JP3519380B2 - Environmental test equipment with downflow cooler - Google Patents

Environmental test equipment with downflow cooler

Info

Publication number
JP3519380B2
JP3519380B2 JP2001183471A JP2001183471A JP3519380B2 JP 3519380 B2 JP3519380 B2 JP 3519380B2 JP 2001183471 A JP2001183471 A JP 2001183471A JP 2001183471 A JP2001183471 A JP 2001183471A JP 3519380 B2 JP3519380 B2 JP 3519380B2
Authority
JP
Japan
Prior art keywords
cooler
circulating air
humidifier
flow path
humidity
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP2001183471A
Other languages
Japanese (ja)
Other versions
JP2002372293A (en
Inventor
知久 柴田
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.)
Espec Corp
Original Assignee
Espec Corp
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Filing date
Publication date
Application filed by Espec Corp filed Critical Espec Corp
Priority to JP2001183471A priority Critical patent/JP3519380B2/en
Publication of JP2002372293A publication Critical patent/JP2002372293A/en
Application granted granted Critical
Publication of JP3519380B2 publication Critical patent/JP3519380B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、冷凍機を構成する
蒸発器を冷却器として備えると共に水蒸気加湿式の加湿
器を備え前記冷却器で冷却された循環空気を前記水蒸気
で加湿するようにした環境試験装置に関し、特に高温高
湿条件を持つ装置において熱的性能の向上と冷凍機及び
加湿器の小型化技術に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention comprises an evaporator constituting a refrigerator as a cooler and a steam humidifier humidifier so that the circulating air cooled by the cooler is humidified by the steam. The present invention relates to an environmental test device, and more particularly to improvement of thermal performance and miniaturization of a refrigerator and a humidifier in a device having high temperature and high humidity conditions.

【0002】[0002]

【従来の技術】環境試験装置では、高温高湿条件から低
温低湿条件まで試験されるべき広範囲の温湿度条件に対
応可能にすると共に大きな冷却能力を持たせるため、通
常冷却及び除湿機能を持つ冷凍機の蒸発器を冷却器とし
て使用している。一方、例えば半導体のような電気電子
部品等からなる試料では、高温高湿環境の下に動作状態
で試験されることがよくある。このときには試料が発熱
負荷となる。又、冷却されるべき負荷はあるが除湿され
るべき負荷の発生はない。
2. Description of the Related Art An environment tester is capable of handling a wide range of temperature and humidity conditions to be tested from high temperature and high humidity conditions to low temperature and low humidity conditions, and has a large cooling capacity. The evaporator of the machine is used as a cooler. On the other hand, a sample including an electric / electronic component such as a semiconductor is often tested in an operating state under a high temperature and high humidity environment. At this time, the sample becomes a heat load. Further, there is a load to be cooled but no load to be dehumidified.

【0003】ところが、高温高湿空気を冷凍機で冷却し
ようとすると、不必要な除湿が行われ、それを補うため
の再加湿が必要になり、これらの現象によって無駄なエ
ネルギー消費が発生すると共に、高温高湿専用の環境試
験装置では、冷凍機や加湿器が大きくなり装置コストも
高くなるという問題がある。
However, when the high-temperature and high-humidity air is cooled by the refrigerator, unnecessary dehumidification is performed, and re-humidification is necessary to make up for it, which causes wasteful energy consumption. However, in the environment test device dedicated to high temperature and high humidity, there is a problem that the refrigerator and the humidifier are large and the device cost is high.

【0004】この場合、本来の蒸気発生式の加湿器に加
えて、加湿機能と共に潜熱冷却機能も持たせるように、
循環空気中に微小水滴を噴霧混入させる超音波式の補助
加湿器を設けて、上記のような試験条件に対処させるよ
うにした装置も知られている。
In this case, in addition to the original steam generating type humidifier, a humidifying function and a latent heat cooling function are provided.
An apparatus is also known in which an ultrasonic auxiliary humidifier that sprays and mixes minute water droplets into the circulating air is provided to deal with the above test conditions.

【0005】しかしながら、補助加湿器を設けることは
動作機器の追加になり、装置構成が複雑化すると共に、
その運転台数の選択や主加湿器との併用や切換タイミン
グの時期等の運転条件の選択が難しいという問題があ
る。
However, the provision of the auxiliary humidifier results in the addition of operating equipment, which complicates the apparatus configuration and
There is a problem that it is difficult to select the number of operating units, combined use with the main humidifier, and operating conditions such as switching timing.

【0006】一方、環境試験装置では、例えば図7に示
す如く、試験室6と隣接させて空調室8を設け、これら
の室の間で温度及び湿度の調節された試験用の空気を循
環させるようにしていて、蒸発器からなる冷却器2は空
調室8に配置され、循環空気が冷却器2の下方側から上
方側に流される上昇流型の循環系になっている(例えば
特開平11−141955号公報参照)。
On the other hand, in the environmental test apparatus, as shown in FIG. 7, for example, an air-conditioning room 8 is provided adjacent to the test room 6, and test air whose temperature and humidity are adjusted is circulated between these rooms. In this way, the cooler 2 composed of the evaporator is arranged in the air-conditioning chamber 8 to form an ascending flow type circulation system in which the circulating air flows from the lower side to the upper side of the cooler 2 (for example, Japanese Patent Laid-Open Publication No. H11-111). (See JP-A-141955).

【0007】[0007]

【発明が解決しようとする課題】このような従来の冷却
器部上昇流型の循環系を備えた環境試験装置は、冷却器
で除湿した水分負荷を冷却器の上流側まで持ち込まず、
冷凍機の除湿機能を重視した低湿運転用に特に適した装
置である。ところが、高温高湿で冷却を必要とする運転
条件がある場合には、冷却器で冷却時に凝縮して落下し
た水分が循環空気によって再蒸発して冷却器に持ち込ま
れたり、この水分負荷が含まれるため冷却器で過大な除
湿が行われ、再加湿量も多くなり、このような点も冷却
及び加湿エネルギーを増大させている要因であることが
判明した。
The conventional environmental testing apparatus having such a cooler section upflow circulation system does not bring the moisture load dehumidified by the cooler to the upstream side of the cooler.
This is a device particularly suitable for low-humidity operation that places importance on the dehumidifying function of the refrigerator. However, when there are operating conditions that require cooling at high temperature and high humidity, the water that has condensed and dropped during cooling in the cooler is re-evaporated by the circulating air and brought into the cooler, and this water load is included. Therefore, it was found that excessive dehumidification was performed in the cooler and the amount of re-humidification also increased, and this point was also a factor that increased cooling and humidification energy.

【0008】そこで本発明は、従来技術における上記問
題を解決し、簡単な構成の下に、高温高湿運転条件での
冷却器の除湿作用を適正化して、運転時の消費エネルギ
ーを減少させ、冷凍機及び加湿器の小形化も可能な環境
試験装置を提供することを課題とする。
Therefore, the present invention solves the above problems in the prior art, optimizes the dehumidifying action of the cooler under high temperature and high humidity operating conditions with a simple structure, and reduces energy consumption during operation, An object of the present invention is to provide an environmental testing device that can also downsize a refrigerator and a humidifier.

