JP2827809B2 - Heat transfer device - Google Patents
Heat transfer deviceInfo
- Publication number
- JP2827809B2 JP2827809B2 JP10807793A JP10807793A JP2827809B2 JP 2827809 B2 JP2827809 B2 JP 2827809B2 JP 10807793 A JP10807793 A JP 10807793A JP 10807793 A JP10807793 A JP 10807793A JP 2827809 B2 JP2827809 B2 JP 2827809B2
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- refrigerant
- gas
- valve
- heat transfer
- 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
Links
Landscapes
- Applications Or Details Of Rotary Compressors (AREA)
- Central Heating Systems (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、冷媒を加熱する時の圧
力上昇を利用して、熱を暖房などに利用する熱搬送装置
に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat transfer apparatus for utilizing heat for heating or the like by utilizing a pressure increase when a refrigerant is heated.
【0002】[0002]
【従来の技術】従来の熱搬送装置は、例えば特開平3−
51631号公報に示されるように、図2のような構成
になっている。2. Description of the Related Art A conventional heat transfer device is disclosed in, for example,
As shown in Japanese Patent No. 51631, the configuration is as shown in FIG.
【0003】すなわち、気液セパレータ1は、冷媒加熱
器2の上方に配設されるとともに冷媒加熱器2の入口管
3と冷媒加熱器2の出口管4とで冷媒加熱器2と連結さ
れ、環状の経路を構成している。さらに、受液器5は気
液セパレータ1の上方に配設され、第1逆止弁6を有す
る落込み管7で下方にある気液セパレータ1へ接続さ
れ、さらに開閉弁8を有する均圧管9により出口管4を
介して気液セパレータ1に接続されている。気液セパレ
ータ1と利用側として室内側に配置される放熱器10
は、ガス冷媒往き管11で接続され、放熱器10と受液
器5は、第2逆止弁12を有する液冷媒戻り管13で接
続されている。以上のように、気液セパレータ1、放熱
器10、第2逆止弁12、受液器5、第1逆止弁6は順
次配管接続された環状の循環路を形成している。That is, the gas-liquid separator 1 is disposed above the refrigerant heater 2 and is connected to the refrigerant heater 2 by an inlet pipe 3 of the refrigerant heater 2 and an outlet pipe 4 of the refrigerant heater 2. It forms an annular path. Further, the liquid receiver 5 is disposed above the gas-liquid separator 1, connected to the gas-liquid separator 1 below by a drop pipe 7 having a first check valve 6, and furthermore, a pressure equalizing pipe having an on-off valve 8. 9 is connected to the gas-liquid separator 1 via the outlet pipe 4. Gas-liquid separator 1 and radiator 10 arranged indoors as a use side
Are connected by a gas refrigerant outgoing pipe 11, and the radiator 10 and the liquid receiver 5 are connected by a liquid refrigerant return pipe 13 having a second check valve 12. As described above, the gas-liquid separator 1, the radiator 10, the second check valve 12, the liquid receiver 5, and the first check valve 6 form an annular circulation path that is sequentially connected to the pipe.
【0004】14は冷媒加熱器2の出口管4に設けた温
度検知器であり、15は温度検知器14の検知する温度
により、開閉弁8の開閉時間を制御する制御装置であ
る。16は冷媒加熱器2に設けたバーナであり、このバ
ーナ16により冷媒を加熱する。17は放熱器10に設
けた送風機である。第1逆止弁6は、冷媒回路で一般に
用いられる圧力差により生じる流れで開閉動作を行うも
のであり、受液器5が気液セパレータ1より低圧力の時
開き、高圧力の時は閉止する。[0004] Reference numeral 14 denotes a temperature detector provided in the outlet pipe 4 of the refrigerant heater 2, and reference numeral 15 denotes a control device for controlling the opening / closing time of the on-off valve 8 based on the temperature detected by the temperature detector 14. Reference numeral 16 denotes a burner provided in the refrigerant heater 2, and the refrigerant is heated by the burner 16. 17 is a blower provided in the radiator 10. The first check valve 6 opens and closes by a flow generated by a pressure difference generally used in the refrigerant circuit, and opens when the receiver 5 is at a lower pressure than the gas-liquid separator 1 and closes when the receiver is at a high pressure. I do.
【0005】上記構成において、その動作を以下に説明
する。冷媒加熱器2において、バーナ16の燃焼熱で加
熱された冷媒は、ガスと液の2相状態で出口管4を通
り、気液セパレータ1へ流入し、液冷媒は入口管3から
再び冷媒加熱器2に流入する。一方、気液セパレータ1
へ流入した2相状態の冷媒のうちガス冷媒は、ガス冷媒
往き管11から放熱器10へ入り、送風機17で送られ
た室内空気と熱交換し、放熱凝縮し過冷却液化する。The operation of the above configuration will be described below. In the refrigerant heater 2, the refrigerant heated by the combustion heat of the burner 16 passes through the outlet pipe 4 in the two-phase state of gas and liquid, flows into the gas-liquid separator 1, and the liquid refrigerant heats again from the inlet pipe 3. Into the vessel 2. On the other hand, the gas-liquid separator 1
Of the two-phase refrigerant flowing into the gas refrigerant, the gas refrigerant enters the radiator 10 through the gas refrigerant outflow pipe 11, exchanges heat with the room air sent by the blower 17, radiates and condenses, and turns into supercooled liquid.
【0006】ここで、開閉弁8が閉のときには、放熱器
10で凝縮液化した過冷却液冷媒は、液冷媒戻り管13
から第2逆止弁12を介して、ガス冷媒を凝縮させるこ
とにより受液器5内へ流入する。このとき受液器5内の
圧力は気液セパレータ1内の圧力より低くなっているた
め、第1逆止弁6は閉状態となる。この状態で、開閉弁
8を開とすると、受液器5と気液セパレータ1とは均圧
管9により連通して均圧状態となり、受液器5内の液冷
媒は重力により第1逆止弁6を通り気液セパレータ1内
へ流入する。When the on-off valve 8 is closed, the supercooled liquid refrigerant condensed and liquefied by the radiator 10 is supplied to the liquid refrigerant return pipe 13.
Then, the gas refrigerant flows into the liquid receiver 5 through the second check valve 12 by condensing the gas refrigerant. At this time, since the pressure in the liquid receiver 5 is lower than the pressure in the gas-liquid separator 1, the first check valve 6 is closed. In this state, when the on-off valve 8 is opened, the liquid receiver 5 and the gas-liquid separator 1 communicate with each other by the pressure equalizing pipe 9 to be in an equal pressure state, and the liquid refrigerant in the liquid receiver 5 is subjected to the first check by gravity. The gas flows into the gas-liquid separator 1 through the valve 6.
