JPH0474639B2 - - Google Patents

Info

Publication number
JPH0474639B2
JPH0474639B2 JP59154333A JP15433384A JPH0474639B2 JP H0474639 B2 JPH0474639 B2 JP H0474639B2 JP 59154333 A JP59154333 A JP 59154333A JP 15433384 A JP15433384 A JP 15433384A JP H0474639 B2 JPH0474639 B2 JP H0474639B2
Authority
JP
Japan
Prior art keywords
heat exchanger
heat
airflow
heat exchange
opening
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 - Lifetime
Application number
JP59154333A
Other languages
Japanese (ja)
Other versions
JPS6131888A (en
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 filed Critical
Priority to JP15433384A priority Critical patent/JPS6131888A/en
Publication of JPS6131888A publication Critical patent/JPS6131888A/en
Publication of JPH0474639B2 publication Critical patent/JPH0474639B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D19/00Regenerative heat-exchange apparatus in which the intermediate heat-transfer medium or body is moved successively into contact with each heat-exchange medium
    • F28D19/04Regenerative heat-exchange apparatus in which the intermediate heat-transfer medium or body is moved successively into contact with each heat-exchange medium using rigid bodies, e.g. mounted on a movable carrier
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D9/00Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/0062Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by spaced plates with inserted elements
    • F28D9/0068Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by spaced plates with inserted elements with means for changing flow direction of one heat exchange medium, e.g. using deflecting zones
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F2203/00Devices or apparatus used for air treatment
    • F24F2203/10Rotary wheel
    • F24F2203/104Heat exchanger wheel
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F2203/00Devices or apparatus used for air treatment
    • F24F2203/10Rotary wheel
    • F24F2203/1052Rotary wheel comprising a non-axial air flow
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F2203/00Devices or apparatus used for air treatment
    • F24F2203/10Rotary wheel
    • F24F2203/1068Rotary wheel comprising one rotor
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F2203/00Devices or apparatus used for air treatment
    • F24F2203/10Rotary wheel
    • F24F2203/1084Rotary wheel comprising two flow rotor segments
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2250/00Arrangements for modifying the flow of the heat exchange media, e.g. flow guiding means; Particular flow patterns
    • F28F2250/10Particular pattern of flow of the heat exchange media
    • F28F2250/108Particular pattern of flow of the heat exchange media with combined cross flow and parallel flow

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、一次気流と二次気流のエンタルピー
を有効に交換する空調換気扇等に用いる熱交換装
置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION FIELD OF INDUSTRIAL APPLICATION The present invention relates to a heat exchange device used in an air conditioning ventilation fan or the like that effectively exchanges enthalpy between a primary airflow and a secondary airflow.

従来例の構成とその問題点 従来一次気流と二次気流のエンタルピー交換と
しては、顕熱(温度)だけを交換する顕熱交換器
と、顕熱および潜熱(湿度)を同時に交換する全
熱交換器がある。このうち全熱交換方式として
は、回転体を用いて、蓄熱、放熱あるいは蓄湿、
放湿を繰り返すことにより全熱交換する蓄熱回転
式と仕切板を介して、顕熱および潜熱を交換する
静止透過式の2方式がある。
Conventional configurations and their problems Conventional enthalpy exchange between primary airflow and secondary airflow is performed using a sensible heat exchanger that exchanges only sensible heat (temperature) and a total heat exchanger that exchanges sensible heat and latent heat (humidity) at the same time. There is a vessel. Among these, the total heat exchange method uses a rotating body to store heat, release heat, or store moisture.
There are two methods: a heat storage rotary type that exchanges all heat by repeating moisture release, and a stationary transmission type that exchanges sensible heat and latent heat through a partition plate.

蓄熱回転式の場合には、蓄熱容量が少なく、か
つ顕熱蓄熱や水分の吸着熱や脱着熱の影響により
エレメントへの水分の有効吸着量が減少する欠点
がある。また静止透過式では温度湿度の交換は隔
壁(仕切板)を通しての伝導、拡散のため一般的
に全熱交換効率が低いという欠点がある。
In the case of the heat storage rotary type, there is a drawback that the heat storage capacity is small, and the effective amount of moisture adsorption to the element is reduced due to the effects of sensible heat storage and heat of adsorption and desorption of moisture. Furthermore, the stationary transmission type has the disadvantage that the total heat exchange efficiency is generally low because temperature and humidity exchange is conducted and diffused through partition walls (partition plates).

