JPH0712362A - Heat conveyor - Google Patents
Heat conveyorInfo
- Publication number
- JPH0712362A JPH0712362A JP15185893A JP15185893A JPH0712362A JP H0712362 A JPH0712362 A JP H0712362A JP 15185893 A JP15185893 A JP 15185893A JP 15185893 A JP15185893 A JP 15185893A JP H0712362 A JPH0712362 A JP H0712362A
- Authority
- JP
- Japan
- Prior art keywords
- receiver
- gas
- liquid separator
- medium
- separator
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Central Heating Systems (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、媒体を加熱し無動力熱
搬送方式で暖房運転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 device which heats a medium to perform heating operation by a non-powered heat transfer method.
【0002】[0002]
【従来の技術】従来この種の熱搬送装置は、図3に示す
ように、媒体加熱器1の上方に配設したレシーバ2の中
間位置に気液セパレータ3を配設し、前記レシーバ2
と、前記気液セパレータ3の間に両者を均圧させる開閉
弁4を有し、さらにレシーバ2と、気液セパレータ3の
間の配管内にメッシュフィルター5と第1逆止弁6を設
けている。媒体加熱器1で蒸発した媒体は、室内熱交換
器7で凝縮され、第2逆止弁8を介しレシーバ2へ流入
される。レシーバ2に液媒体が溜まると、開閉弁4を開
き、レシーバ2と気液セパレータ3を均圧化し、レシー
バ2の液媒体をメッシュフィルター5と第1逆止弁6を
介し、気液セパレータ3に流入させる。流入し終わると
開閉弁4を閉じ第1逆止弁6も閉じるため、再び室内熱
交換器7から凝縮された液媒体がレシーバ2に流入され
る。このような動作を繰り返して媒体による熱搬送を行
い、暖房運転を行うようになっていた。2. Description of the Related Art Conventionally, as shown in FIG. 3, a heat transfer device of this type has a gas-liquid separator 3 disposed at an intermediate position between a receiver 2 disposed above a medium heater 1 and the receiver 2
And an open / close valve 4 for equalizing the pressure between the gas-liquid separator 3 and a mesh filter 5 and a first check valve 6 in the pipe between the receiver 2 and the gas-liquid separator 3. There is. The medium evaporated in the medium heater 1 is condensed in the indoor heat exchanger 7 and flows into the receiver 2 via the second check valve 8. When the liquid medium accumulates in the receiver 2, the on-off valve 4 is opened, the receiver 2 and the gas-liquid separator 3 are pressure-equalized, and the liquid medium of the receiver 2 is passed through the mesh filter 5 and the first check valve 6 to make the gas-liquid separator 3 Flow into. When the inflow is completed, the on-off valve 4 is closed and the first check valve 6 is also closed, so that the liquid medium condensed from the indoor heat exchanger 7 is again flowed into the receiver 2. Such an operation is repeated to carry the heat by the medium to perform the heating operation.
【0003】[0003]
【発明が解決しようとする課題】しかしながら、上記の
ような構成では次のような課題を有していた。However, the above-mentioned structure has the following problems.
【0004】レシーバ2に溜まった液媒体を気液セパレ
ータ3内の静圧成分と均圧させて重力差で流出させるた
め、開閉弁4の開時間を長く設定しなければならず、媒
体循環量G(g/sec)、開閉弁4の周期(開時間T0+閉時
間T1)をTとすると、 G=V×γ/T (V:レシーバ容積(cc)) (γ:レシーバ内液媒体密度(g/cc)) からTが大きくなると、Gが減少し大きな熱搬送量が得
られない。Since the liquid medium accumulated in the receiver 2 is equalized with the static pressure component in the gas-liquid separator 3 and flows out due to the difference in gravity, the opening time of the on-off valve 4 must be set long and the medium circulation amount Let G (g / sec) and the cycle of the on-off valve 4 (open time T 0 + close time T 1 ) be T: G = V × γ / T (V: receiver volume (cc)) (γ: liquid in receiver When T increases from the medium density (g / cc), G decreases and a large heat transfer amount cannot be obtained.