【0007】次に、開閉弁8を再び閉にすると、受液器
8内のガス冷媒が凝縮するためこの受液器8内は気液セ
パレータ1より低圧となり、第1逆止弁6は閉状態にな
る。そして、受液器5内へ放熱器10の凝縮過冷却した
液冷媒が受液器5内の急減圧により吸引され、受液器5
が液冷媒で満たされるサイクルを繰り返す。このよう
に、気液セパレータ1と冷媒加熱器2間は蒸発した冷媒
圧による自然循環サイクルであり、受液器5から気液セ
パレータ1および冷媒加熱器2への液冷媒の供給は開閉
弁8の開閉周期による間欠動作サイクルである。Next, when the on-off valve 8 is closed again, the gas refrigerant in the receiver 8 is condensed, so that the pressure in the receiver 8 is lower than that of the gas-liquid separator 1 and the first check valve 6 is closed. State. Then, the liquid refrigerant condensed and supercooled by the radiator 10 is sucked into the receiver 5 by the rapid decompression in the receiver 5, and
Is repeated with the liquid refrigerant. As described above, a natural circulation cycle is performed between the gas-liquid separator 1 and the refrigerant heater 2 by the evaporated refrigerant pressure, and the supply of the liquid refrigerant from the receiver 5 to the gas-liquid separator 1 and the refrigerant heater 2 is performed by the on-off valve 8. Is an intermittent operation cycle based on the opening / closing cycle.
【0008】[0008]
【発明が解決しようとする課題】上記従来の構成におい
て、冷媒加熱による熱搬送を行なうため開閉弁8の開閉
動作周期の設定は、図3に示すように、受液器5内の減
圧が発生して空となった受液器5内が液冷媒で満たされ
減圧が完了する開閉弁8の閉時間TOFFと満液となった
受液器5から気液セパレータ1へ液冷媒が落し込まれる
開閉弁8の開時間TONとの和が開閉周期TS(TS=TON
+TOFF)である。In the above-mentioned conventional structure, the opening and closing operation cycle of the on-off valve 8 for carrying out heat transfer by heating the refrigerant is performed as shown in FIG. The liquid receiver drops into the gas-liquid separator 1 from the liquid receiver 5 which is full when the shut- off time T OFF of the on-off valve 8 is completed when the inside of the liquid receiver 5 which has become empty is filled with the liquid refrigerant and the decompression is completed. sum closing period of the opening time T ON of the on-off valve 8 to T S (T S = T ON
+ T OFF ).
【0009】閉時間TOFFは受液器5の内容積および放
熱器10から受液器5までの流路抵抗により定まり、さ
らに開時間TONは受液器5の内容積および均圧管9と落
込み管7および第1逆止弁の流路抵抗により定まる。The closing time T OFF is determined by the internal volume of the receiver 5 and the flow path resistance from the radiator 10 to the receiver 5, and the opening time T ON is the internal volume of the receiver 5 and the pressure equalizing pipe 9. It is determined by the flow path resistance of the drop pipe 7 and the first check valve.
【0010】このように開閉弁8の開閉周期TSは開時
間TONと閉時間TOFFの和(TS=TO N+TOFF)であ
り、この開時間TONが比較的大きいために、開閉周期T
Sが長目に設定せざるを得ない状況となり、熱搬送量
(暖房に利用の場合は暖房能力)の大能力化に制約があ
った。[0010] the sum of the closing period T S is open time T ON and the closing time T OFF of the thus-off valve 8 (T S = T O N + T OFF), due to the relatively large this open time T ON , Opening and closing cycle T
There was a situation where S had to be set longer, and there was a restriction on increasing the heat transfer amount (heating capacity in the case of heating).
【0011】本発明は上記課題を解決するもので、容器
を上部の受液部と下部の液溜部に仕切る仕切り板により
構成し、この仕切り板に開閉弁を有することにより、均
圧管を無くし落込み管を無くし、この流路抵抗を小さく
して落し込み時間を短くすることにより開閉周期を短縮
にでき、熱搬送量の大能力化と、受液部と気液セパレー
タ部と液溜部を一つの容器で構成し、かつ逆止弁を無く
すことができるため部品が少なくまたロー付け箇所の減
少になることにより信頼性の向上と低コスト化を図るこ
とを目的とする。The present invention has been made to solve the above-mentioned problem, and comprises a partition plate for partitioning a container into an upper liquid receiving portion and a lower liquid reservoir portion. This partition plate has an on-off valve to eliminate the pressure equalizing pipe. The opening / closing cycle can be shortened by eliminating the dropping pipe and reducing the flow path resistance and shortening the dropping time, increasing the heat transfer capacity, increasing the liquid receiving part, gas-liquid separator part, and liquid reservoir part. It is an object of the present invention to improve reliability and reduce costs by reducing the number of parts and reducing the number of brazing points because the check valve can be constituted by one container and the check valve can be eliminated.
【0012】[0012]
【課題を解決するための手段】本発明は上記目的を達成
するために、冷媒加熱器、この冷媒加熱器の上方に配設
された容器、前記容器内を上部の受液部と下部の気液セ
パレータ液溜部に仕切る仕切り板、前記冷媒加熱器と前
記気液セパレータ液溜部を連通する入口管と出口管、前
記仕切り板に開閉弁を有する熱搬送部と、前記気液セパ
レータ液溜部、放熱器および前記受液部を順次接続した
環状の循環路と、前記開閉弁の開閉を行う制御部からな
る構成としている。In order to achieve the above object, the present invention provides a refrigerant heater, a container disposed above the refrigerant heater, and an upper liquid receiving part and a lower gas receiver in the container. A partition plate for partitioning the liquid separator into a liquid reservoir, an inlet pipe and an outlet pipe that communicate the refrigerant heater with the gas-liquid separator liquid reservoir, a heat transfer unit having an on-off valve in the partition plate, and the gas-liquid separator liquid reservoir. And a control unit that opens and closes the on-off valve.
【0013】仕切り板の上下に断熱材を設け、または仕
切り板の形状を下方に凸状にしたものである。さらに出
口管の気液セパレータ液溜部と連通部と循環路の気液セ
パレータ液溜部との接続部の間に開口部を有する板を設
けたものである。A heat insulating material is provided above and below the partition plate, or the shape of the partition plate is made convex downward. Further, a plate having an opening is provided between a connection portion between the gas-liquid separator liquid storage portion of the outlet pipe and the communication portion, and a connection portion between the gas-liquid separator liquid storage portion of the circulation path.
