JPH0827005B2 - Heating system - Google Patents
Heating systemInfo
- Publication number
- JPH0827005B2 JPH0827005B2 JP15712188A JP15712188A JPH0827005B2 JP H0827005 B2 JPH0827005 B2 JP H0827005B2 JP 15712188 A JP15712188 A JP 15712188A JP 15712188 A JP15712188 A JP 15712188A JP H0827005 B2 JPH0827005 B2 JP H0827005B2
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- refrigerant
- gas
- receiver
- liquid 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.)
- Expired - Fee Related
Links
- 238000010438 heat treatment Methods 0.000 title claims description 14
- 239000007788 liquid Substances 0.000 claims description 98
- 239000003507 refrigerant Substances 0.000 claims description 81
- 230000005484 gravity Effects 0.000 description 5
- 230000007423 decrease Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000013526 supercooled liquid Substances 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 238000004781 supercooling Methods 0.000 description 1
Landscapes
- Central Heating Systems (AREA)
Description
【発明の詳細な説明】 産業上の利用分野 本発明は冷媒を加熱し無動力熱搬送方式で暖房運転す
る暖房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 heating device that heats a refrigerant and performs heating operation by a non-powered heat transfer system.
従来の技術 従来のこの種の暖房装置は第2図に示すように冷媒加
熱器1より上方に位置した受液器2の中間位置に気液分
離器3を配設し前記受液器2と前記気液分離器3の間に
両者を均圧させる開閉弁4を有しさらに受液器2と気液
分離器3の間に逆止弁5を有する構成を有し、冷媒加熱
器1で蒸発した冷媒は放熱器6で凝縮し受液器2へ流入
する。受液器2へ液冷媒が溜ると開閉弁4を開き受液器
2と気液分離器3とを均圧化し受液器2の液冷媒を気液
分離器3へ流入させる。流入し終わると開閉弁4を閉じ
逆止弁5も閉じるため再び放熱器6から凝縮した液冷媒
が受液器2へ流入する。このような動作を繰り返して熱
搬送を行ない暖房運転を行なうようになっていた。(例
えば実開昭61-43679号公報) 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気液分離器と受液
器の間に均圧管を有する開閉弁を設けているため受液器
に溜った液冷媒を開閉弁を開にして気液分離器へ流入さ
せる際、静圧成分のみで均圧させて液冷媒自体の重力作
用で流入させるため、開閉弁の開時間を長く設定しなけ
ればならず、冷媒循環量G(g/sec)、開閉弁の周期
(開時間T0+閉時間T1)をTとすると G=V×γ/T(受液器容積(cc)、受液器内液冷媒密
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という課題を有していた。2. Description of the Related Art In a conventional heating device of this type, as shown in FIG. 2, a gas-liquid separator 3 is arranged at an intermediate position of a liquid receiver 2 located above a refrigerant heater 1 and the liquid receiver 2 is provided. The refrigerant heater 1 has a structure in which an opening / closing valve 4 for equalizing the pressure of the both is provided between the gas-liquid separator 3 and a check valve 5 is further provided between the liquid receiver 2 and the gas-liquid separator 3. The evaporated refrigerant is condensed by the radiator 6 and flows into the liquid receiver 2. When the liquid refrigerant collects in the liquid receiver 2, the on-off valve 4 is opened and the liquid receiver 2 and the gas-liquid separator 3 are pressure-equalized so that the liquid refrigerant in the liquid receiver 2 flows into the gas-liquid separator 3. When the inflow is completed, the on-off valve 4 is closed and the check valve 5 is also closed, so that the liquid refrigerant condensed from the radiator 6 again flows into the liquid receiver 2. By repeating such operations, heat transfer is performed to perform heating operation. (For example, Japanese Utility Model Laid-Open No. 61-43679) Problem to be Solved by the Invention However, in the above-mentioned configuration, since the on-off valve having the pressure equalizing pipe is provided between the gas-liquid separator and the liquid receiver, the liquid receiver When the liquid refrigerant that has accumulated in the liquid refrigerant flows into the gas-liquid separator by opening the on-off valve, it equalizes only with the static pressure component and flows by the gravity action of the liquid refrigerant itself, so the opening time of the on-off valve should be set long. If the refrigerant circulation amount G (g / sec) and the on-off valve cycle (opening time T 0 + closing time T 1 ) are T, then G = V × γ / T (receiver volume (cc), From the liquid refrigerant density (g / cc) in the receiver, there is a problem that when T increases, G decreases and a large heat transfer amount cannot be obtained.