【0009】[0009]

【課題を解決するための手段】 本発明は上記課
題を解決するために、請求項1の発明は、冷凍機を構成
する蒸発器を冷却器として備えると共に水蒸気加湿式の
加湿器を備え前記冷却器で冷却された循環空気を前記水
蒸気で加湿するようにした環境試験装置において、前記
循環空気を前記冷却器の上方から下方に通過可能にする
下降流経路と、該下降流経路を反転させて上向きにした
部分と、前記反転させる位置に前記冷却器から出された
結露水を前記循環空気と接触させるように設けられた布
や多孔質材料からなる水分回収ガイドと、を有すること
を特徴とする。
Means for Solving the Problems In order to solve the above-mentioned problems, the present invention according to claim 1 is provided with an evaporator constituting a refrigerator as a cooler and a steam humidifier humidifier. In an environmental test device configured to humidify circulating air cooled in a cooler with the steam, a downward flow path that allows the circulating air to pass from above the cooler to a lower side, and the downward flow path is reversed. Turned up
Part and out of the cooler in the inverted position
A cloth provided to bring the condensed water into contact with the circulating air.
And a moisture recovery guide made of a porous material .

【0010】請求項2の発明は、冷凍機を構成する蒸発
器を冷却器として備えると共に水蒸気加湿式の加湿器を
備え前記冷却器で冷却された循環空気を前記水蒸気で加
湿するようにした環境試験装置において、前記循環空気
を前記冷却器の上方から下方に通過可能にする下降流経
路と、前記循環空気を前記冷却器の下方から上方に通過
可能にする上昇流経路を有し、該上昇流経路と前記下
降流経路とを切換可能にするダンパを設けたことを特徴
とする。
The invention according to claim 2 is an evaporator which constitutes a refrigerator.
Equipped with a steam generator as a cooler and a steam humidifier
The circulating air cooled by the cooler is added by the steam.
In an environmental testing device that is adapted to be moistened, the circulating air
Downward flow which enables the passage of the cooling water from above the cooler to below.
And wherein the road, the circulating air and a rising flow path to allow passage from below to above the cooler, that the said descending flow path and the upward flow path provided a damper that allows switching To do.

【0011】請求項3の発明は、冷凍機を構成する蒸発
器を冷却器として備えると共に水蒸気加湿式の加湿器を
備え前記冷却器で冷却された循環空気を前記水蒸気で加
湿するようにした環境試験装置において、前記循環空気
を前記冷却器の上方から下方に通過可能にする下降流経
路と、前記下降流経路の下流側に設けられた下流側冷却
器と、該下流側冷却器の下方から上方に前記循環空気を
通過可能にする上昇流経路と、を有することを特徴とす
る。
The invention of claim 3 is an evaporator which constitutes a refrigerator.
Equipped with a steam generator as a cooler and a steam humidifier
The circulating air cooled by the cooler is added by the steam.
In an environmental testing device that is adapted to be moistened, the circulating air
Downward flow which enables the passage of the cooling water from above the cooler to below.
A passage, a downstream cooler provided on the downstream side of the downward flow path, and an upward flow path that allows the circulating air to pass from below to above the downstream cooler. .

【0012】[0012]

【発明の実施の形態】図1は本発明の下降流経路を有す
る構造を適用した環境試験装置の全体構成の一例示す。
本例の環境試験装置は、冷凍機1を構成する蒸発器を冷
却器2として備えると共に加湿器3を備えていて、冷却
器2で冷却された循環空気を加湿器3で加湿ノズル31
から水蒸気を放出して加湿するようにした装置であり、
循環空気を冷却器2の上方から下方に通過可能にする下
降流経路を有する構造として、図において矢印で示すよ
うに、本例では専用の下向き風路4が配設された構造に
なっている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT FIG. 1 has a downflow path of the present invention.
1 shows an example of the overall configuration of an environmental testing device to which the structure described above is applied.
The environment test apparatus of this example includes an evaporator constituting the refrigerator 1 as a cooler 2 and a humidifier 3, and the circulating air cooled by the cooler 2 is humidified by the humidifier 3 with a humidifying nozzle 31.
It is a device that humidifies by releasing water vapor from
As a structure having a downward flow path that allows circulating air to pass from above the cooler 2 to below, in the present example, a dedicated downward air passage 4 is provided as shown by the arrow in the figure. .

【0013】この環境試験装置は、通常の構成部分とし
て、断熱壁5、試験室6、仕切板7で試験室6に隣接し
て配置された空調室8、前記冷却器2等と共にその中に
配置された加熱器9、送風機10、温度及び湿度センサ
11、12、温度及び湿度の設定部13を備えその一部
分のみを図示している操作制御盤14、等を備えてい
る。冷却器2には、圧縮機や凝縮機や電子膨張弁等を備
えた図示しない冷凍回路から例えば−20℃程度の温度
の冷媒が供給される。
This environmental testing device includes, as usual components, an insulating wall 5, a test chamber 6, an air conditioning chamber 8 arranged adjacent to the test chamber 6 by a partition plate 7, the cooler 2 and the like. It is provided with a heater 9, a blower 10, temperature and humidity sensors 11 and 12, an operation control panel 14 which is provided with a temperature and humidity setting unit 13 and only a part of which is illustrated, and the like. Refrigerant having a temperature of, for example, about −20 ° C. is supplied to the cooler 2 from a refrigerating circuit (not shown) including a compressor, a condenser, an electronic expansion valve, and the like.

【0014】以上のような環境試験装置は次のように運
転されその作用効果を発揮する。試験室6に発熱負荷を
発生させる電気電子部品等の試料Wが入れられ、冷凍機
1、加湿器3、加熱器9、送風機10等が運転され、試
験すべき温度ts及び相対湿度φs(以下単に「湿度」
という)が操作制御盤14の設定部13で設定される
と、温度及び湿度センサ11、12で循環空気の実際の
温度tp及び湿度φpを検出しつつ、検出値が設定値に
なるように機器類が制御され、目的とするts及びφs
の空気が循環されて試料Wに供給される。
The above-mentioned environmental test device is operated in the following manner and exhibits its effects. A sample W such as an electric / electronic component that generates a heat load is placed in the test chamber 6, the refrigerator 1, the humidifier 3, the heater 9, the blower 10 and the like are operated, and the temperature ts to be tested and the relative humidity φs (hereinafter Simply "humidity"
Is set by the setting unit 13 of the operation control panel 14, the temperature and humidity sensors 11 and 12 detect the actual temperature tp and the humidity φp of the circulating air, and the detected value becomes the set value. Controlled ts and φs
Is circulated and supplied to the sample W.