【0014】[0014]
【作用】本発明は上記構成によって、容器を上部の受液
部と下部の気液セパレータ液溜部に仕切る仕切り板によ
り構成し、均圧管を無くし前記開閉弁から液冷媒の落下
と同時にガス冷媒が置換する様に前記開閉弁の口径を大
きくする。落込み管は前記仕切り板に直接開閉弁を取付
けたことにより最短となり、前記開閉弁の口径を大きく
すると、均圧管に相当する流路抵抗と落し込み管の流路
抵抗は小さくなり、開閉弁が開成と同時に、満液となっ
た受液部の液冷媒は気液セパレータ液溜部へ大量に短時
間に落し込まれる。According to the present invention, the above-mentioned construction comprises a partition plate for partitioning the container into an upper liquid receiving portion and a lower gas-liquid separator liquid reservoir portion. The diameter of the on-off valve is increased so that is replaced. The downpipe becomes the shortest by attaching the on-off valve directly to the partition plate, and when the diameter of the on-off valve is increased, the flow path resistance corresponding to the pressure equalizing pipe and the flow path resistance of the dropping pipe become small, and the on-off valve At the same time as the opening, the liquid refrigerant in the liquid receiving section that has become full is dropped in a large amount into the gas-liquid separator liquid storage section in a short time.
【0015】このように流路抵抗を小さくすることによ
り、開閉弁の開時間を大幅に短縮して開閉周期を小さく
し、単位時間当りの受液器の吸引・落込み回数を増大さ
せて冷媒循環量を増大可能とし、冷媒加熱量を増大させ
る。また、開閉弁と第1逆止弁を一つの開閉弁で構成で
きる。By reducing the flow path resistance in this way, the opening time of the on-off valve is greatly reduced, the opening / closing cycle is reduced, and the number of suction / drops of the liquid receiver per unit time is increased to increase the refrigerant flow. The circulation amount can be increased, and the refrigerant heating amount is increased. Further, the on-off valve and the first check valve can be constituted by one on-off valve.
【0016】さらに、仕切り板を下方に凸状に形成する
ことにより、液冷媒が受液部から落ちる時間が短くな
る。また、仕切り板の上部または下部に断熱材を設ける
構成として、受液部と気液セパレータ液溜部を断熱し受
液部の温度上昇を防止する。Further, by forming the partition plate in a downwardly convex shape, the time for the liquid refrigerant to fall from the liquid receiving portion is reduced. Further, as a configuration in which a heat insulating material is provided above or below the partition plate, the liquid receiving part and the gas-liquid separator liquid storing part are insulated to prevent a rise in the temperature of the liquid receiving part.
【0017】そして、連通部と、接続部の間に、開口部
を有する板を設けることにより、気液混合冷媒の液冷媒
は下の液溜部に溜りガス冷媒は循環路へと流れる。By providing a plate having an opening between the communicating portion and the connecting portion, the liquid refrigerant of the gas-liquid mixed refrigerant is stored in the lower liquid storage portion, and the gas refrigerant flows to the circulation path.
【0018】また、この断熱材を下方に凸状に形成し、
断熱材の最下端部に対応する仕切り板に逆止弁を設ける
ことにより、液冷媒が受液部から落ちる時間が短くな
り、開閉弁の開時間TONを短縮でき、冷媒循環能力が増
大する。Further, the heat insulating material is formed in a downward convex shape,
By providing a check valve on the partition plate corresponding to the lowermost end of the heat insulating material, the time during which the liquid refrigerant falls from the liquid receiving portion is shortened, the open time T ON of the on-off valve can be shortened, and the refrigerant circulation capacity increases. .
【0019】[0019]
【実施例】以下本発明の一実施例を図1で説明する。図
1において、図3と同一符号は同一部材を示し同一機能
を有しているので詳細な説明は省略し、異なる点を中心
に説明する。FIG. 1 shows an embodiment of the present invention. 1, the same reference numerals as those in FIG. 3 denote the same members, and have the same functions. Therefore, detailed description will be omitted, and different points will be mainly described.
【0020】18は、冷媒加熱器2の上方に配置された
容器であり、この容器18を上部の受液部19と下部の
気液セパレータ液溜部20に仕切り板21により仕切っ
ている。冷媒加熱器2と気液セパレータ液溜部20を入
口管3と出口管4で連通してある。22は、バーナ16
を有する冷媒加熱器2と気液セパレータ液溜部20を環
状管路に接続し、受液部19と気液セパレータ液溜部2
0の間に開閉弁23を設けた管路と前記環状管路に接続
した熱搬送部である。24は気液セパレータ液溜部2
0、放熱器10、第2逆止弁12、受液部19を順次配
管接続した環状の循環路である。容器18は、鉄アルミ
等金属を成型した後ブレージング、溶接等で仕切り板2
1と一体に形成し、開閉弁23は仕切り板21と接合ま
たは、一体構成とする。本実施例では、仕切り板21と
一体に弁座部27を構成し、この弁座部27に接して摺
動する弁体28を電磁コイル29で動かし、開閉弁23
を開閉する。Reference numeral 18 denotes a container arranged above the refrigerant heater 2, and the container 18 is divided into an upper liquid receiving portion 19 and a lower gas-liquid separator liquid reservoir 20 by a partition plate 21. The refrigerant heater 2 and the gas-liquid separator liquid reservoir 20 communicate with each other through an inlet pipe 3 and an outlet pipe 4. 22 is the burner 16
The liquid heater 20 and the gas-liquid separator liquid reservoir 20 are connected to an annular pipe, and the liquid receiver 19 and the gas-liquid separator liquid reservoir 2 are connected to each other.
0 and a heat transfer section connected to the annular pipe provided with the on-off valve 23 and the annular pipe. 24 is a gas-liquid separator liquid reservoir 2
0, a radiator 10, a second check valve 12, and a liquid receiving portion 19 are sequentially connected to the pipe by an annular circulation path. The container 18 is made of a metal such as iron or aluminum, and then brazed, welded, or the like.
1, the on-off valve 23 is joined to the partition plate 21 or is formed as an integral structure. In the present embodiment, a valve seat 27 is formed integrally with the partition plate 21, and a valve body 28 slid in contact with the valve seat 27 is moved by an electromagnetic coil 29, and the on-off valve 23 is opened.
Open and close.
【0021】25はバーナ16の燃焼量を可変する燃焼
量可変装置、26は開閉弁23、温度検知器14、燃焼
量可変装置25に電気的に接続された制御装置である。Reference numeral 25 denotes a combustion amount varying device for varying the combustion amount of the burner 16, and 26 denotes a control device electrically connected to the on-off valve 23, the temperature detector 14, and the combustion amount varying device 25.