【0005】レシーバ2と気液セパレータ3間の配管内
に、第1逆止弁6を保護するメッシュフィルター5があ
り、特に配管内壁と近接する周方向を通過する際の抵抗
が大きく、流入時間を短くし、大きな熱搬送量を得るに
は、単純にレシーバ2をさらに上方に位置させ、液面を
高くする必要があり、レシーバ2と気液セパレータ3間
の高さが大きくなり機器全体が大きくなる。In the pipe between the receiver 2 and the gas-liquid separator 3, there is a mesh filter 5 which protects the first check valve 6, and in particular, the resistance when passing in the circumferential direction close to the inner wall of the pipe is large and the inflow time is long. In order to shorten the temperature and obtain a large amount of heat transfer, it is necessary to simply position the receiver 2 further upward and raise the liquid level, which increases the height between the receiver 2 and the gas-liquid separator 3 and growing.
【0006】本発明は、上記従来の課題を解決するもの
で、開閉弁が開の時、レシーバの液媒体をより短時間で
気液セパレータに流入させることにより、より大きな熱
搬送量を得るとともに、レシーバと気液セパレータの高
さ方向の構成を小形コンパクトにすることを目的とす
る。The present invention solves the above-mentioned conventional problems. When the on-off valve is opened, the liquid medium of the receiver is introduced into the gas-liquid separator in a shorter time, thereby obtaining a larger heat transfer amount. , The receiver and the gas-liquid separator are intended to be compact and compact in the height direction.
【0007】[0007]
【課題を解決するための手段】上記目的を達成するため
に、本発明の熱搬送装置は、媒体加熱器と、この媒体加
熱器の上方に配設した気液セパレータと、この気液サパ
レータのさらに上方に配設したレシーバと、前記気液セ
パレータ頂部と前記レシーバを室内熱交換器を介して配
管し、さらに前記レシーバと気液セパレータの間に配設
した開閉弁と、前記レシーバとメッシュフィルターを介
して気液セパレータ頂部に配管した第1逆止弁とからな
り、前記メッシュフィルターは、レシーバ容器内に臨ま
せてなるものである。In order to achieve the above object, the heat transfer device of the present invention comprises a medium heater, a gas-liquid separator disposed above the medium heater, and a gas-liquid separator. A receiver arranged further above, the gas-liquid separator top and the receiver are piped through an indoor heat exchanger, and an on-off valve arranged between the receiver and the gas-liquid separator, the receiver and a mesh filter. And a first check valve piped to the top of the gas-liquid separator via the mesh filter, and the mesh filter faces the inside of the receiver container.
【0008】[0008]
【作用】本発明は、上記した構成によって、メッシュフ
ィルターの面積が大きくとれ、開閉弁を開にしてレシー
バ内に溜まった液媒体の流出時、メッシュフィルターを
通過する際の抵抗を最も少なくすることができるため、
レシーバから完全に液媒体が気液セパレータへ流入する
までの時間短縮が図れ、大きな熱搬送量が得られる。
又、気液セパレータ内に必要な最短距離で流入すること
ができるため、レシーバと気液セパレータの高さ方向の
構成を小形コンパクトにすることができる。According to the present invention, the area of the mesh filter can be made large by the above construction, and the resistance when passing through the mesh filter when the liquid medium accumulated in the receiver is opened by opening the on-off valve is minimized. Because you can
The time required for the liquid medium to completely flow into the gas-liquid separator from the receiver can be shortened, and a large amount of heat transfer can be obtained.
Further, since the gas can flow into the gas-liquid separator in the required shortest distance, the configuration of the receiver and the gas-liquid separator in the height direction can be made compact and compact.