【0015】このような運転において、循環空気を高温
高湿条件にすると共に、試料Wに駆動電源を与えてこれ
を作動させる試験を行うと、試料Wが空調機器に対して
発熱負荷を与えることになるが、そのような運転条件の
ときでも、本発明を適用した本例の装置によれば、従来
の装置よりも、冷凍機の能力を低くして加湿器の加湿量
を減らした省エネ運転をすることができる。
In such an operation, when the circulating air is subjected to a high temperature and high humidity condition and a test is performed in which a driving power source is applied to the sample W to operate it, the sample W gives a heat generation load to the air conditioner. However, even under such operating conditions, according to the device of the present example to which the present invention is applied, energy-saving operation in which the capacity of the refrigerator is reduced and the humidification amount of the humidifier is reduced compared to the conventional device. You can

【0016】即ち、冷凍機の蒸発器を使用した冷却器2
では、単なる顕熱除去だけをすることはできず不可避的
に除湿作用も行われるが、本例の装置によれば、試験室
6で試料Wの発熱負荷が加えられて温度上昇して同じ絶
対温度の下に相対湿度の下がった循環空気が、そのまま
の状態で冷却器2に流入するので、冷却器2では、従来
の装置で冷却器の入口側において冷却器に追加されてい
た除湿負荷がないため、冷却器の除湿量が減少すると共
に、除湿され重力の作用で下方に落下している凝縮水の
一部分が冷却器2の後流側で循環空気に加わって搬送さ
れるので、従来の装置とは反対にこの水分が加湿用に利
用可能になり、加湿器3による再加湿のための蒸気量を
減少させることができる。その結果、冷却器及び加湿器
の発生能力を低減させて、装置の小形化を可能にすると
共に運転時の省エネ化を図ることができる。
That is, the cooler 2 using the evaporator of the refrigerator
However, the sensible heat cannot be simply removed and the dehumidifying action is inevitably performed. However, according to the apparatus of this example, the heating load of the sample W is applied in the test chamber 6 and the temperature rises to the same absolute value. Since the circulating air whose relative humidity has dropped below the temperature flows into the cooler 2 as it is, in the cooler 2, the dehumidifying load added to the cooler at the inlet side of the cooler in the conventional device is applied. Since the amount of dehumidification of the cooler is reduced, part of the condensed water that is dehumidified and drops downward due to the action of gravity is added to the circulating air on the downstream side of the cooler 2 and conveyed, so Contrary to the device, this moisture is made available for humidification and the amount of steam for re-humidification by the humidifier 3 can be reduced. As a result, it is possible to reduce the generation capacity of the cooler and the humidifier, enable downsizing of the device, and save energy during operation.

【0017】図2は、本例の装置及び従来の装置におけ
る循環空気の状態変化を湿り空気線図の一部分に示した
図である。図3及び図8は、それぞれの冷却器で除湿さ
れた水分と空気流れの状態を模式的に示している。これ
らの図により、本発明の上記作用効果について、具体的
数値例を挙げて従来の装置と対比しつつ更に詳しく説明
する。
FIG. 2 is a diagram showing a part of a moist air diagram showing changes in the state of circulating air in the apparatus of this example and the conventional apparatus. 3 and 8 schematically show the states of the moisture dehumidified by the respective coolers and the air flow. With reference to these drawings, the above-described effects of the present invention will be described in more detail by giving a concrete numerical example and comparing with a conventional device.

【0018】設定部13では、例えばts=t1 =60
℃、φs=φ1 =95%の高温高湿条件が与えられ、こ
の条件の循環空気が試験室入口状態として送風機によ
って試験室6に送り出され、試料Wに当てられる。図2
の湿り空気線図上にこのの位置を示している。試料W
が通電されると、その発熱によって循環空気が例えば1
0℃温度上昇し、それによって相対湿度が下がり、循環
空気はt2 =70℃、φ2 =約52%の試験室出口状態
になり、試験室6から排出される。からの間では
水分負荷の出入りがないので、絶対湿度xは一定であ
る。従って、はから絶対湿度一定で温度が10℃高
くなった位置になっている。
In the setting unit 13, for example, ts = t 1 = 60
High-temperature and high-humidity conditions of ° C and φs = φ 1 = 95% are given, and the circulating air under these conditions is blown out to the test chamber 6 by the blower as a test chamber inlet state and applied to the sample W. Figure 2
This position is shown on the moist air diagram of. Sample W
When the power is supplied to the
The temperature rises by 0 ° C., the relative humidity decreases, and the circulating air is discharged from the test chamber 6 at the test chamber outlet state of t 2 = 70 ° C. and φ 2 = about 52%. Since there is no moisture load in and out between and, the absolute humidity x is constant. Therefore, the temperature is 10 ° C. higher with a constant absolute humidity.

【0019】本発明を適用した冷却器部循環空気下降流
型の図1に示す装置では、図2において実線で示す如
く、循環空気は、上記の位置からそのままの状態で直
ちに冷却、除湿され、高温低湿冷却線Aに従った状態変
化をして冷却器出口状態に至る。このとき、図3に示
す如く、冷却器2で冷却されその冷却管やフィンに付着
した凝縮水滴や空気中で凝縮してある程度の大きさにな
った微小水滴からなる水滴pは、重力で落下すると共に
矢印で示す循環空気流れの搬送力により、冷却器2から
その下方で且つ下流側に送り出される。
In the cooler section circulating air downflow type apparatus shown in FIG. 1 to which the present invention is applied, the circulating air is immediately cooled and dehumidified as it is from the above position, as indicated by the solid line in FIG. The state changes according to the high-temperature and low-humidity cooling line A to reach the cooler outlet state. At this time, as shown in FIG. 3, the condensed water droplets cooled by the cooler 2 and attached to the cooling pipes or fins thereof or the water droplets p formed by minute water droplets condensed in the air and having a certain size fall by gravity. At the same time, it is sent out from the cooler 2 to the lower side and the downstream side by the carrying force of the circulating air flow indicated by the arrow.

【0020】冷凍機の蒸発器からなる冷却器における上
記高温低湿冷却線Aのような状態変化線の方向は、潜熱
負荷と顕熱負荷の比率によって定まる。即ち、湿度が低
く相対的に潜熱負荷が小さければ、顕熱負荷が取れやす
く、従って温度が下がりやすく、湿り空気線図上では傾
斜の緩くなる方向に状態変化をする傾向になり、反対に
湿度が高くなると、傾斜が大きくなる傾向になる。そし
て、この状態変化は、ほぼ、変化の開始点から図示の飽
和線Lに接線を引く方向になることが一般に知られてい
る。この場合、前記高温低湿冷却線Aは、の初期位置
から変化するので、湿度が下がっていてある程度傾斜の
緩くなった線になる。そしてこの線上での位置が定ま
る。なお、線Lは図において下方に次第に傾斜が小さく
なる曲線である。
The direction of the state change line such as the high temperature and low humidity cooling line A in the cooler composed of the evaporator of the refrigerator is determined by the ratio of the latent heat load and the sensible heat load. That is, if the humidity is low and the latent heat load is relatively small, the sensible heat load is easy to take, and therefore the temperature is likely to drop, and there is a tendency for the state to change in the direction of a gentle slope on the wet air diagram, and conversely Is higher, the inclination tends to be larger. It is generally known that this state change is almost in the direction of drawing a tangent line to the illustrated saturation line L from the start point of the change. In this case, since the high-temperature low-humidity cooling line A changes from the initial position of, the line becomes a line with a moderate inclination and a slight inclination. And the position on this line is decided. It should be noted that the line L is a curve in which the inclination gradually decreases downward in the figure.