【0022】上記構成において、開閉弁23の開閉動作
とバーナ16での燃焼、送風機17の運転により冷媒加
熱による熱搬送の暖房を行なう。ここで冷媒の流れは、
開閉弁23が閉状態の時に、ガス冷媒が放熱器10で凝
縮液化し過冷却となった液冷媒が液冷媒戻り管13から
第2逆止弁12を介して受液部19に流入し、このガス
冷媒を凝縮させることにより受液部19内の圧力が低下
し、急激に受液部19へ液冷媒が流入する。In the above configuration, heating of heat transfer by refrigerant heating is performed by opening / closing operation of the on-off valve 23, combustion by the burner 16, and operation of the blower 17. Here, the flow of the refrigerant is
When the on-off valve 23 is closed, the gas refrigerant is condensed and liquefied in the radiator 10 and the supercooled liquid refrigerant flows into the liquid receiving portion 19 from the liquid refrigerant return pipe 13 through the second check valve 12, By condensing the gas refrigerant, the pressure in the liquid receiving portion 19 decreases, and the liquid refrigerant rapidly flows into the liquid receiving portion 19.
【0023】この受液部19内が液冷媒で満液状態にな
ると液冷媒の流れは停止する。そこで、開閉弁23を開
とすると、受液部19と気液セパレータ液溜部20とは
連通して均圧状態となり、受液部19内の液冷媒は重力
により開閉弁23を通り気液セパレータ液溜部20内へ
流入する。この時、同時に受液部19の液冷媒と置換す
る気液セパレータ液溜部20のガス冷媒は、開閉弁23
を通り受液部19へと流れる。When the inside of the liquid receiving section 19 is filled with the liquid refrigerant, the flow of the liquid refrigerant stops. Therefore, when the on-off valve 23 is opened, the liquid receiving part 19 and the gas-liquid separator liquid reservoir 20 communicate with each other to be in a pressure equalized state, and the liquid refrigerant in the liquid receiving part 19 passes through the on-off valve 23 due to gravity to be gas-liquid. It flows into the separator liquid reservoir 20. At this time, the gas refrigerant in the gas-liquid separator liquid reservoir 20, which is simultaneously replaced with the liquid refrigerant in the liquid receiver 19,
And flows to the liquid receiving portion 19.
【0024】次に、受液部19内の液冷媒が全て流れた
時、開閉弁23を再び閉にすると、受液部19が瞬時に
減圧され低圧となり、受液部19内に放熱器10の凝縮
過冷却した液冷媒が吸引され、受液部19が液冷媒で満
たされるサイクルを繰り返す。Next, when the liquid refrigerant in the liquid receiving portion 19 has completely flowed, when the on-off valve 23 is closed again, the liquid receiving portion 19 is instantaneously reduced in pressure to a low pressure, and the radiator 10 is placed in the liquid receiving portion 19. The cycle in which the condensed and supercooled liquid refrigerant is sucked and the liquid receiving portion 19 is filled with the liquid refrigerant is repeated.
【0025】ここで、従来例にある均圧管9を無くし、
開閉弁23から液冷媒の落下と同時にガス冷媒が置換す
る様に開閉弁23の口径を大きくすることにより最短の
長さとなり、落込み管7は仕切り板21に直接開閉弁2
3を取付けたことにより最短となる。そのため、この開
閉弁23を流れるガス冷媒と液冷媒の流路抵抗は小さく
なり、開閉弁23が開成と同時に満液となった受液部の
液冷媒はガス冷媒と置換し気液セパレータ液溜部20へ
大量に落し込まれる。Here, the pressure equalizing tube 9 in the conventional example is eliminated,
By increasing the diameter of the on-off valve 23 so that the gas refrigerant is replaced at the same time as the liquid refrigerant falls from the on-off valve 23, the length becomes the shortest.
3 is the shortest. Therefore, the flow path resistance between the gas refrigerant and the liquid refrigerant flowing through the on-off valve 23 is reduced, and the liquid refrigerant in the liquid receiving part, which becomes full at the same time as the on-off valve 23 is opened, is replaced with the gas refrigerant and the gas-liquid separator liquid is stored. It is dropped into the unit 20 in large quantities.
【0026】従って、流路抵抗を小さくすることがで
き、開閉弁23の開時間TONを大幅に短縮できる。この
ため、受液部19での液冷媒の吸引・落込み回数の増加
により冷媒循環能力が増大し、冷媒加熱器2での燃焼量
増大させ熱搬送量(暖房に利用の場合は暖房能力)の大
能力化ができる。Therefore, the flow path resistance can be reduced, and the opening time T ON of the on-off valve 23 can be greatly reduced. For this reason, the refrigerant circulation capacity increases due to an increase in the number of times the liquid refrigerant is sucked and dropped in the liquid receiving section 19, and the amount of combustion in the refrigerant heater 2 increases, and the heat transfer amount (heating capacity in the case of use for heating). Can be increased.
【0027】さらに、容器18を上部の受液部19と下
部の気液セパレータ液溜部20に仕切り板21により仕
切り、気液セパレート機能と冷媒の液溜機能を合わせ持
つ気液セパレータ液溜部20とした。このため、上部で
気液セパレートした冷媒の液はただちに下部の液溜の溜
るため、気液セパレート性能が向上し循環路24の渇き
度が高く顕熱比が大きいため熱搬送量が増大し、このこ
とと、液冷媒がただちに気液セパレータ液溜部20に溜
るため充填冷媒量が少なくて運転できる。Further, the container 18 is partitioned into an upper liquid receiving part 19 and a lower gas-liquid separator liquid storage part 20 by a partition plate 21, and has a gas-liquid separator liquid storage part having both a gas-liquid separation function and a refrigerant liquid storage function. 20. For this reason, the liquid of the refrigerant gas-liquid separated in the upper part immediately accumulates in the liquid reservoir in the lower part, so that the gas-liquid separation performance is improved, the degree of thirst of the circulation path 24 is high, and the sensible heat ratio is large, so that the heat transfer amount is increased. In addition, since the liquid refrigerant is immediately stored in the gas-liquid separator liquid storage section 20, the operation can be performed with a small amount of the charged refrigerant.
【0028】また、図4に示す本発明の別の実施例は、
容器18の外に開閉弁23を取付け、この開閉弁23の
おのおのを受液部19と気液セパレータ液溜部20に連
通してある。この構成においても、前記実施例と同じ作
用、効果があり、開閉弁23の取付けが容易であり、交
換補修が簡単に出来る。Another embodiment of the present invention shown in FIG.