【0009】[0009]
【実施例】以下、本発明の一実施例を図面にもとづいて
説明する。尚、図3と同一部材には同一番号を付してあ
る。DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings. The same members as those in FIG. 3 are designated by the same reference numerals.
【0010】図1、図2において、1は、媒体加熱器
で、この媒体加熱器1の上方にはレシーバ2、さらにこ
のレシーバ2と前記媒体加熱器1の中間位置には、気液
セパレータ3が配設されている。前記レシーバ2容器内
には、略水平状態にメッシュフィルター5が取り付けら
れている。前記気液セパレータ3の頂部には、接続口A
9と、前記レシーバ2の底部を、第1逆止弁6を介し接
続する接続口B10と、室内熱交換器7の一端と接続配
管する接続口C11を有し、底部には、接続口D12と
接続口E13を有している。前記気液セパレータ3と媒
体加熱器1とは、前記媒体加熱器1の底部と接続口D1
2とを接続する加熱器入口管14と、前記媒体加熱器1
の頂部と接続管E13とを接続する加熱器出口管15と
でループ状に接続してあり、前記加熱器出口管15は、
前記気液セパレータ3内へ挿入するとともに、先端開口
部は、前記接続口A9の下方に位置させてある。前記レ
シーバ2の頂部には、接続口A9からの均圧管16を開
閉弁4を介し接続する接続口F17と、前記室内熱交換
器7の他端と第2逆止弁8を介し接続する接続口G18
を設けてある。In FIGS. 1 and 2, 1 is a medium heater, a receiver 2 is provided above the medium heater 1, and a gas-liquid separator 3 is provided at an intermediate position between the receiver 2 and the medium heater 1. Is provided. A mesh filter 5 is attached in a substantially horizontal state inside the receiver 2 container. The top of the gas-liquid separator 3 has a connection port A
9, a connection port B10 for connecting the bottom portion of the receiver 2 via the first check valve 6, and a connection port C11 for connecting and piping one end of the indoor heat exchanger 7, and a connection port D12 at the bottom portion. And a connection port E13. The gas-liquid separator 3 and the medium heater 1 are connected to the bottom of the medium heater 1 and the connection port D1.
2 is connected to the heater inlet pipe 14, and the medium heater 1
Is connected in a loop with a heater outlet pipe 15 connecting the top part of the heater and the connecting pipe E13, and the heater outlet pipe 15 is
The tip end opening is located below the connection port A9 while being inserted into the gas-liquid separator 3. At the top of the receiver 2, a connection port F17 for connecting the pressure equalizing pipe 16 from the connection port A9 through the opening / closing valve 4, and a connection for connecting the other end of the indoor heat exchanger 7 through the second check valve 8. Mouth G18
Is provided.
【0011】上記構成において、媒体加熱器1で加熱さ
れた媒体は、2相状態で加熱器出口管15を通り、気液
セパレータ3内に流入し、ここで液媒体は、気液セパレ
ータ3内に落下し、再び加熱器入口管14を通って媒体
加熱器1に流入する。一方、気液セパレータ3内に媒体
加熱器1から流入した2相状態のガス媒体は、接続口C
11から室内熱交換器7に圧送され、熱交換して凝縮液
化する。この時、開閉弁4が閉の時は、第1逆止弁6は
閉状態で、レシーバ2へ室内熱交換器7からの過冷却液
媒体が第2逆止弁8を通り圧送され、レシーバ2内のガ
ス媒体が凝縮液化し、レシーバ2内の圧力が急激に低下
し、室内熱交換器7の過冷却液媒体がレシーバ2内へ引
き込まれ、レシーバ2内は、室内熱交換器7からの凝縮
液媒体で満たされる。この状態で開閉弁4を開にする
と、レシーバ2と気液セパレータ3とは均圧状態とな
り、レシーバ2内の液媒体は、メッシュフィルター5と
第1逆止弁6を通り、気液セパレータ3に流入する。こ
の時、第2逆止弁8は閉状態である。In the above structure, the medium heated by the medium heater 1 flows into the gas-liquid separator 3 through the heater outlet pipe 15 in a two-phase state, where the liquid medium is the gas-liquid separator 3. To the medium heater 1 again through the heater inlet pipe 14. On the other hand, the gas medium in the two-phase state that has flowed into the gas-liquid separator 3 from the medium heater 1 has a connection port C.