また空調換気扇を考えた場合、夏場の冷房時に
おいては、室内側の温度、湿度とも室外側よりも
低い場合には全熱交換が有利である。また湿度が
室内のほうが高い場合などは逆に顕熱交換が有利
になる。
Furthermore, when considering air conditioning ventilation fans, total heat exchange is advantageous during cooling in the summer when both the temperature and humidity inside the room are lower than those outside the room. On the other hand, when the humidity is higher indoors, sensible heat exchange becomes advantageous.

以上のように年間を通じて有効な空調換気をす
るためには、顕熱交換と全熱交換が分離できるこ
とが望ましい。しかしながら前記2方式ともに、
全熱交換の単一機能であり、有効な空調換気がで
きない欠点がある。
As mentioned above, in order to provide effective air conditioning and ventilation throughout the year, it is desirable to be able to separate sensible heat exchange and total heat exchange. However, both of the above two methods
It has a single function of total heat exchange, and has the disadvantage that effective air conditioning and ventilation cannot be performed.

発明の目的 本発明は上記欠点を改良するもので従来よりも
高効率で一つの熱交換器で、顕熱交換および全熱
交換が別々に出来るという複合機能をもつた新方
式である蓄熱透過回転熱交換装置を提供するもの
である。
Purpose of the Invention The present invention aims to improve the above-mentioned drawbacks, and is a new system with heat storage transmission rotation that has higher efficiency than conventional heat exchangers and has a combined function of separately performing sensible heat exchange and total heat exchange. A heat exchange device is provided.

発明の構成 本発明は、空気流路を形成する第1および第2
のエレメントを円周方向に交互に積層して肉厚の
円筒形状熱交換器を形成し、前記第1と第2のエ
レメント間の隔壁を非透湿とするとともに、前記
第1の第2のエレメントを構成する素材の少なく
とも一部を吸湿性とし、前記第1のエレメントは
円筒状熱交換器の一端側の内周部と他端側の外周
部に開口部を有し、内周部開口部から軸方向通路
を通つて多端側の外周部の開口部へおよびその逆
に流れるように気流を通過可能とし、前記第2の
エレメントは他端側の内周部と一端側の外周部に
開口部を有し、他端側の内周開口部から軸方向通
路を通つて一端側の外周開口部へおよびその逆に
気流を通過可能とし、前記第1のエレメントと第
2のエレメントの空気流路にそれぞれ異なる一次
気流と二次気流を隔壁を介して向流方向に流す構
成とするとともに、前記円筒形状熱交換器を回転
することにより前記第1のエレメントと第2のエ
レメントの通路を通過する一次気流と二次気流を
周期的に入れ換える構成としたものである。よつ
て、円筒形状熱交換器を回転させれば第1のエレ
メントと第2のエレメントの両方に一次気流と二
次気流が周期的に流れ込むので、全熱交換が行
え、また、円筒形状熱交換器の回転を停止すれ
ば、隣り合う第1のエレメントと第2のエレメン
トとの間で顕熱交換を行うことができる。熱交換
は、エレメントへの蓄熱蓄湿だけでなく、仕切板
を介しての熱の透過がある。つまり蓄熱回転式と
静止透過式の組み合せになり、従来より高い熱交
換効率が得られる。これは従来の蓄熱回転式で
は、蓄熱板に流入する熱量は、その熱容量により
制限されるが、本発明の蓄熱体になる仕切板は、
他方の面へ熱が透過しているため、発生した吸着
熱や流入熱量の処理がエレメントの回転以外でも
可能なためエレメントの流入熱量が増加するとと
もに、エレメントへの水分の有効吸着量を多くと
れるためである。
Structure of the Invention The present invention provides first and second
elements are stacked alternately in the circumferential direction to form a thick-walled cylindrical heat exchanger, the partition wall between the first and second elements is made non-permeable, and the first and second elements are made non-permeable. At least a part of the material constituting the element is hygroscopic, and the first element has an opening on an inner circumference on one end side of the cylindrical heat exchanger and an outer circumference on the other end side. The second element is configured to allow airflow to pass through the axial passage from the inner periphery of the other end to the outer periphery of the other end and vice versa. an opening that allows air to pass from the inner circumferential opening on the other end side through the axial passage to the outer circumferential opening on the one end side and vice versa, and air in the first element and the second element The passage between the first element and the second element is configured so that different primary airflow and secondary airflow flow through the flow path in countercurrent directions through a partition wall, and the passage between the first element and the second element is formed by rotating the cylindrical heat exchanger. The structure is such that the passing primary airflow and secondary airflow are periodically replaced. Therefore, when the cylindrical heat exchanger is rotated, the primary airflow and the secondary airflow periodically flow into both the first element and the second element, so total heat exchange can be performed. When the rotation of the container is stopped, sensible heat exchange can be performed between the adjacent first element and second element. Heat exchange involves not only heat storage and moisture storage in the element, but also heat transmission through the partition plate. In other words, it is a combination of a heat storage rotation type and a stationary transmission type, and higher heat exchange efficiency can be obtained than before. In the conventional heat storage rotary type, the amount of heat flowing into the heat storage plate is limited by its heat capacity, but the partition plate that becomes the heat storage body of the present invention
Since the heat is transmitted to the other surface, the generated adsorption heat and inflow heat can be processed outside of the rotation of the element, which increases the inflow heat of the element and increases the effective amount of water adsorption into the element. It's for a reason.