An on-off valve 23 is mounted outside the container 18, and each of the on-off valves 23 communicates with a liquid receiving part 19 and a gas-liquid separator liquid storage part 20. Also in this configuration, the same operation and effect as those of the above-described embodiment are obtained, the on-off valve 23 is easily mounted, and replacement and repair can be easily performed.
【0029】また、図5に示す本発明の別の実施例は、
仕切り板21に開閉弁の代わりにスプリング30で閉弁
する逆止弁31を有し、この逆止弁31を強制的に開弁
する手段としてピン32を動かす電磁弁33、この電磁
弁33の動作を制御部26を設けてある。そして、逆止
弁31近傍の受液部19に、この受液部19の上端近傍
と連通する置換連通管34を設けた。受液部19内が液
冷媒で満液状態になり、電磁弁33の動作で逆止弁31
を開とすると、受液部19内の液冷媒は重力により逆止
弁31を通り気液セパレータ液溜部20内へ流入する。
この時、同時に受液部19の液冷媒と置換する気液セパ
レータ液溜部20のガス冷媒は、逆止弁31を通り受液
部19へと流れる。この時、逆止弁31近傍の受液部1
9に上端近傍と連通する置換連通管34を設けたため、
置換するガス冷媒はこの置換連通管34内を通り受液部
19の上部に流れ、逆止弁31を液冷媒が流下するのと
を分離でき、受液部19内の液冷媒がより短時間で全て
流れ落ちる。また、逆止弁31は、電磁弁33の開閉動
作で開動作の時は開弁し、閉動作の時は受液部19に液
冷媒の無い時のみ閉弁する。すなわち、閉動作の時、受
液部19に液冷媒のが有ると、重力で逆止弁31が開き
液冷媒が落下する。受液部19に液冷媒が無くなるとス
プリング30の力で瞬時に閉弁する。そのため、受液部
19が瞬時に減圧され低圧となり、受液部19内に放熱
器10の凝縮過冷却した液冷媒が吸引され、受液部19
が液冷媒で満たされるサイクルを繰り返す。このよう
に、各サイクルで受液部19の液冷媒は完全に置換でき
るため、1サイクルの搬送冷媒量は、受液部19の容積
と同じ最大量を保つことができ、受液部19での液冷媒
の吸引・落込み回数の増加と最大容量の維持により冷媒
循環能力が増大し大能力化ができる。Another embodiment of the present invention shown in FIG.
The partition plate 21 has a check valve 31 that is closed by a spring 30 instead of an open / close valve, and a solenoid valve 33 that moves a pin 32 as means for forcibly opening the check valve 31. The operation is provided with a control unit 26. Then, a replacement communication pipe 34 communicating with the vicinity of the upper end of the liquid receiver 19 is provided in the liquid receiver 19 near the check valve 31. The inside of the liquid receiving portion 19 is filled with the liquid refrigerant, and the check valve 31 is operated by the operation of the solenoid valve 33.
Is opened, the liquid refrigerant in the liquid receiving section 19 flows into the gas-liquid separator liquid storing section 20 through the check valve 31 by gravity.
At this time, the gas refrigerant in the gas-liquid separator liquid reservoir 20 that simultaneously displaces the liquid refrigerant in the liquid receiver 19 flows to the liquid receiver 19 through the check valve 31. At this time, the liquid receiving part 1 near the check valve 31
9 is provided with the replacement communication pipe 34 communicating with the vicinity of the upper end,
The gas refrigerant to be replaced flows through the replacement communication pipe 34 to the upper part of the liquid receiving portion 19, and can be separated from the flow of the liquid refrigerant through the check valve 31. All run down. The check valve 31 opens when the solenoid valve 33 is opened and closed, and when closed, closes only when there is no liquid refrigerant in the liquid receiving portion 19. That is, at the time of the closing operation, if there is liquid refrigerant in the liquid receiving portion 19, the check valve 31 opens by gravity and the liquid refrigerant drops. When the liquid refrigerant in the liquid receiving portion 19 is exhausted, the valve is instantly closed by the force of the spring 30. Therefore, the liquid receiving section 19 is instantaneously decompressed to a low pressure, and the condensed and supercooled liquid refrigerant of the radiator 10 is sucked into the liquid receiving section 19 and the liquid receiving section 19 is sucked.
Is repeated with the liquid refrigerant. As described above, the liquid refrigerant in the liquid receiving portion 19 can be completely replaced in each cycle, so that the amount of the refrigerant transferred in one cycle can be maintained at the same maximum amount as the volume of the liquid receiving portion 19. By increasing the number of suctions and drops of the liquid refrigerant and maintaining the maximum capacity, the circulation capacity of the refrigerant is increased and the capacity can be increased.
【0030】また、出口管4の気液セパレータ液溜部2
0との連通部35と、循環路24の気液セパレータ液溜
部20との接続部36の間に、複数の開口部37を有す
る板38を設けることにより、冷媒加熱器2から連通部
35に流れる気液混合冷媒は板38に仕切られ、液冷媒
は下の液溜部に溜りガス冷媒は開口部37から接続部3
6を通り循環路24へと流れる。このため、より一層、
気液セパレート性能が向上し熱搬送量が増大するととも
に、逆止弁31からの冷媒の落下等により液溜部の液冷
媒が波うち乱れた場合も、気液セパレート性能は維持で
きる。The gas-liquid separator liquid reservoir 2 of the outlet pipe 4
In addition, a plate 38 having a plurality of openings 37 is provided between the communication part 35 for connecting the refrigerant heater 2 and the connection part 36 for connecting the gas-liquid separator liquid storage part 20 of the circulation path 24 to the communication part 35. The gas-liquid mixed refrigerant flowing to the liquid refrigerant is partitioned by a plate 38, the liquid refrigerant is stored in a lower liquid storage part, and the gas refrigerant is supplied from the opening 37 to the connection part 3.
6 to the circulation path 24. For this reason,
The gas-liquid separation performance is improved, the heat transfer amount is increased, and the gas-liquid separation performance can be maintained even when the liquid refrigerant in the liquid reservoir is disturbed by the drop of the refrigerant from the check valve 31 or the like.