It is pressure-fed from 11 to the indoor heat exchanger 7 and exchanges heat to be condensed and liquefied. At this time, when the on-off valve 4 is closed, the first check valve 6 is closed, and the supercooled liquid medium from the indoor heat exchanger 7 is pressure-fed to the receiver 2 through the second check valve 8 and The gas medium in 2 is condensed and liquefied, the pressure in the receiver 2 is rapidly reduced, the supercooled liquid medium in the indoor heat exchanger 7 is drawn into the receiver 2, and the inside of the receiver 2 is separated from the indoor heat exchanger 7. Filled with the condensate medium. When the on-off valve 4 is opened in this state, the receiver 2 and the gas-liquid separator 3 are in a pressure equalized state, and the liquid medium in the receiver 2 passes through the mesh filter 5 and the first check valve 6 and passes through the gas-liquid separator 3 Flow into. At this time, the second check valve 8 is closed.
【0012】次に開閉弁4を閉にすると、第1逆止弁6
も閉となり、再びレシーバ2に室内熱交換器7から過冷
却液媒体が流入し、レシーバ2を凝縮液媒体で満たし、
開閉弁4を開にするというサイクルを繰り返す。すなわ
ち、気液セパレータ3と媒体加熱器1の間は自然循環サ
イクル、気液セパレータ3、室内熱交換器7、第2逆止
弁8、レシーバ2、第1逆止弁6のサイクルは、レシー
バ2へ室内熱交換器7からの過冷却液媒体を溜めて、そ
れを間歇的に気液セパレータ3に供給するという間欠動
作サイクルである。Next, when the on-off valve 4 is closed, the first check valve 6
Also closes, the supercooled liquid medium flows into the receiver 2 again from the indoor heat exchanger 7, and fills the receiver 2 with the condensed liquid medium,
The cycle of opening the on-off valve 4 is repeated. That is, the natural circulation cycle between the gas-liquid separator 3 and the medium heater 1, the cycle of the gas-liquid separator 3, the indoor heat exchanger 7, the second check valve 8, the receiver 2, and the first check valve 6 is the receiver. 2 is an intermittent operation cycle in which the supercooled liquid medium from the indoor heat exchanger 7 is stored in the space 2 and is intermittently supplied to the gas-liquid separator 3.
【0013】ここで、第1逆止弁6をごみ等から保護す
るメッシュフィルター5は、前記レシーバ2容器内に大
きな面積で臨ませており、言わば全面積を液媒体が通過
するため、液媒体の流出時、メッシュフィルター5を通
過する際の抵抗を、従来よりはるかに少なくすることが
できる。その結果、レシーバ2から完全に液媒体が気液
セパレータ3へ流入するまでの時間短縮がなされ、より
大きな熱搬送量を得ることができる。Here, the mesh filter 5 for protecting the first check valve 6 from dust and the like is made to face the inside of the container of the receiver 2 with a large area. When flowing out, the resistance when passing through the mesh filter 5 can be made much smaller than in the conventional case. As a result, the time until the liquid medium completely flows into the gas-liquid separator 3 from the receiver 2 is shortened, and a larger heat transfer amount can be obtained.
【0014】又、気液セパレータ3内へ最短距離で流出
することができるため、レシーバ2と気液セパレータ3
の高さ方向の構成を小形コンパクトにすることができ
る。Further, since the gas can flow out into the gas-liquid separator 3 in the shortest distance, the receiver 2 and the gas-liquid separator 3 can be discharged.