【0021】循環空気が冷却器2でからまで状態変
化をすると、上記の如く、この間に冷却・除湿され、絶
対湿度及びエンタルピがxa及びha低下する。このう
ち絶対湿度の低下分xaは、循環空気が含有していた水
蒸気が部分的に冷却されて凝縮し、水滴となって冷却器
2から排出された0分量である。
When the circulating air changes its state from the cooler 2 to the cooler 2, as described above, it is cooled and dehumidified, and the absolute humidity and the enthalpy decrease by xa and ha. Of these, the amount of decrease in absolute humidity xa is the amount of 0 minutes discharged from the cooler 2 as water droplets, where water vapor contained in the circulating air is partially cooled and condensed.

【0022】この場合、図1の装置によれば、前述の如
く、冷却器2から下方に重力で落下した上記水分が循環
空気中に混入し、その水分の一部分で特に小径で軽量な
水分が循環空気と共に搬送されることになる。この付加
される水分は循環空気と同じ温度になっていて、搬送さ
れる間に循環空気と熱交換して再蒸発するとすれば、循
環空気は、冷却器出口状態から、絶対湿度及び相対湿
度が大きくなると共に温度が下がり、中間状態に到達
する。この状態変化は、熱の出入りがないので、エンタ
ルピ一定、即ちh4 =h3 の下で、x4 及びφ4 がx3
及びφ3 より大きくなってt4 がt3 より小さくなる変
化である。
In this case, according to the apparatus of FIG. 1, as described above, the above-mentioned water content dropped by gravity from the cooler 2 is mixed into the circulating air, and a part of the water content is particularly small in diameter and lightweight. It will be transported with the circulating air. If the added water has the same temperature as the circulating air and exchanges heat with the circulating air during transport to re-evaporate, the circulating air will have an absolute humidity and a relative humidity from the cooler outlet state. As the temperature increases, the temperature decreases and the intermediate state is reached. This state change, since there is no out of heat, enthalpy constant, i.e. h 4 = under h 3, x 4 and phi 4 are x 3
And φ 3 and t 4 become smaller than t 3 .

【0023】このからの変化により、循環空気に対
する水分冷却効果と中間加湿効果とが生じ、冷却器2に
おける冷却のための除湿が中断される形になり、後述す
るように冷却器での冷却量及び加湿器での再加湿量が減
少することになる。
Due to the change from this, a moisture cooling effect and an intermediate humidifying effect on the circulating air are generated, and dehumidification for cooling in the cooler 2 is interrupted, so that the cooling amount in the cooler will be described later. Also, the amount of re-humidification in the humidifier will be reduced.

【0024】中間状態から、加湿器3の加湿ノズル3
1で循環空気に水蒸気が加えられると、循環空気の温度
及び湿度は、最終状態であり且つ最初の試験室入口状態
に再調整される。この場合、加湿器3では通常100
℃で内部エネルギーu=640kcal/kg の熱量を持つ飽
和水蒸気を発生させるので、この蒸気が循環空気に水分
負荷を与えると共にこれを再加熱し、の状態の循環空
気をの状態に至らしめる。前記循環空気中に随伴され
た水分は、この加湿水蒸気の過熱度によって最終的に6
0℃の水蒸気となり、加湿水蒸気と共にの湿度状態を
実現させることになる。
From the intermediate state, the humidifying nozzle 3 of the humidifier 3
When steam is added to the circulating air at 1, the temperature and humidity of the circulating air is readjusted to the final state and to the initial chamber inlet state. In this case, the humidifier 3 is usually 100
Since saturated steam having a calorific value of internal energy u = 640 kcal / kg at ℃ is generated, this steam imposes a moisture load on the circulating air and reheats it, so that the circulating air in the state of is brought to the state of. The amount of water entrained in the circulating air is finally 6 due to the superheat of the humidified steam.
The water vapor becomes 0 ° C., and the humidity condition together with the humidified water vapor is realized.

【0025】の状態をの状態にするまでの加湿兼再
加熱変化線Bは、一定量で一定の温湿度条件Xを持つ循
環空気に対して、u=640の水蒸気を加える量を変化
させ、循環空気を最終状態に至らしめるときの状態X
の変化を示す曲線であり、の位置と加湿蒸気条件であ
る前記u=640の水蒸気条件とによって定まり、か
ら一定の向きとして、湿り空気線図上のU=640の線
Mに平行な傾斜を持った線である。従って、この曲線B
は、の状態から、湿度及び温度を下げて行く傾向の線
であり、その方向は定まっている。
The change line B for humidifying and reheating until the state of is changed to the state of changing the amount of water vapor of u = 640 added to the circulating air having the constant temperature and humidity condition X at a constant amount. State X when circulating air reaches the final state
Is determined by the position of and the steam condition of u = 640, which is a humidified steam condition, and a slope parallel to the line M of U = 640 on the moist air diagram is taken as a constant direction from It is the line I have. Therefore, this curve B
Is a line that tends to decrease the humidity and temperature from the state of, and its direction is fixed.

【0026】以上により、の位置は高温低湿冷却線A
上になること、の位置はから等エンタルピ線上で随
伴水分量によって定まること、換言すればからまで
の線は方向及び長さが定まっていること、及び、曲線B
は点からの方向が定まっていることが明らかになった
ので、曲線A上での位置を動かし、線分−をスラ
イドさせ、の位置が曲線B上に乗ると、の位置が決
定することになる。その結果、−−−−の循
環空気のすべて状態が確定する。
From the above, the position of is the high temperature low humidity cooling line A
The position of being up is determined by the amount of associated water on the isenthalpic line from, that is, the line from to is of fixed direction and length, and the curve B
Since it became clear that the direction from the point is fixed, move the position on the curve A, slide the line segment-, and if the position of is on the curve B, the position of will be decided. Become. As a result, all the states of the circulating air of ----- are established.

【0027】なお、曲線Aは本来的には冷却のための線
であるから温度を下げる方向に変化し、曲線Bは温度の
高い水蒸気で加湿するための線であるから温度を上げる
方向に変化するので、曲線AとBとは互いに接近する方
向に向いた線になっている。従って、線分−の大き
さを問わず、の点は必ず存在する点である。
Since the curve A is originally a line for cooling, it changes in the direction of lowering the temperature, and the curve B is a line for humidifying with steam having a high temperature, so it changes in the direction of increasing temperature. Therefore, the curves A and B are lines oriented in a direction toward each other. Therefore, the point is always present regardless of the size of the line segment.

【0028】このように定められる及びの状態の具
体例を示すためには、線分−に相当する冷却器出口
の水分搬送取込み量を推定する必要がある。この水分
は、循環空気がの条件のときには、これまでの実際の
装置における種々の計測や計算結果から、絶対湿度の
0.3%程度、即ちΔx=3g/kg´(乾燥空気)だ
け絶対湿度を上昇させる程度の量と推定される。
In order to show a concrete example of the above-defined conditions and, it is necessary to estimate the amount of water taken in at the outlet of the cooler corresponding to the line segment. When the circulating air is in the condition of, the moisture content is about 0.3% of the absolute humidity, that is, Δx = 3 g / kg '(dry air), from the various measurement and calculation results in the actual device so far. It is estimated to be an amount that raises.