【0031】そして、仕切り板21を下に凸状に形成
し、仕切り板21の最下端部に開閉弁31を設けること
により、開閉弁31を開き受液部19内の液冷媒を重力
により逆止弁31を通り気液セパレータ液溜部20内へ
流入する時、受液部19の底を形成する仕切り板21が
下方に凸状になり、この仕切り板21の最下端部に逆止
弁31を設けてあるため、この凸状に沿って液冷媒が流
れて逆止弁31から気液セパレータ液溜部20内へ流入
するため、液冷媒が完全に受液部19から気液セパレー
タ液溜部20に落ちる時間がさらに短くなる。従って、
開閉弁31の開時間TONをより短縮でき、受液部19で
の液冷媒の吸引・落込み回数の増加により冷媒循環能力
が増大し大能力化ができる。The partition plate 21 is formed to be convex downward, and an on-off valve 31 is provided at the lowermost end of the partition plate 21 to open the on-off valve 31 to reverse the liquid refrigerant in the liquid receiving portion 19 by gravity. When flowing into the gas-liquid separator liquid reservoir 20 through the stop valve 31, the partition plate 21 forming the bottom of the liquid receiving portion 19 becomes convex downward, and a check valve is provided at the lowermost end of the partition plate 21. Since the liquid refrigerant flows along the convex shape and flows into the gas-liquid separator liquid reservoir 20 from the check valve 31, the liquid refrigerant completely flows from the liquid receiver 19 to the gas-liquid separator liquid. The time for falling into the reservoir 20 is further reduced. Therefore,
The opening time T ON of the on-off valve 31 can be further reduced, and the number of times the liquid refrigerant is sucked and dropped in the liquid receiving section 19 increases the refrigerant circulation capacity, thereby increasing the capacity.
【0032】また、図4に示ように、仕切り板21の上
部にテフロン、ナイロン等の樹脂を成型した断熱材39
を設ける構成として、受液部19と気液セパレータ液溜
部20を断熱している。開閉弁31が閉状態の時に、放
熱器10で凝縮液化し過冷却となった液冷媒が液冷媒戻
り管13から第2逆止弁12を介して受液部19に流入
し、このガス冷媒を凝縮させる時、受液部19も冷却し
ている。この時、気液セパレータ液溜部20は高温の飽
和冷媒であるから、熱は、気液セパレータ液溜部20か
ら受液部19へ流れる。これを断熱材39で断熱する事
により受液部19の温度上昇を防止でき、過冷却冷媒に
よる受液部19内のガス冷媒が凝縮し圧力が低下する時
間が短縮し、早く受液部19への液冷媒の流入が完了す
る。このため、開閉弁31の閉時間TOFFを短縮でき、
受液部19での液冷媒の吸引・落込み回数の増加によ
り、さらに大能力化ができる。As shown in FIG. 4, a heat insulating material 39 made of resin such as Teflon or nylon is formed on the upper part of the partition plate 21.
Is provided, the liquid receiving part 19 and the gas-liquid separator liquid storing part 20 are insulated. When the on-off valve 31 is in the closed state, the liquid refrigerant condensed and liquefied by the radiator 10 and supercooled flows from the liquid refrigerant return pipe 13 into the liquid receiving portion 19 via the second check valve 12, and the gas refrigerant Is condensed, the liquid receiving part 19 is also cooled. At this time, since the gas-liquid separator liquid reservoir 20 is a high-temperature saturated refrigerant, heat flows from the gas-liquid separator liquid reservoir 20 to the liquid receiver 19. By insulating this with the heat insulating material 39, the temperature rise of the liquid receiving part 19 can be prevented, the time for the gas refrigerant in the liquid receiving part 19 to be condensed by the supercooled refrigerant and the pressure is reduced, and the liquid receiving part 19 is quickly reduced. The flow of the liquid refrigerant into the refrigerant is completed. Therefore, the closing time T OFF of the on- off valve 31 can be reduced,
The capacity can be further increased by increasing the number of times the liquid refrigerant is sucked and dropped in the liquid receiving section 19.
【0033】なお、駆動入力は変化無く、熱搬送のため
の入力としては開閉弁31の入力のみであり経済性は変
わらない。また、受液部19と気液セパレート機能と液
溜機能を合わせ持つ気液セパレータ液溜部20を一つの
容器18で構成したため部品点数が少なくなり、またこ
のためロー付け箇所の減少になり信頼性が向上し、かつ
コンパクト、低コストとなる。また、従来の開閉弁8と
第1逆止弁6を一つの開閉弁31で構成できるため、部
品が少なく、かつロー付け箇所の減少になり、受液部1
9のシール部が開閉弁31の1箇所であるため、リーク
が半減し信頼性も向上する。The drive input does not change, and the only input for heat transfer is the input of the on-off valve 31, so that the economic efficiency does not change. In addition, since the liquid receiving portion 19 and the gas-liquid separator liquid storing portion 20 having both the gas-liquid separating function and the liquid storing function are constituted by one container 18, the number of parts is reduced, and the number of brazing points is reduced, so that reliability is reduced. Performance, compactness and low cost. Further, since the conventional on-off valve 8 and the first check valve 6 can be constituted by one on-off valve 31, the number of parts is reduced, the number of brazing points is reduced, and the liquid receiving part 1 is reduced.
Since the seal portion 9 is one portion of the on-off valve 31, the leak is reduced by half and the reliability is improved.
【0034】[0034]
【発明の効果】以上のように本発明の熱搬送装置は、冷
媒加熱器、この冷媒加熱器の上方に配設された容器、前
記容器内を上部の受液部と下部の気液セパレータ液溜部
に仕切る仕切り板、前記冷媒加熱器と前記気液セパレー
タ液溜部を連通する入口管と出口管、前記仕切り板に開
閉弁を有する熱搬送部と、前記気液セパレータ液溜部、
放熱器および前記受液部を順次接続した環状の循環路
と、前記開閉弁の開閉を行う制御部からなる構成として
いるので以下の効果がある。As described above, the heat transfer device of the present invention comprises a refrigerant heater, a container disposed above the refrigerant heater, and an upper liquid receiving portion and a lower gas-liquid separator liquid in the container. A partition plate that partitions into a reservoir, an inlet pipe and an outlet pipe that communicate the refrigerant heater and the gas-liquid separator liquid reservoir, a heat transfer unit having an on-off valve in the partition plate, and the gas-liquid separator liquid reservoir;
The following effects can be obtained because the radiator and the liquid receiving unit are sequentially connected to each other, and the control unit performs opening and closing of the on-off valve.