The configuration in the height direction of can be made compact and compact.
【0015】[0015]
【発明の効果】以上の実施例で説明したように本発明の
熱搬送装置によれば、次の効果が得られる。As described in the above embodiments, the heat transfer device of the present invention has the following effects.
【0016】(1)第1逆止弁を保護するメッシュフィ
ルターを、レシーバ容器内に大きな面積で臨ませてお
り、言わば全面積を液媒体が通過するため、液媒体の流
出時、メッシュフィルターを通過する際の抵抗を最も少
なくすることができるので、液媒体がレシーバから気液
セパレータへ流入するまでの時間短縮がなされ、より大
きな熱搬送量を得ることができる。(1) The mesh filter for protecting the first check valve is made to face a large area inside the receiver container. In other words, the liquid medium passes through the entire area. Since the resistance when passing through can be minimized, the time until the liquid medium flows from the receiver to the gas-liquid separator is shortened, and a larger heat transfer amount can be obtained.
【0017】(2)又、通過抵抗が最も少ないので、気
液セパレータ内へ最短距離で流入出することができるた
め、レシーバと気液セパレータの高さ方向の構成を小形
コンパクトにすることができる。(2) Further, since the passage resistance is the smallest, the gas can flow into and out of the gas-liquid separator in the shortest distance, so that the constitution of the receiver and the gas-liquid separator in the height direction can be made compact and compact. .
【図1】本発明の一実施例における熱搬送装置の回路構
成図FIG. 1 is a circuit configuration diagram of a heat transfer device according to an embodiment of the present invention.
【図2】同要部断面図FIG. 2 is a sectional view of the same main part.
【図3】従来の熱搬送装置の回路構成図FIG. 3 is a circuit configuration diagram of a conventional heat transfer device.
1 媒体加熱器 2 レシーバ 3 気液セパレータ 4 開閉弁 5 メッシュフィルター 6 第1逆止弁 7 室内熱交換器 1 Medium Heater 2 Receiver 3 Gas-Liquid Separator 4 Open / Close Valve 5 Mesh Filter 6 First Check Valve 7 Indoor Heat Exchanger
Claims (1)
設した気液セパレータと、この気液サパレータのさらに
上方に配設したレシーバと、前記気液セパレータ頂部と
前記レシーバを室内熱交換器を介して配管し、さらに前
記レシーバと気液セパレータの間に配設した開閉弁と、
前記レシーバとメッシュフィルターを介して気液セパレ
ータ頂部に配管した第1逆止弁とからなり、前記メッシ
ュフィルターは、レシーバ容器内に臨ませてなる熱搬送
装置。1. A medium heater, a gas-liquid separator disposed above the medium heater, a receiver disposed further above the gas-liquid separator, a top portion of the gas-liquid separator and the receiver for indoor heat. An on-off valve, which is piped through an exchanger, is arranged between the receiver and the gas-liquid separator,
A heat transfer device comprising the receiver and a first check valve that is piped to the top of the gas-liquid separator through a mesh filter, and the mesh filter faces the inside of the receiver container.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15185893A JPH0712362A (en) | 1993-06-23 | 1993-06-23 | Heat conveyor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15185893A JPH0712362A (en) | 1993-06-23 | 1993-06-23 | Heat conveyor |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0712362A true JPH0712362A (en) | 1995-01-17 |
Family
ID=15527795
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP15185893A Pending JPH0712362A (en) | 1993-06-23 | 1993-06-23 | Heat conveyor |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0712362A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US11260416B2 (en) | 2012-05-15 | 2022-03-01 | Eyenovia, Inc. | Ejector devices, methods, drivers, and circuits therefor |
-
1993
- 1993-06-23 JP JP15185893A patent/JPH0712362A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US11260416B2 (en) | 2012-05-15 | 2022-03-01 | Eyenovia, Inc. | Ejector devices, methods, drivers, and circuits therefor |
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