【0029】このようにして決定された各点から、冷却
器2の冷却熱量及び加湿器3の加湿熱量を計算すると次
のとおりである: 各部のエンタルピ(kcal/ kg) 試験室入口状態 ; 104.0 同出口状態 ; 107.5 冷却器入口状態 ; 107.5 冷却器出口状態 ; 96.5 加湿器入口状態 ; 96.5 加湿器出口状態 ; 103.0 (試験室入口状態) 冷却器2の冷却熱量ha = −=107.5−96.5=11 加湿器3の加湿熱量hb = −=104.0−96.5=7.5 これに対して、図7に示す従来の装置では、循環空気
は、試験室入口状態から出口状態までは本例の装置
と同じ図2の実線で示すように推移するが、冷却器2の
入口側である下方位置に到達すると、図8に示す如く、
冷却器2で除湿されて落下してくる水滴pと接触する。
このとき、試料の発熱によって循環空気が昇温している
ので、水滴の一部分が再蒸発して冷却器2に持ち込ま
れ、その除湿負荷を大きくする。
From the points thus determined, the cooling heat quantity of the cooler 2 and the humidification heat quantity of the humidifier 3 are calculated as follows: Enthalpy of each part (kcal / kg) Test chamber inlet state; .0 Same outlet state; 107.5 Cooler inlet state; 107.5 Cooler outlet state; 96.5 Humidifier inlet state; 96.5 Humidifier outlet state; 103.0 (Test chamber inlet state) Cooler 2 Cooling heat quantity ha =-= 107.5-96.5 = 11 Humidification heat quantity hb of humidifier 3 =-= 104.0-96.5 = 7.5 On the other hand, in the conventional device shown in FIG. The circulating air changes from the inlet state to the outlet state of the test chamber as shown by the solid line in FIG. 2, which is the same as in the apparatus of this example, but when it reaches the lower position on the inlet side of the cooler 2, it is shown in FIG. as,
The water drops p that are dehumidified by the cooler 2 and fall are brought into contact.
At this time, since the circulating air is heated by the heat of the sample, a part of the water droplets is re-evaporated and brought into the cooler 2 to increase the dehumidifying load.

【0030】このときの水滴の蒸発は、循環空気自体の
保有熱によって起こるので、等エンタルピ下で行われ
る。又、このときの水滴の蒸発による循環空気の絶対湿
度の上昇は、条件は相違するが図1の装置での冷却器出
口側のときとほぼ同じでΔx´=3g/kg´と推定さ
れる。その結果、循環空気は、図2でから´のよう
に余分の状態変化をしてから冷却器2に入ることにな
る。
Since the evaporation of water drops at this time is caused by the heat retained by the circulating air itself, it is carried out under isoenthalpy. Further, the increase in absolute humidity of the circulating air due to the evaporation of water droplets at this time is almost the same as that at the cooler outlet side in the apparatus of FIG. 1 though the conditions are different, and it is estimated that Δx ′ = 3 g / kg ′. . As a result, the circulating air enters the cooler 2 after undergoing an extra state change as indicated by 'in FIG.

【0031】冷却器2内では、実線の高温低湿冷却線A
と類似の状態変化をするが、変化前の状態が相違するた
め、即ち、´の状態はの状態よりも温度が下がり湿
度が高くなっていので、線Aに較べて、潜熱負荷が大き
く顕熱負荷が取れ難い傾向の線になる。そして、湿り空
気線図上で線Aより傾斜の大きい線である低温高湿冷却
線Cに従って変化し、冷却器出口状態´に至る。線C
も線Aと同様に飽和線Lに接線を引く方向になってい
る。
In the cooler 2, the solid high temperature and low humidity cooling line A
Although the state change is similar to, but the state before change is different, that is, since the temperature is lower and the humidity is higher in the state of ′ than in the state of ′, the latent heat load is larger and the sensible heat is larger than that of line A. It becomes a line that tends to be difficult to take the load. Then, the temperature changes according to the low-temperature high-humidity cooling line C, which is a line having a larger inclination than the line A on the moist air diagram, and reaches the cooler outlet state '. Line C
Similarly to the line A, the tangent line is drawn to the saturation line L.

【0032】冷却器2から排出される循環空気は、上方
に向いて流れるため、今度は図1の装置のように落下す
る凝縮水滴を水分負荷として追加することができず、直
ちに加湿器3で加湿されることになる。即ち、実線のよ
うにからの中間状態への変化が存在しない。その結
果、凝縮水滴を利用した加湿及び冷却効果が得られず、
冷却器2における冷却のための除湿量が大きくなり、そ
れによる再加湿量も多くなる。そして、加湿器3では、
実線の場合と同様に、循環空気は´からの方向に延
びる加湿兼再加熱変化線Bに乗っての目的とする初期
状態に到達するが、加湿のための熱量が多くなってい
る。
Since the circulating air discharged from the cooler 2 flows upward, it is not possible to add the condensing water droplets which fall like the device of FIG. 1 as a moisture load, and the humidifier 3 immediately starts. It will be humidified. That is, there is no change from to the intermediate state as shown by the solid line. As a result, the humidifying and cooling effects using condensed water droplets cannot be obtained,
The amount of dehumidification for cooling in the cooler 2 increases, and the amount of re-humidification increases accordingly. And in the humidifier 3,
As in the case of the solid line, the circulating air reaches the desired initial state on the humidifying and reheating change line B extending in the direction from ', but the amount of heat for humidification is large.

【0033】以上のような図7の従来の装置における冷
却器2の冷却熱量及び加湿器3の加湿熱量を計算すると
次のとおりである: 各部のエンタルピ(kcal/ kg) 試験室入口状態 ; 104.0 同出口状態 ; 107.5 冷却器入口状態 ´; 107.5 冷却器出口状態 ´; 91.8 加湿器入口状態 ´; 91.8 加湿器出口状態 ; 103.0 (試験室入口状態) 冷却器2の冷却熱量 = ´−´=107.5−91.8=15.7 加湿器3の加湿熱量 = −´=104.0−91.8=12.2 この従来の装置の結果を本発明を適用した本例の装置の
前記結果と比較すると次のとおりである: 従来の装置 本発明の装置 差 省エネ率 冷却器2の冷却熱量 = 15.7 11 4.7 30 % 加湿器3の加湿熱量 = 12.2 7.5 4.7 39 % 合計 27.9 18.5 9.4 34 % 以上の如く、本発明を適用すれば、冷却器で発生した凝
縮水を湿り空気線図上の特性と組み合わせて利用するこ
とにより、環境試験装置の運転において大幅な省エネ化
が図られると共に、冷却器及び加湿器の最大能力がこの
ように高温高湿条件下の発熱負荷の発生という運転条件
で定まる場合には、冷凍機と冷却器及び加湿器の容量を
下げて装置のコスト低減を図ることができる。
Calculation of the cooling heat amount of the cooler 2 and the humidification heat amount of the humidifier 3 in the conventional apparatus shown in FIG. 7 is as follows: Enthalpy of each part (kcal / kg) test chamber inlet state; .0 Same outlet state; 107.5 Cooler inlet state '; 107.5 Cooler outlet state'; 91.8 Humidifier inlet state '; 91.8 Humidifier outlet state; 103.0 (Test chamber inlet state) Cooling heat quantity of cooler 2 = '-' = 107.5-91.8 = 15.7 Humidification heat quantity of humidifier 3 =-'= 104.0-91.8 = 12.2 The result of this conventional device is It is as follows when compared with the above result of the apparatus of this example to which the present invention is applied: Conventional apparatus Apparatus of the present invention Energy saving rate Cooling heat amount of cooler 2 = 15.7 11 4.7 30% Humidification of humidifier 3 Heat quantity = 12.2 7.5 4.7 39% Total 27.9 8.5 9.4 34% As described above, if the present invention is applied, by using the condensed water generated in the cooler in combination with the characteristics on the moist air diagram, it is possible to significantly reduce energy consumption in the operation of the environmental test device. If the maximum capacity of the cooler and the humidifier is determined by the operating conditions such as the generation of heat load under high temperature and high humidity conditions, reduce the capacity of the refrigerator, the cooler and the humidifier, and The cost can be reduced.