また非透質湿の隔壁(仕切板)のため水分の移
行はエレメントへの蓄湿によつてのみ行なわれ
る。よつて熱交換器の回転を停止した場合には湿
度の交換がなくなり温度だけ交換する顕熱交換器
になる。このことにより、有効な空調換気を全熱
交換と顕熱交換を組み合せることにより実現でき
る。
Furthermore, since the partition wall is a non-permeable moisture barrier, moisture transfer is only carried out by accumulating moisture in the element. Therefore, when the rotation of the heat exchanger is stopped, humidity is no longer exchanged, and the heat exchanger becomes a sensible heat exchanger that only exchanges temperature. As a result, effective air conditioning ventilation can be achieved by combining total heat exchange and sensible heat exchange.

実施例の説明 本発明の一実施例を図面にもとづいて説明す
る。第1図は本発明の実施例における円筒状熱交
換器である。図中1は第1のエレメント、2は第
2のエレメントであり、それらが交互に積層して
円筒状熱交換器を形成する。第2図は第1および
第2のエレメントを示した図であり、エレメント
は、非透湿性の隔壁(仕切板)3と、円筒軸方向
の端面、内周部および外周部に、一次気流と二次
気流の混合を防止するための端面部間隔板4と、
一次気流と二次気流をエレメント内通路をくまな
く流すための間隔板5によつて構成されており、
これらの材質は塩化ビニルの板で表面に吸湿材と
してコロイダルシリカを塗布して乾燥させたもの
である。
DESCRIPTION OF EMBODIMENTS An embodiment of the present invention will be described based on the drawings. FIG. 1 shows a cylindrical heat exchanger in an embodiment of the present invention. In the figure, 1 is a first element and 2 is a second element, which are alternately stacked to form a cylindrical heat exchanger. FIG. 2 is a diagram showing the first and second elements, and the elements include a moisture-impermeable partition wall (partition plate) 3, an end face in the axial direction of the cylinder, an inner peripheral part, and an outer peripheral part, and the primary air flow. an end spacer plate 4 for preventing mixing of secondary airflow;
It is composed of a spacer plate 5 that allows the primary airflow and secondary airflow to flow throughout the passage within the element.
These materials are vinyl chloride plates coated with colloidal silica as a moisture absorbing material and dried.

