に急上昇する。また、蒸発器を始動させると冷却作
用が始まり、蒸発器を通過した空気の温度は直ちに低下
する。次に、再熱器によって加熱するとき前記精度が高
い温度制御器を用いても再熱器の吐き出し空気温度が瞬
時または一時的に急降下する等の問題点を払拭できる。
That is, when cooling the air having a low specific heat, which is the object to be cooled, when the evaporator is stopped, the cooling action is lost and the air temperature at the outlet of the evaporator immediately rises. Next, when heating by the reheater, the temperature of the air discharged from the reheater suddenly or temporarily increases even if a highly accurate temperature controller is used. Further, when the evaporator is started, the cooling action starts, and the temperature of the air passing through the evaporator immediately drops. Next, when heating with the reheater, even if the temperature controller with high accuracy is used, it is possible to eliminate the problem that the discharge air temperature of the reheater suddenly or temporarily drops.

【0060】つまり、蒸発器と再熱器間に蓄熱器を設け
たから、蒸発器を停止すると冷却作用がなくなっても、
蒸発器出口の空気温度の上昇を蓄熱器の吸熱作用により
防止することができる。また、蒸発器を始動して冷却作
用を始めても、蒸発器出口の空気温度の低下を蓄熱器の
発熱作用により防止することができる。
That is, since the heat accumulator is provided between the evaporator and the reheater, even if the cooling function disappears when the evaporator is stopped,
An increase in the air temperature at the evaporator outlet can be prevented by the heat absorbing action of the heat storage device. Further, even if the evaporator is started to start the cooling action, the decrease in the air temperature at the outlet of the evaporator can be prevented by the heat generating action of the heat accumulator.

【0061】これにより、比較的規模が小さい恒温・恒
湿装置を作製する場合に、冷温水設備や温水製造装置の
ような大がかりな付帯設備が不要で、設備空間が小さ
く、かつ安価に、性能の高い温湿度制御装置を提供する
ことができる。
As a result, in the case of producing a thermostat / humidity device having a relatively small scale, large-scale auxiliary equipment such as cold / hot water equipment and hot water production equipment is not required, the equipment space is small, and the performance is low. It is possible to provide a high temperature and humidity controller.

【図面の簡単な説明】[Brief description of drawings]

【図1】蒸発器として冷媒による直接膨張式空気冷却装
置と余熱器、再熱器に電熱ヒータを用いた本発明の宇宙
開発ロケットのフェアリング等の恒温・恒湿空間の温湿
度制御装置の系統図である。
FIG. 1 shows a temperature / humidity control device for a constant temperature / constant humidity space such as a fairing of a space rocket according to the present invention, which uses a direct expansion type air cooling device using a refrigerant as an evaporator and a reheater, and an electric heater as a reheater. It is a system diagram.

【図2】本発明に使用する蓄熱器の一例を示す斜視図で
ある。
FIG. 2 is a perspective view showing an example of a heat storage device used in the present invention.

【図3】再熱器吐き出し空気温度の変動が改善されたこ
とを示す本発明の温湿度制御装置の取り入れ空気温度と
送風機、蒸発器、再熱器の各出口温度の時間に対する変
動状態の冷却時の線図である。
[Fig. 3] Fig. 3 is a graph showing that the fluctuation of the air temperature discharged from the reheater is improved, and the fluctuation of the intake air temperature of the temperature / humidity control device of the present invention and the outlet temperatures of the blower, the evaporator, and the reheater with respect to time It is a diagram of time.

【符号の説明】[Explanation of symbols]

1 予熱器 2 蒸発器 3 蓄熱器 31 枠組ケーシング 32 管板 33 管 34 フィン 35 管端 36 覆い 37 流路 38 蓄熱部 4 再熱器 5 送風機 51 吸込口 6 ケーシング 7 フレキシブルダクト 8 フェアリング 9 圧縮機 10 凝縮器 11 膨張弁 12 冷媒配管 13 取り入れ空気(外気) 14 再熱器吐き出し空気 15 温度スイッチ 16,17 温度調節器 18 加湿器 181 電磁弁等 19 吸入圧力検出器 20 湿度スイッチ 1 Preheater 2 Evaporator 3 Heat accumulator 31 Framework casing 32 Tube plate 33 Tube 34 Fin 35 Tube end 36 Cover 37 Flow path 38 Heat storage section 4 Reheater 5 Blower 51 Suction port 6 Casing 7 Flexible duct 8 Fairing 9 Compressor 10 Condenser 11 Expansion Valve 12 Refrigerant Pipe 13 Intake Air (Outside Air) 14 Reheater Exhaust Air 15 Temperature Switch 16, 17 Temperature Controller 18 Humidifier 181 Solenoid Valve 19 Intake Pressure Detector 20 Humidity Switch