【0035】(1)均圧管を無くし、開閉弁から液冷媒
の落下と同時にガス冷媒が置換する様に開閉弁の口径を
大きくし、落込み管は仕切り板に直接開閉弁を取付けた
ことにより、この均圧管と落し込み管の流路抵抗を小さ
くすることができ、開閉弁の開時間を大幅に短縮による
熱搬送量の大能力化を得ることができる。(1) Eliminating the equalizing pipe, increasing the diameter of the on-off valve so that the gas refrigerant is replaced at the same time as the liquid refrigerant drops from the on-off valve, and the dropping pipe is provided with the on-off valve directly attached to the partition plate. The flow resistance of the pressure equalizing pipe and the dropping pipe can be reduced, and the opening time of the on-off valve can be greatly shortened, thereby increasing the heat transfer capacity.
【0036】(2)容器を上部の受液部と下部の気液セ
パレータ液溜部に仕切る仕切り板により構成し、落込み
管は前記仕切り板に開閉弁を取付けたことにより、受液
部と気液セパレート機能と液溜機能を合わせ持つ気液セ
パレータ液溜部を一つの容器で構成でき部品点数が少な
くなり、またこのためロー付け箇所の減少し信頼性が向
上し、かつコンパクト、低コストとなる。(2) The container is constituted by a partition plate for partitioning an upper liquid receiving portion and a lower gas-liquid separator liquid reservoir portion. The liquid reservoir of the gas-liquid separator, which has both the gas-liquid separation function and the liquid storage function, can be composed of one container, and the number of parts is reduced, and therefore the number of parts to be brazed is reduced, reliability is improved, and compactness and low cost are achieved. Becomes
【0037】(3)そして、開閉弁と第1逆止弁を一つ
の開閉弁で構成できるため、部品が少なく、かつロー付
け箇所の減少になり、受液部のシール部が開閉弁1箇所
であるため、リークによる信頼性も向上する。(3) Since the on-off valve and the first check valve can be constituted by one on-off valve, the number of parts is reduced and the number of brazing points is reduced, and the sealing portion of the liquid receiving part is provided by one on-off valve. Therefore, reliability due to leakage is also improved.
【0038】(4)また、駆動入力は変化無く、熱搬送
のための入力としては開閉弁の入力のみであり経済性は
変わらない。(4) The drive input does not change, and the input for the heat transfer is only the input of the on-off valve, so that the economic efficiency does not change.
【0039】(5)逆止弁の受液部に受液部の上端近傍
と連通する置換連通管を設けたことにより、受液部の液
冷媒と置換する置換するガス冷媒はこの置換連通管内を
通り受液部の上部に流れるため、受液部内の液冷媒がよ
り短時間で全て流れ落ち、開時間を大幅に短縮による熱
搬送量の大能力化を得ることができる。(5) By providing the replacement communication pipe communicating with the vicinity of the upper end of the liquid receiving section in the liquid receiving section of the check valve, the gas refrigerant to be replaced with the liquid refrigerant in the liquid receiving section is replaced in the replacement communication pipe. Therefore, all the liquid refrigerant in the liquid receiving section flows down in a shorter time, and the opening time can be greatly shortened, thereby increasing the heat transfer capacity.
【0040】(6)仕切り板に逆止弁を有し、この逆止
弁を強制的に開弁する手段を設けたことにより、各サイ
クルで受液部の液冷媒は完全に置換でき、1サイクルの
搬送冷媒量は、最大量を保つことができ、液冷媒の吸引
・落込み回数の増加と最大容量の維持により冷媒循環能
力が増大し大能力化ができる。(6) Since the partition plate has a check valve and the means for forcibly opening the check valve is provided, the liquid refrigerant in the liquid receiving section can be completely replaced in each cycle. The maximum amount of refrigerant conveyed in the cycle can be maintained, and the refrigerant circulation capacity can be increased and the capacity can be increased by increasing the number of suctions and drops of the liquid refrigerant and maintaining the maximum capacity.
【0041】(7)さらに、仕切り板を下方に凸状に形
成し、この仕切り板の最下端部に逆止弁を設けることに
より、この凸状に沿って液冷媒が流れ、液冷媒が受液部
から落ちる時間が短くなる。また、仕切り板の上部また
は下部に断熱材を設ける構成として、受液部と気液セパ
レータ液溜部を断熱し受液部の温度上昇を防止すること
により、ガス冷媒が凝縮し圧力が低下する時間が短縮
し、このため、開閉弁の閉時間TOFFを短縮でき、さら
に大能力化ができる。(7) Further, the partition plate is formed in a convex shape downward, and a check valve is provided at the lowermost end of the partition plate, so that the liquid refrigerant flows along the convex shape and receives the liquid refrigerant. The time to drop from the liquid part is shorter. In addition, as a configuration in which a heat insulating material is provided on the upper or lower part of the partition plate, the liquid receiving portion and the gas-liquid separator liquid reservoir are insulated to prevent the temperature of the liquid receiving portion from rising, whereby the gas refrigerant is condensed and the pressure is reduced. As a result, the closing time T OFF of the on- off valve can be shortened, and the capacity can be further increased.
【0042】(8)そして、連通部と、接続部の間に、
開口部を有する板を設けることにより、気液混合冷媒の
液冷媒は下の液溜部に溜りガス冷媒は循環路へと流れる
ため、気液セパレート性能が向上し熱搬送量が増大し、
変動に対しても気液セパレート性能は維持できる。(8) Then, between the communicating part and the connecting part,
By providing a plate having an opening, the liquid refrigerant of the gas-liquid mixed refrigerant collects in the lower liquid reservoir and the gas refrigerant flows to the circulation path, so that the gas-liquid separation performance is improved and the heat transfer amount is increased,
The gas-liquid separation performance can be maintained even with fluctuations.
【0043】(9)また、この断熱材を下方に凸状に形
成し、断熱材の最下端部に対応する仕切り板に逆止弁を
設けることにより、液冷媒が受液部から落ちる時間が短
くなり、開閉弁の開時間TONを短縮でき、冷媒循環能力
が増大し大能力化ができる。(9) By forming the heat insulating material in a downwardly convex shape and providing a check valve on a partition plate corresponding to the lowermost end of the heat insulating material, the time required for the liquid refrigerant to fall from the liquid receiving portion is reduced. As a result, the opening time T ON of the on-off valve can be shortened, the refrigerant circulation capacity can be increased, and the capacity can be increased.
【図1】本発明の一実施例の熱搬送装置のシステム構成
図FIG. 1 is a system configuration diagram of a heat transfer device according to an embodiment of the present invention.
【図2】従来の熱搬送装置のシステム構成図FIG. 2 is a system configuration diagram of a conventional heat transfer device.
【図3】従来の熱搬送装置での受液器の減圧特性図FIG. 3 is a decompression characteristic diagram of a liquid receiver in a conventional heat transfer device.