本発明はかかる従来の課題を解消するもので、開閉弁
が開時の時、冷媒加熱器で蒸発した冷媒の動圧成分を受
液器内へ導入し、受液器へ溜った液冷媒を、気液分離器
内へ短時間で流入させることにより、大きな熱搬送量を
得ることを目的とする。The present invention is to solve such conventional problems, when the on-off valve is open, the dynamic pressure component of the refrigerant evaporated in the refrigerant heater is introduced into the receiver, the liquid refrigerant accumulated in the receiver The purpose is to obtain a large heat transfer amount by allowing the gas to flow into the gas-liquid separator in a short time.
課題を解決するための手段 上記課題を解決するために本発明の暖房装置は、冷媒
加熱器を気液分離器より下方に配設し前記冷媒加熱器と
気液分離器とを冷媒加熱器入口管と冷媒加熱器出口管と
でループ状に配管接続する一方、前記気液分離器、放熱
器、第2逆止弁、前記気液分離器より上方に配設した受
液器、第1逆止弁、前記気液分離器を順次配管接続した
冷媒回路を有し、前記受液器と前記冷媒加熱器出口管と
の間に開閉弁を有する均圧管を設けたものである。Means for Solving the Problems In order to solve the above problems, the heating device of the present invention has a refrigerant heater arranged below a gas-liquid separator, and the refrigerant heater and the gas-liquid separator are connected to the refrigerant heater inlet. While connecting the pipe and the refrigerant heater outlet pipe in a loop, the gas-liquid separator, the radiator, the second check valve, the liquid receiver disposed above the gas-liquid separator, and the first reverse. A stop valve and a refrigerant circuit in which the gas-liquid separator is sequentially connected by piping are provided, and a pressure equalizing pipe having an opening / closing valve is provided between the liquid receiver and the refrigerant heater outlet pipe.
作用 本発明は上記した構成によって受液器へ流入した液冷
媒を開閉弁を開にして気液分離器内へ重力差で流入させ
る際、冷媒加熱器で蒸発した冷媒のもつ動圧成分が冷媒
加熱器出口管及び開閉弁を介し受液器内へ作用するた
め、重力差プラス動圧成分で受液器内へ溜った液冷媒が
気液分離器内へ完全に流入する時間の短縮化が得られ、
冷媒循環量が増加し、その結果大きな熱搬送量が得られ
る。Effect The present invention, when the liquid refrigerant that has flowed into the receiver by the above-described structure is made to flow into the gas-liquid separator by the gravity difference by opening the on-off valve, the dynamic pressure component of the refrigerant evaporated in the refrigerant heater is the refrigerant. Since it acts on the inside of the receiver via the heater outlet pipe and the on-off valve, the time required for the liquid refrigerant accumulated in the receiver due to the gravity difference plus the dynamic pressure component to completely flow into the gas-liquid separator can be shortened. Obtained,
The refrigerant circulation amount increases, and as a result, a large heat transfer amount can be obtained.