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 圧縮機、凝縮器、膨張弁、蒸発器を順に
流れ、再び圧縮機に戻る冷媒直接膨張式空気冷却装置の
蒸発器における空気系統上下流にそれぞれ熱源を電気エ
ネルギーとした予熱器および再熱器を配置し、再熱器下
流に加湿器を設備して温湿度を一定にするようにした恒
温・恒湿空間において、前記蒸発器の空気系統下流にお
ける再熱器の熱容量の過不足を蒸発器と再熱器との間の
蓄熱器により補うようになしたことを特徴とする恒温・
恒湿空間の温湿度制御方法。
1. A preheater in which an electric energy is used as a heat source upstream and downstream of an air system in an evaporator of a refrigerant direct expansion air cooling device which flows through a compressor, a condenser, an expansion valve, and an evaporator in order, and then returns to the compressor. In a constant temperature / humidity space in which a reheater is installed and a humidifier is installed downstream of the reheater to keep the temperature and humidity constant, the heat capacity of the reheater over the air system downstream of the evaporator is exceeded. A constant temperature characterized in that the shortage was made up by a heat storage device between the evaporator and the reheater.
Temperature and humidity control method for constant humidity space.
【請求項2】 圧縮機、凝縮器、膨張弁、蒸発器を順に
流れ、再び圧縮機に戻る冷媒直接膨張式空気冷却装置の
蒸発器における空気系統上下流にそれぞれ熱源を電気エ
ネルギーとした予熱器および再熱器を配置し、再熱器下
流に加湿器を設備して温湿度を一定にするようにした恒
温・恒湿空間において、前記蒸発器の空気系統下流にお
ける蒸発器と再熱器との間に蓄熱器を設け、再熱器の発
熱部を構成する熱保有量以上の熱容量をこの蓄熱器の蓄
熱部に保持せしめたことを特徴とする恒温・恒湿空間の
温湿度制御装置。
2. A preheater in which an electric energy is used as a heat source upstream and downstream of the air system in the evaporator of the refrigerant direct expansion type air cooling device which flows through the compressor, the condenser, the expansion valve, and the evaporator in order, and then returns to the compressor. In a constant temperature / humidity space in which a reheater is arranged and a humidifier is installed downstream of the reheater to keep the temperature and humidity constant, an evaporator and a reheater downstream of the evaporator in the air system A temperature / humidity control device for a constant temperature / humidity space characterized in that a heat storage device is provided between the heat storage device and a heat storage unit of the reheater, which has a heat capacity equal to or more than the heat storage amount, is held in the heat storage unit of the heat storage device.
【請求項3】 複数の管孔を穿設した管板を相対する面
に固定した直方体状の枠組ケーシングを設け、複数のフ
ィンを貫通して両端を開放した複数の管をこれら管板間
に介在せしめ、各管板の管孔よりそれぞれの管端を突出
せしめて蓄熱部となし、再熱器の発熱部の熱保有量に応
じてこれら管内を空とするか、またはこれら管内に液体
を注入して両管端をそれぞれ閉塞せしめ、これらの管と
直交する空気の流路を構成せしめ、この空気の流路と前
記管板以外の枠組ケーシングに覆いを設けて蓄熱器とな
したことを特徴とする請求項2記載の恒温・恒湿空間の
温湿度制御装置。
3. A rectangular parallelepiped frame casing in which tube plates having a plurality of tube holes are fixed to opposite surfaces, and a plurality of tubes having both ends opened through a plurality of fins are provided between the tube plates. By interposing them, each tube end is projected from the tube hole of each tube sheet to form a heat storage section, and these tubes are emptied or liquid is stored in these tubes depending on the amount of heat retained in the heat generation section of the reheater. By injecting and blocking both pipe ends respectively, an air flow passage orthogonal to these pipes was formed, and a cover was provided on the air flow passage and the frame casing other than the pipe sheet to form a heat storage device. The temperature / humidity control device for a constant temperature / constant humidity space according to claim 2.
JP15438095A 1995-06-21 1995-06-21 Method and apparatus for controlling temperature and humidity in constant temperature / humidity space Pending JPH094879A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15438095A JPH094879A (en) 1995-06-21 1995-06-21 Method and apparatus for controlling temperature and humidity in constant temperature / humidity space

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15438095A JPH094879A (en) 1995-06-21 1995-06-21 Method and apparatus for controlling temperature and humidity in constant temperature / humidity space

Publications (1)

Publication Number Publication Date
JPH094879A true JPH094879A (en) 1997-01-10

Family

ID=15582887

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15438095A Pending JPH094879A (en) 1995-06-21 1995-06-21 Method and apparatus for controlling temperature and humidity in constant temperature / humidity space

Country Status (1)

Country Link
JP (1) JPH094879A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006234293A (en) * 2005-02-25 2006-09-07 Taikisha Ltd Heat pump type cooling device, air conditioner using the same, and heat pump type heating device
JP2007309572A (en) * 2006-05-18 2007-11-29 Kandenko Co Ltd Constant temperature and humidity air conditioner and temperature control method for the air conditioner
JP2009198141A (en) * 2008-02-25 2009-09-03 Nippon Spindle Mfg Co Ltd Heat exchange apparatus
CN104577771A (en) * 2015-01-29 2015-04-29 国家电网公司 Constant-temperature constant-humidity control crucible for intelligent substations
CN106091207A (en) * 2016-08-05 2016-11-09 上海湿腾电器有限公司 A kind of wine cellar constant temperature and humidity machine
CN107023993A (en) * 2017-05-22 2017-08-08 吉林省电力科学研究院有限公司 A kind of electric heat storage boiler of high-efficiency environment friendly solid

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006234293A (en) * 2005-02-25 2006-09-07 Taikisha Ltd Heat pump type cooling device, air conditioner using the same, and heat pump type heating device
JP2007309572A (en) * 2006-05-18 2007-11-29 Kandenko Co Ltd Constant temperature and humidity air conditioner and temperature control method for the air conditioner
JP2009198141A (en) * 2008-02-25 2009-09-03 Nippon Spindle Mfg Co Ltd Heat exchange apparatus
CN104577771A (en) * 2015-01-29 2015-04-29 国家电网公司 Constant-temperature constant-humidity control crucible for intelligent substations
CN106091207A (en) * 2016-08-05 2016-11-09 上海湿腾电器有限公司 A kind of wine cellar constant temperature and humidity machine
CN107023993A (en) * 2017-05-22 2017-08-08 吉林省电力科学研究院有限公司 A kind of electric heat storage boiler of high-efficiency environment friendly solid
CN107023993B (en) * 2017-05-22 2023-03-24 吉林省电力科学研究院有限公司 High-efficient environmental protection solid electricity heat accumulation boiler

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