第3図は熱交換器6内の気流の流出入経路を示
した図である。図において、熱交換器は上下に完
全に仕切られている。熱交換器の上部において、
一次気流Aは円筒の一端側の内周部より入り、他
端側の外周部より出る。一方二次気流Bに同様
に、他端側の内周部より入り、一端側の外周部よ
り出る。また図における熱交換器下部では、一次
気流Aは、一端側外周部より入り、他端側内周部
より出る。同様に二次気流Bは、他端側外周部よ
り入り一端側内周部より出る。すなわち、熱交換
器6の上部において一次気流Aが流れる第1のエ
レメントが熱交換器6の下部に移動すれば、その
第1のエレメントには二次気流Bが流れるように
して第1のエレメントが上部から下部に移動する
ことで全熱交換が行えるようにしている。なお、
第1のエレメントの流路が上部の一次気流Aの流
れとすると、下部に移動した第1のエレメントの
流路は二次気流Bの流れとなり、上部と下部とで
は流れる方向が逆転する構成である。第4図は熱
交換器の一部を示したもので、第3図の熱交換器
の上部における各エレメント中の気流の流れを示
している。一次気流Aは第1のエレメント1の内
周部から入り、外周部より出る。また二次気流B
も第2のエレメント2の内周部から入り外周部よ
り出る。熱交換器は回転しているため、第4図に
示した熱交換器の一部は第3図に示されている下
部の部分に移る。今度は、一次気流Aが第2のエ
レメント中を、二次気流Bの流れとは逆の方向、
つまり外周部から入り内周部より出る。二次気流
Bも同様に、第1のエレメント中を、一次気流A
の流れの方向とは逆に流れる。このようにエレメ
ントの回転により、第1のエメレントと第2のエ
メレント中を流れる気流を交換することができ
る。以上が本発明における熱交換器内を流れる気
流の流れの一実施例である。
FIG. 3 is a diagram showing the inflow and outflow paths of airflow within the heat exchanger 6. In the figure, the heat exchanger is completely partitioned into upper and lower parts. At the top of the heat exchanger,
The primary airflow A enters from the inner periphery of one end of the cylinder and exits from the outer periphery of the other end. On the other hand, similarly to the secondary air flow B, it enters from the inner circumferential portion on the other end side and exits from the outer circumferential portion on the one end side. Further, in the lower part of the heat exchanger in the figure, the primary air flow A enters from the outer circumferential portion on one end side and exits from the inner circumferential portion on the other end side. Similarly, the secondary airflow B enters from the outer periphery of the other end and exits from the inner periphery of the one end. That is, if the first element through which the primary airflow A flows in the upper part of the heat exchanger 6 moves to the lower part of the heat exchanger 6, the secondary airflow B flows through the first element and the first element moves from the top to the bottom, allowing for total heat exchange. In addition,
If the flow path of the first element is the flow of the primary airflow A in the upper part, the flow path of the first element that has moved to the lower part is the flow of the secondary airflow B, and the flow direction is reversed between the upper and lower parts. be. FIG. 4 shows a part of the heat exchanger, and shows the flow of air in each element in the upper part of the heat exchanger of FIG. The primary airflow A enters from the inner circumference of the first element 1 and exits from the outer circumference. Also, secondary airflow B
It also enters from the inner periphery of the second element 2 and exits from the outer periphery. As the heat exchanger is rotating, the portion of the heat exchanger shown in FIG. 4 is transferred to the lower portion shown in FIG. This time, the primary airflow A flows through the second element in the opposite direction to the flow of the secondary airflow B,
In other words, it enters from the outer circumference and exits from the inner circumference. Similarly, the secondary airflow B flows through the primary airflow A through the first element.
Flows in the opposite direction to the direction of flow. By rotating the element in this way, the airflow flowing through the first emerent and the second emerent can be exchanged. The above is an example of the flow of air flowing inside the heat exchanger according to the present invention.