【0034】なお、これまでの説明から明らかなよう
に、本発明の装置と従来の装置との消費エネルギーの差
は、共に3g/kg´とした前記Δx及びΔx´の値
と、の位置及びΔx´によって変化した´の位置の
差に基づく図2の冷却除湿線A、Bの傾斜角によって異
なってくる。この場合、例えば図1の装置のように、冷
却器の出口風路の下向き長さが長く、結露水が搬送され
やすいような装置では、Δxが大きくなり、省エネ効果
が大きくなる。又、後述するように図4(a)の装置で
水分回収ガイド41を設ければ、Δxが大きくなって同
様に省エネ効果が大きくなる。
As is clear from the above description, the difference in energy consumption between the device of the present invention and the conventional device is 3 g / kg ', and the values of Δx and Δx' are It depends on the inclination angle of the cooling / dehumidifying lines A and B in FIG. 2 based on the difference in the position of ′ changed by Δx ′. In this case, for example, in a device such as the device shown in FIG. 1 in which the downward air length of the outlet air passage of the cooler is long and condensed water is easily transported, Δx becomes large and the energy saving effect becomes large. Further, as will be described later, if the water recovery guide 41 is provided in the apparatus of FIG. 4A, Δx becomes large and the energy saving effect becomes large as well.

【0035】図4(a)は本発明を適用した環境試験装
置の例を示す。この装置では、下降流径路である下向
き風路4を装置の下方位置に設け、反転させて上向きに
した部分まで延設している。これにより、従来の通常の
環境試験装置と同様に、循環空気を試験室6内に上方か
ら吹き出せるようにしている。この反転式の下向き風路
4では、布や適当な多孔質材料からなる図示のような水
分回収ガイド41を設けている。そのようにすれば、水
分回収ガイド41の表面に結露水を滞留させ、これを効
率良く循環空気と接触させることができる。その結果、
水分の再加湿化及び水分気化による冷却効果を促進し、
省エネ効果を一層向上させることができる。又、風の流
れを円滑にし、流れ抵抗を減少させることができる。
FIG. 4 (a) shows an example of an environment test apparatus to which the present invention is applied. In this device, a downward air passage 4 which is a downward flow path is provided at a lower position of the device, and is extended up to a reversed and upward portion. As a result, the circulating air can be blown into the test chamber 6 from above, as in the case of the conventional normal environment testing device. The inversion-type downward air passage 4 is provided with a water recovery guide 41 as shown, which is made of cloth or a suitable porous material . By doing so, the dew condensation water can be retained on the surface of the water content recovery guide 41 and efficiently contacted with the circulating air. as a result,
Promotes the cooling effect by re-humidification of water and vaporization of water,
The energy saving effect can be further improved. Also, the flow of wind can be made smooth and the flow resistance can be reduced.

【0036】図4(b)は本発明を適用した環境試験装
置の他の例を示す。この装置は、図1の装置の下向き風
路4に加えて、循環空気を冷却器2の下方から上方に通
過可能にする上昇流径路として図において二点鎖線で示
す上向き風路15を有し、この上向き風路15と前記下
向き風路4とを切換可能にするダンパ16、17を設け
た構造にしている。このダンパ16、17は、通常、手
動又は遠隔手動で操作されるが、温湿度サイクル試験を
行うような装置では自動操作される。
FIG . 4 (b) shows an environmental test equipment to which the present invention is applied.
Another example of the arrangement will be shown. This equipment, in addition to the downward air passage 4 of the device of FIG. 1, have the upward air path 15 indicated by the two-dot chain line in FIG circulating air upflow paths to allow passage from below of the cooler 2 above However, a structure is provided in which dampers 16 and 17 for switching the upward air passage 15 and the downward air passage 4 are provided. The dampers 16 and 17 are usually manually or remotely operated, but are automatically operated in an apparatus for performing a temperature / humidity cycle test.

【0037】本例の装置では、高湿運転時には、ダンパ
16、17をそれぞれ実線の位置にして、下向き径路4
を開通させる。これにより、これまで説明した省エネ運
転を行うことができる。一方、低湿運転条件では、ダン
パ16、17をそれぞれ二点鎖線の位置にして、上向き
風路15を開通させる。これにより、冷却器2で除湿し
た後の循環空気中への水分負荷の持ち込みがなくなり、
加湿器3による加湿制御によって確実に低湿条件を保持
できることになる。
In the apparatus of this example, the dampers 16 and 17 are set to the positions indicated by the solid lines during the high humidity operation, and the downward path 4 is
To open. As a result, the energy saving operation described above can be performed. On the other hand, under the low-humidity operating condition, the dampers 16 and 17 are respectively set to the positions indicated by the two-dot chain line to open the upward air passage 15. As a result, no moisture load is brought into the circulating air after dehumidifying with the cooler 2,
The humidification control by the humidifier 3 ensures that the low humidity condition can be maintained.

【0038】図5は本発明を適用した環境試験装置の空
調装置部分の更に他の例を示す。本例の空調装置部分
は、下向き風路4及び上向き風路15を備えていて、こ
れらが4枚のダンパ18〜21で切り換え可能なように
構成されている。本例の空調装置部分は、例えば環境試
験装置の試験室の上又は下に配設される。これらのダン
パも、手動、遠隔手動又は自動で操作される。
FIG. 5 shows still another example of the air conditioner portion of the environment test apparatus to which the present invention is applied. The air conditioner portion of this example includes a downward air passage 4 and an upward air passage 15, which are configured to be switchable by four dampers 18 to 21. The air conditioner portion of the present example is disposed, for example, above or below the test chamber of the environmental test device. These dampers are also manually, remotely or manually operated.

【0039】本例の装置では、高湿運転時には、ダンパ
18、21が開きダンパ19、20が閉まり,実線の矢
印で示す下向き風路4が開通する。又、低湿運転時に
は、図示していないがダンパ18、21が閉まりダンパ
19、20が開き,二点鎖線の矢印で示す上向き風路1
5が開通する。そして図5の装置と同様に、高湿条件で
は省エネ運転ができ、低湿条件では確実にこれを制御で
きる。
In the apparatus of this embodiment, during high humidity operation, the dampers 18 and 21 are opened, the dampers 19 and 20 are closed, and the downward air passage 4 indicated by the solid arrow is opened. Further, at the time of low humidity operation, although not shown, the dampers 18 and 21 are closed and the dampers 19 and 20 are opened, and the upward air passage 1 indicated by the two-dot chain line arrow.
5 opens. As in the device of FIG. 5, energy saving operation can be performed under high humidity conditions, and this can be reliably controlled under low humidity conditions.