【図4】本発明の他の実施例の熱搬送装置のシステム構
成図FIG. 4 is a system configuration diagram of a heat transfer device according to another embodiment of the present invention.
【図5】本発明の他の実施例の熱搬送装置のシステム構
成図FIG. 5 is a system configuration diagram of a heat transfer device according to another embodiment of the present invention.
2 冷媒加熱器 3 入口管 4 出口管 10 放熱器 12 第2逆止弁 18 容器 19 受液部 20 気液セパレータ液溜部 21 仕切り板 22 熱搬送部 23 開閉弁 24 循環路 26 制御部 31 逆止弁 34 置換連通管 2 Refrigerant heater 3 Inlet pipe 4 Outlet pipe 10 Radiator 12 Second check valve 18 Container 19 Liquid receiving part 20 Gas-liquid separator liquid storage part 21 Partition plate 22 Heat transfer part 23 Open / close valve 24 Circulation path 26 Control part 31 Reverse Stop valve 34 Displacement communication pipe
───────────────────────────────────────────────────── フロントページの続き (72)発明者 垰 統雄 大阪府門真市大字門真1006番地 松下電 器産業株式会社内 (56)参考文献 特開 昭60−30991(JP,A) 特開 平3−156218(JP,A) 特開 平5−288427(JP,A) (58)調査した分野(Int.Cl.6,DB名) F24D 7/00 F04C 23/02──────────────────────────────────────────────────続 き Continued on the front page (72) Norio Tao, Inventor 1006 Kazuma Kadoma, Kadoma, Osaka Prefecture Matsushita Electric Industrial Co., Ltd. (56) References JP-A-60-30991 (JP, A) JP-A-3 -156218 (JP, A) JP-A-5-288427 (JP, A) (58) Fields investigated (Int. Cl. 6 , DB name) F24D 7/00 F04C 23/02
Claims (6)
置された上部の受液部と下部の気液セパレータ液溜部に
仕切る仕切り板を内部に有する容器と、前記冷媒加熱器
と前記気液セパレータ液溜部を連通する入口管と出口管
と、前記仕切り板に開閉弁を有する熱搬送部と、前記気
液セパレータ液溜部、放熱器および前記受液部を順次接
続した環状の循環路と、前記開閉弁の開閉を行う制御部
からなる熱搬送装置。A container having therein a refrigerant heater, a partition plate for partitioning an upper liquid receiving portion and a lower gas-liquid separator liquid reservoir portion disposed above the refrigerant heater, and the refrigerant heater; An inlet pipe and an outlet pipe communicating with the gas-liquid separator liquid reservoir, a heat transfer unit having an on-off valve in the partition plate, an annular shape in which the gas-liquid separator liquid reservoir, a radiator and the liquid receiver are sequentially connected. And a control unit for opening and closing the on-off valve.
強制的に開弁する手段と、この手段の動作の指示を行う
制御部を設けた請求項1記載の熱搬送装置。2. A heat transfer apparatus according to claim 1, further comprising a check valve disposed on the partition plate, means for forcibly opening the check valve, and a control unit for instructing the operation of the check valve. apparatus.
連通する置換連通管を設けた請求項1記載の熱搬送装
置。3. The heat transfer device according to claim 1, wherein a replacement communication pipe communicating with the vicinity of the upper end of the liquid receiving portion is provided in the liquid receiving portion of the on-off valve.
た請求項1記載の熱搬送装置。4. The heat transfer device according to claim 1, wherein a heat insulating material is provided above or below the partition plate.
り板の最下端部に開閉弁を設けた請求項1記載の熱搬送
装置。5. The heat transfer device according to claim 1, wherein the partition plate is formed to be convex downward, and an on-off valve is provided at a lowermost end of the partition plate.
と、循環路の気液セパレータ液溜部との接続部の間に、
開口部を有する板を設けた請求項1記載の熱搬送装置。6. An outlet pipe between a communicating portion with the gas-liquid separator liquid reservoir and a connecting portion of the circulation path with the gas-liquid separator liquid reservoir.
The heat transfer device according to claim 1, further comprising a plate having an opening.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10807793A JP2827809B2 (en) | 1993-05-10 | 1993-05-10 | Heat transfer device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10807793A JP2827809B2 (en) | 1993-05-10 | 1993-05-10 | Heat transfer device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH06323559A JPH06323559A (en) | 1994-11-25 |
| JP2827809B2 true JP2827809B2 (en) | 1998-11-25 |
Family
ID=14475296
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10807793A Expired - Lifetime JP2827809B2 (en) | 1993-05-10 | 1993-05-10 | Heat transfer device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2827809B2 (en) |
-
1993
- 1993-05-10 JP JP10807793A patent/JP2827809B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH06323559A (en) | 1994-11-25 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CA2160659C (en) | Heat transfer apparatus and methods for solid-vapor sorption systems | |
| US4381798A (en) | Combination reversing valve and expansion device for a reversible refrigeration circuit | |
| JP2827809B2 (en) | Heat transfer device | |
| JP3252530B2 (en) | Heat transfer device | |
| JP3252529B2 (en) | Heat transfer device | |
| JP3254838B2 (en) | Heat transfer device | |
| US5533669A (en) | Heat transfer apparatus | |
| JP2827863B2 (en) | Heat transfer device | |
| JPH07158872A (en) | Heat carrier | |
| JP3428302B2 (en) | Heating and cooling machine | |
| JP3252577B2 (en) | Heat transfer device | |
| JP2689663B2 (en) | Heating system | |
| JP2827928B2 (en) | Heat transfer device | |
| JPH0712360A (en) | Heat carrier | |
| JP2827931B2 (en) | Heat transfer device | |
| JP3684708B2 (en) | Heating and cooling machine | |
| JP2789894B2 (en) | heater | |
| JPH07174351A (en) | Heat carrier | |
| JPH07174353A (en) | Heat carrier | |
| JPH07174350A (en) | Heat carrier | |
| JPH07174354A (en) | Heat carrier | |
| JPH06117653A (en) | Heat carrier | |
| JP3399025B2 (en) | Heat transfer device | |
| JPH0791679A (en) | Heat carrier | |
| JPH06117652A (en) | Heat carrier |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080918 Year of fee payment: 10 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080918 Year of fee payment: 10 |
|
| S801 | Written request for registration of abandonment of right |
Free format text: JAPANESE INTERMEDIATE CODE: R311801 |
|
| ABAN | Cancellation of abandonment | ||
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Year of fee payment: 10 Free format text: PAYMENT UNTIL: 20080918 |
|
| R350 | Written notification of registration of transfer |
Free format text: JAPANESE INTERMEDIATE CODE: R350 |