この様な方式では従来の静止透過式もしくは蓄
熱回転式に比べて高い効率の熱交換を可能にな
る。以下それについて述べる。一次気流Aと二次
気流B間の熱交換は、第2図における第1と第2
エレメント間の隔壁(仕切板)3を通して行なわ
れるが、隔壁は非透湿性の材料を用いているた
め、顕熱交換だけ行なわれる。しかし、前述の様
に熱交換器は回転しており、第1のエレメントで
は、一次気流と二次気流とが交互に入れ換わるこ
とを繰り返すことにより蓄熱回転式と同様に、全
熱交換が行なえる。すなわち非透湿性の隔壁(仕
切板)3、第2図で示した間隔板5に吸湿剤、シ
リカを塗布しているので温度と水分を交換する全
熱交換器になる。なお間隔板5の材質は、透湿性
の紙や不透湿性の金属などいずれでもよい。
This type of system enables heat exchange with higher efficiency than the conventional stationary transmission type or heat storage rotating type. I will discuss it below. The heat exchange between the primary airflow A and the secondary airflow B is
This is carried out through partition walls (partition plates) 3 between the elements, but since the partition walls are made of moisture-impermeable material, only sensible heat exchange takes place. However, as mentioned above, the heat exchanger rotates, and in the first element, the primary airflow and the secondary airflow are alternated repeatedly, so that total heat exchange can be performed as in the heat storage rotary type. Ru. That is, since the moisture-impermeable partition wall (partition plate) 3 and the spacer plate 5 shown in FIG. 2 are coated with a moisture absorbent and silica, it becomes a total heat exchanger that exchanges temperature and moisture. Note that the material of the spacer plate 5 may be any material such as moisture-permeable paper or moisture-impermeable metal.

本発明の熱交換器の利点は上記のごとく、熱交
換が、静止透過式と蓄熱回転式を合わせたもので
あり、高効率が得られることである。これは、顕
熱のみならず、エレメントへの水分の吸着および
脱着にともなう吸着熱や脱着熱を、熱交換器の回
転による蓄熱だけによらず、隔壁(仕切板)3を
通して移行さすことができるためと、そのことに
よりエレメントの水分の有効吸収量を多くとるこ
とができることに起因する。
As mentioned above, the advantage of the heat exchanger of the present invention is that the heat exchange is a combination of the stationary transmission type and the heat storage rotation type, and high efficiency can be obtained. This allows not only sensible heat, but also adsorption heat and desorption heat associated with adsorption and desorption of moisture to the element, to be transferred through the partition wall (partition plate) 3 and not only due to heat storage due to the rotation of the heat exchanger. This is because the element can effectively absorb a large amount of water.

また前記熱交換器の回転を停止した場合には、
熱交換機構は隔壁(仕切板)3を通しての通過
(伝導)だけになり、顕熱交換を行なうことがで
きる。
Furthermore, when the rotation of the heat exchanger is stopped,
The heat exchange mechanism consists only of passage (conduction) through the partition wall (partition plate) 3, and sensible heat exchange can be performed.

発明の効果 以上のごとく本発明の熱交換装置では、全熱交
換効率を隔壁からの透過(伝導)と回転による蓄
熱、蓄湿の両方からの効果により、従来より高く
出来る。また熱交換器の回転を停止することによ
り、全熱交換を顕熱交換にすることができる。す
なわち環境条件に応じて全熱交換と顕熱交換を使
い分けることができ、より有効な熱交換を行なえ
る特徴をもつている。
Effects of the Invention As described above, in the heat exchange device of the present invention, the total heat exchange efficiency can be made higher than before due to the effects of both transmission (conduction) from the partition walls and heat storage and moisture storage due to rotation. Further, by stopping the rotation of the heat exchanger, the total heat exchange can be changed to sensible heat exchange. In other words, it is possible to use total heat exchange and sensible heat exchange depending on the environmental conditions, and has the feature of more effective heat exchange.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の熱交換装置を実現するための
一実施例の熱交換器の斜視図、第2図は前記熱交
換を構成する第1および第2のエレメントの斜視
図、第3図は前記熱交換器内を通る気流の説明
図、第4図は第3図の気流を示す熱交換器の部分
的概略説明図である。 1……第1エレメント、2……第2エレメン
ト、3……隔壁(仕切板)、4……端面部仕切板、
5……間隔板、6……熱交換器。
FIG. 1 is a perspective view of a heat exchanger of an embodiment for realizing the heat exchange device of the present invention, FIG. 2 is a perspective view of first and second elements constituting the heat exchange, and FIG. 3 4 is an explanatory diagram of the airflow passing through the heat exchanger, and FIG. 4 is a partial schematic explanatory diagram of the heat exchanger showing the airflow of FIG. 3. 1... First element, 2... Second element, 3... Partition wall (partition plate), 4... End face partition plate,
5... Spacing plate, 6... Heat exchanger.