【0040】図6は本発明を適用した環境試験装置の更
に他の例を示す。本例の装置は、図2の装置に加えて、
下向き風路4の下流側に設けられた下流側冷却器2
2 と、この冷却器22 の下方から上方に循環空気を通過
可能にする上昇流経路として上向き専用風路22とを有
する。この装置では、図2の装置の冷却器2は冷却器2
1 として設けられている。
FIG. 6 shows still another example of the environment test apparatus to which the present invention is applied. The device of this example is in addition to the device of FIG.
Downstream cooler 2 provided downstream of the downward air passage 4
2, and a upward-only air duct 22 upflow path that can pass through the circulating air from the bottom to the top of the cooler 2 2. In this device, the cooler 2 of the device of FIG.
It is provided as 1 .

【0041】本例の装置によれば、高湿運転時には、冷
却器21 を使用して省エネ効果が得られるようにし、中
間湿度又は低湿度運転時には、冷却器22 を使用して湿
度制御性を確保し、湿度制御をしない運転時には、両方
の冷却器21 及び22 を使用して冷却面積の大きい冷却
器として有効に利用することができる。本例の装置で
は、冷却器台数が1台追加になるが、ダンパのような動
作部品が不要になる。
According to the apparatus of this example, the energy saving effect is obtained by using the cooler 2 1 during the high humidity operation, and the humidity control is performed by using the cooler 2 2 during the intermediate or low humidity operation. It is possible to effectively utilize as a cooler having a large cooling area by using both coolers 2 1 and 2 2 during the operation that secures the property and does not control the humidity. In the device of this example, the number of coolers is increased by one, but operating parts such as dampers are unnecessary.

【0042】[0042]

【発明の効果】以上の如く本発明によれば、環境試験装
置が、冷凍機を構成する蒸発器からなる冷却器の上方か
ら下方に循環空気を通過可能にする下降流経路を有し、
冷却器で冷却された循環空気を加湿器の水蒸気で加湿す
るように構成されているので、高湿度条件の循環空気を
冷却するときに、冷却器で凝縮し重力で滴下する水分と
同じ方向に循環空気が流れるため、循環空気が水分を再
蒸発させて冷却器に持ち込んで冷却器における除湿負荷
を増加させることがない。
As described above , according to the present invention, the environment test apparatus has the downward flow path that allows the circulating air to pass from the upper side to the lower side of the cooler composed of the evaporator constituting the refrigerator,
Since the circulating air cooled by the cooler is humidified by the steam of the humidifier, when cooling the circulating air under high humidity conditions, it is condensed in the cooler in the same direction as the water dropped by gravity. Since the circulating air flows, the circulating air does not re-evaporate water and bring it into the cooler to increase the dehumidification load in the cooler.

【0043】又、循環空気が冷却器を出た後には、冷却
器から落下する凝縮水の一部分を取り込んで再蒸発さ
せ、循環空気に加湿と冷却効果を付与することができ
る。そして、循環空気を効果的に顕熱冷却し、冷却器で
の冷却のための除湿量を減少させ、冷却器で不可避的に
過大除湿された循環空気を再加湿するための加湿量も低
減させることができる。
Further, after the circulating air exits the cooler, a part of the condensed water falling from the cooler can be taken in and re-evaporated to give the circulating air a humidifying and cooling effect. Then, the circulating air is effectively sensible cooled, the dehumidifying amount for cooling in the cooler is reduced, and the humidifying amount for rehumidifying the circulating air that is inevitably excessively dehumidified in the cooler is also reduced. be able to.

【0044】その結果、通常電力からなる冷却器用冷凍
機の駆動エネルギーを減少させると共に、加湿のための
エネルギー消費量減少させることができる。従って、
請求項1の発明によれば、冷却器で発生した凝縮水を湿
り空気線図上の特性と組み合わせて利用することによ
り、環境試験装置の運転において大幅な省エネ化を図る
ことができる。又、冷却器とこれを含む冷凍機及び加湿
器の容量を下げて、装置コストを低減させることが可能
になる。そして請求項1の発明においては、上記の基本
的効果に加えて、所定の構成を備えた水分回収ガイドを
設けるので、結露水を循環空気と接触させて水分の再加
湿化及び水分気化による冷却効果を促進し、省エネ効果
を一層向上させることができる。又、風の流れを円滑に
し、流れ抵抗を減少させることができる。
[0044] As a result, reduces the driving energy of the cooler refrigerator comprising a normal power, it is possible to reduce the energy consumption for humidification. Therefore,
According to the first aspect of the present invention, by using the condensed water generated in the cooler in combination with the characteristics on the wet air diagram, it is possible to significantly save energy in the operation of the environmental test device. In addition, the capacity of the cooler and the refrigerator and the humidifier including the cooler can be reduced to reduce the device cost. In the invention of claim 1, the above basic
In addition to the mechanical effect, a moisture recovery guide with a predetermined configuration is provided.
Since it is provided, the condensed water is brought into contact with the circulating air to re-add moisture.
Energy-saving effect by promoting the cooling effect by humidification and moisture vaporization
Can be further improved. In addition, smooth the flow of wind
However, the flow resistance can be reduced.

【0045】請求項2の発明においては、前記の基本的
効果に加えて、循環空気を冷却器の下方から上方に通過
可能にする上昇流経路を設け、この経路と下降流経路と
を切換可能にするダンパを設けるので、高湿運転時には
下降流径路を開通させることにより、上記の省エネ運転
効果が得られ、一方、中間湿度又は低湿度運転条件で
は、ダンパによって上昇流径路を開通させ、冷却器を出
た後の循環空気内への凝縮水の持ち込みを解消すること
により、加湿器3による加湿制御によって中低湿条件を
確実に実現することができる。
According to the invention of claim 2, the above-mentioned basic
In addition to the effect , an ascending flow path that allows the circulating air to pass from the lower side to the upper side of the cooler is provided, and a damper that allows switching between this path and the descending flow path is provided. The above energy-saving operation effect can be obtained by opening the valve.On the other hand, under intermediate or low humidity operating conditions, the damper opens the upward flow path and brings the condensed water into the circulating air after exiting the cooler. By eliminating the above, it is possible to surely realize the middle and low humidity conditions by the humidification control by the humidifier 3.