Claims (1)

【特許請求の範囲】[Claims] 1 空気流路を形成する第1および2のエレメン
トを円周方向に交互に積層して肉厚の円筒形状熱
交換器を形成し、前記第1と第2のエレメント間
の隔壁を非透湿とするとともに、前記第1の第2
のエレメントを構成する素材の少なくとも一部を
吸湿性とし、前記第1のエレメントは円筒状熱交
換器の一端側の内周部と他端部の外周部に開口部
を有し、内周部開口部から軸方向通路を通つて多
端側の外周部の開口部へおよびその逆に流れるよ
うに気流を通過可能とし、前記第2のエレメント
は他端側の内周部と一端側の外周部に開口部を有
し、他端側の内周開口部から軸方向通路を通つて
一端側の外周開口部へおよびその逆に流れるよう
に気流を通過可能とし、前記第1のエレメントと
第2のエレメントの空気流路にそれぞれ異なる一
次気流と二次気流を隔壁を介して向流方向に流す
構成とするとともに、前記円筒形状熱交換器を回
転することにより前記第1のエレメントと第2の
エレメントの通路を通過する一次気流と二次気流
を周期的に入れ換える構成とした熱交換装置。
1 A thick cylindrical heat exchanger is formed by alternately stacking first and second elements that form an air flow path in the circumferential direction, and the partition wall between the first and second elements is made non-moisture permeable. and the first and second
At least a part of the material constituting the element is hygroscopic, and the first element has an opening at an inner periphery at one end of the cylindrical heat exchanger and an outer periphery at the other end. The second element allows air to pass through the opening through the axial passage to the opening on the outer periphery of the other end and vice versa, and the second element has an inner periphery on the other end and an outer periphery on the one end. has an opening at the other end, and allows airflow to pass through the inner opening at the other end through the axial passage to the outer opening at the one end, and vice versa; In addition, by rotating the cylindrical heat exchanger, the first element and the second A heat exchange device configured to periodically replace the primary airflow and secondary airflow that pass through the element passage.
JP15433384A 1984-07-25 1984-07-25 Heat exchanging device Granted JPS6131888A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15433384A JPS6131888A (en) 1984-07-25 1984-07-25 Heat exchanging device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15433384A JPS6131888A (en) 1984-07-25 1984-07-25 Heat exchanging device

Publications (2)

Publication Number Publication Date
JPS6131888A JPS6131888A (en) 1986-02-14
JPH0474639B2 true JPH0474639B2 (en) 1992-11-26

Family

ID=15581854

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15433384A Granted JPS6131888A (en) 1984-07-25 1984-07-25 Heat exchanging device

Country Status (1)

Country Link
JP (1) JPS6131888A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001069154A1 (en) * 2000-03-14 2001-09-20 Air-Change Pty Limited Heat exchanger
ES2935298T3 (en) * 2015-03-17 2023-03-03 Zehnder Group Int Ag Interchange element for passenger cabin, as well as passenger cabin equipped with said interchange element
NL2016731B1 (en) * 2016-05-03 2017-11-10 Recair Holding B V Device for exchanging energy between two air flows.

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5741592A (en) * 1980-08-25 1982-03-08 Matsushita Electric Ind Co Ltd Composite heat exchanger

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5741592A (en) * 1980-08-25 1982-03-08 Matsushita Electric Ind Co Ltd Composite heat exchanger

Also Published As

Publication number Publication date
JPS6131888A (en) 1986-02-14

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