【0046】請求項3の発明においては、前記の基本的
効果に加えて、下降流経路の下流側に下流側冷却器を設
け、その下方から上方に循環空気を通過可能にする上昇
流経路を設けるので、高湿運転時には下降流径路の冷却
器を使用して省エネ効果が得られ、中間湿度又は低湿度
運転時には下流側冷却器と上昇流径路とを使用して湿度
制御性を確保し、湿度制御が不要な運転時には、下降流
径路及び上昇流径路の両方の冷却器を使用し、これらを
冷却面積の大きい冷却器として有効に利用することがで
きる。この場合、冷却器台数が1台追加になるが、上記
ダンパが不要になって動作部品数を減らすことができ
る。
According to the invention of claim 3, the above-mentioned basic
In addition to the effect , a downstream cooler is installed on the downstream side of the downward flow path, and an upward flow path that allows circulating air to pass through from below is provided, so a cooler in the downward flow path is used during high humidity operation. Energy saving effect is obtained, the humidity controllability is secured by using the downstream side cooler and the upflow path during the operation with intermediate humidity or low humidity, and the downflow path and the upflow path are provided during the operation without the humidity control. It is possible to use both of the above coolers and effectively use them as a cooler having a large cooling area. In this case, the number of coolers is increased by one, but the damper is not necessary and the number of operating parts can be reduced.

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

【図1】本発明を適用した環境試験装置の全体構成の一
例を示す説明図である。
FIG. 1 is an explanatory diagram showing an example of the overall configuration of an environment test apparatus to which the present invention has been applied.

【図2】上記装置の高温高湿運転時の循環空気の状態を
湿り空気線図に示した説明図である。
FIG. 2 is an explanatory diagram showing a state of circulating air during high-temperature and high-humidity operation of the above apparatus, in a moist air diagram.

【図3】冷却器で生成した凝縮水の落下する状態と循環
空気の流れ方向を示した説明図である。
FIG. 3 is an explanatory diagram showing a state in which condensed water generated by a cooler falls and a flow direction of circulating air.

【図4】(a)及び(b)は本発明を適用した環境試験
装置の他の例を示す説明図である。
4A and 4B are explanatory views showing another example of the environment test apparatus to which the present invention is applied.

【図5】本発明を適用した環境試験装置の空調機器部分
の更に他の例を示す説明図である。
FIG. 5 is an explanatory diagram showing still another example of the air conditioner portion of the environment test apparatus to which the present invention is applied.

【図6】本発明を適用した環境試験装置の更に他の例を
示す説明図である。
FIG. 6 is an explanatory diagram showing still another example of the environment test apparatus to which the present invention is applied.

【図7】従来の環境試験装置の全体構成の一例を示す説
明図である。
FIG. 7 is an explanatory diagram showing an example of the overall configuration of a conventional environment test apparatus.

【図8】上記装置において冷却器で生成した凝縮水の落
下する状態と循環空気の流れ方向を示した説明図であ
る。
FIG. 8 is an explanatory diagram showing a state in which condensed water generated by a cooler in the above apparatus falls and a flow direction of circulating air.

【符号の説明】[Explanation of symbols]

1 冷凍機 2 冷却器 3 加湿器 4 下向き風路(下降流径路) 15 上向き風路(上昇流経路) 16〜21 ダンパ 22 上向き専用風路(上昇流径路) 1 refrigerator 2 cooler 3 humidifier 4 Downward air path (downward flow path) 15 Upward wind path (upflow path) 16-21 damper 22 Upward dedicated wind path (upstream flow path)

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 冷凍機を構成する蒸発器を冷却器として
備えると共に水蒸気加湿式の加湿器を備え前記冷却器で
冷却された循環空気を前記水蒸気で加湿するようにした
環境試験装置において、 前記循環空気を前記冷却器の上方から下方に通過可能に
する下降流経路と、該下降流経路を反転させて上向きに
した部分と、前記反転させる位置に前記冷却器から出さ
れた結露水を前記循環空気と接触させるように設けられ
た布や多孔質材料からなる水分回収ガイドと、を有する
ことを特徴とする環境試験装置。
1. An environmental test apparatus comprising an evaporator constituting a refrigerator as a cooler and a steam humidifier humidifier to humidify the circulating air cooled by the cooler with the steam. A downward flow path that allows circulating air to pass downward from above the cooler, and an upward direction by reversing the downward flow path.
The part that has been
Is provided to bring the condensed water that has formed into contact with the circulating air.
And a moisture recovery guide made of a porous material, and an environmental testing device.
【請求項2】 冷凍機を構成する蒸発器を冷却器として
備えると共に水蒸気加湿式の加湿器を備え前記冷却器で
冷却された循環空気を前記水蒸気で加湿するようにした
環境試験装置において、 前記循環空気を前記冷却器の上方から下方に通過可能に
する下降流経路と、 前記循環空気を前記冷却器の下方か
ら上方に通過可能にする上昇流経路を有し、該上昇流
経路と前記下降流経路とを切換可能にするダンパを設け
たことを特徴とする環境試験装置。
2. An evaporator constituting a refrigerator as a cooler
In addition to being equipped with a steam humidifier humidifier
The cooled circulating air was humidified with the steam.
In the environmental testing device, the circulating air can pass from above the cooler to below
A downward flow path for, the circulating air and a rising flow path to allow passage from below to above the cooler, to the said descending flow path and the upward flow path provided a damper that allows switching Environmental testing equipment characterized by.
【請求項3】 冷凍機を構成する蒸発器を冷却器として
備えると共に水蒸気加湿式の加湿器を備え前記冷却器で
冷却された循環空気を前記水蒸気で加湿するようにした
環境試験装置において、 前記循環空気を前記冷却器の上方から下方に通過可能に
する下降流経路と、 前記下降流経路の下流側に設けられ
た下流側冷却器と、該下流側冷却器の下方から上方に前
記循環空気を通過可能にする上昇流経路と、を有するこ
とを特徴とする環境試験装置。
3. An evaporator constituting a refrigerator as a cooler
In addition to being equipped with a steam humidifier humidifier
The cooled circulating air was humidified with the steam.
In the environmental testing device, the circulating air can pass from above the cooler to below
A downstream flow cooler provided downstream of the downstream flow cooler, and an upward flow flow path that allows the circulating air to pass from below to above the downstream cooler. Characteristic environmental test equipment.
JP2001183471A 2001-06-18 2001-06-18 Environmental test equipment with downflow cooler Expired - Fee Related JP3519380B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001183471A JP3519380B2 (en) 2001-06-18 2001-06-18 Environmental test equipment with downflow cooler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001183471A JP3519380B2 (en) 2001-06-18 2001-06-18 Environmental test equipment with downflow cooler

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Publication Number Publication Date
JP2002372293A JP2002372293A (en) 2002-12-26
JP3519380B2 true JP3519380B2 (en) 2004-04-12

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ID=19023418

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Country Link
JP (1) JP3519380B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006214672A (en) * 2005-02-04 2006-08-17 Techno Ryowa Ltd Indoor circulation type cooling device
JP4466466B2 (en) * 2005-05-13 2010-05-26 積水ハウス株式会社 Weather resistance test method and weather resistance test apparatus
CN104502257B (en) * 2014-11-05 2017-02-15 中国人民解放军第二炮兵工程大学 Adhesive-corrosion-resistant performance detection method for solid self-lubricating coating
CN105043961A (en) * 2014-12-24 2015-11-11 高铁检测仪器(东莞)有限公司 Ozone-resistance test machine
CN112014305A (en) * 2020-09-01 2020-12-01 重庆阿泰可科技股份有限公司 Water-air spraying device and environment simulation system

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