実施例 以下、本発明の実施例を添付図面にもとづいて説明す
る。なお第2図と同一部には同一番号を付してある。第
1図において1は気液分離器3より下方に配設し、冷媒
加熱入口管7、冷媒加熱出口管8とでループ状に前記気
液分離器3と接続してある冷媒加熱器、2は気液分離器
3より上方に第1逆止弁5を介し配設してある受液器、
6は放熱器であり、気液分離器3と放熱器6とはガス往
き管11、放熱器6と受液器2とは第2逆止弁9を介し、
液戻り管12とで接続され、1,8,3,7の自然循環回路と3,
6,9,2,5の冷媒循環回路を有しており、前記受液器2と
冷媒加熱器出口管8との間に開閉弁4を有する均圧管10
を配設してある。Embodiments Embodiments of the present invention will be described below with reference to the accompanying drawings. The same parts as those in FIG. 2 are designated by the same reference numerals. In FIG. 1, reference numeral 1 denotes a refrigerant heater arranged below the gas-liquid separator 3 and connected to the gas-liquid separator 3 in a loop with a refrigerant heating inlet pipe 7 and a refrigerant heating outlet pipe 8; Is a liquid receiver disposed above the gas-liquid separator 3 via the first check valve 5,
Reference numeral 6 is a radiator, the gas-liquid separator 3 and the radiator 6 are connected to each other through a gas outflow pipe 11, and the radiator 6 and the receiver 2 are connected via a second check valve 9.
Connected with the liquid return pipe 12, 1,8,3,7 natural circulation circuit and 3,
A pressure equalizing pipe 10 having a refrigerant circulation circuit of 6, 9, 2, 5 and having an opening / closing valve 4 between the liquid receiver 2 and the refrigerant heater outlet pipe 8.
Is provided.
上記構成において、冷媒加熱器1で加熱された冷媒は
冷媒加熱器出口管8を通り、2相状態で気液分離器3内
に流入し、2相冷媒の液冷媒成分は再び冷媒加熱器入口
管7を通って冷媒加熱器1へ流入する。一方気液分離器
3内に冷媒加熱器1から流入した2相冷媒のガス冷媒は
ガス往き管11を通り放熱器6で凝縮し、冷媒は過冷却状
態まで冷却される。この時開閉弁4が閉の時、第1逆止
弁5は気液分離器3内の圧力が高いため、閉状態とな
り、放熱器6で凝縮した液冷媒回路は一瞬先づまり状態
となる。過冷却液冷媒の圧力が受液器2内の圧力よりも
若干高くなると、過冷却冷媒は液戻り管12、第2逆止弁
9を通って受液器2に入る。受液器2内に入った液冷媒
は、受液器2内のガス状態の冷媒を凝縮させるので受液
器2内の圧力は急速に減圧される。例えば受液器2内に
60℃の飽和ガスが存在し、放熱器6から30℃の液冷媒
(過冷却度30deg)が受液器2へ流入すると、60℃の飽
和圧力24kg/cm2G(HCFC22)から5〜6kg/cm2受液器2
の圧力に低下する。そうすると放熱器6の液冷媒が液戻
り管12、第2逆止弁9を通って圧力の下がった受液器2
内に吸引され、受液器2内は液冷媒で満たされる。そし
て一定時間後開閉弁4を開くと、冷媒加熱器出口管8よ
り噴出する気液2相冷媒を受液器2へ導き、重力作用に
さらに冷媒加熱器出口管8からの2相冷媒の動圧成分が
加わり、受液器2内の液冷媒は短時間に第1逆止弁5を
通って気液分離器3内へ流出する。この時第2逆止弁9
は受液器2の圧力が高い為、閉状態である。次に開閉弁
4を一定時間後閉にすると第1逆止弁5は再び閉状態と
なり、受液器2内へ放熱器6から過冷却液冷媒が流入
し、受液器2内は液冷媒で満たされ、一定時間後、開閉
弁4を開にするという動作を繰返す。すなわち気液分離
器3と冷媒加熱1の間のサイクルは自然循環サイクル、
気液分離器3、放熱器6、第2逆止弁9、受液器2、第
1逆止弁5のサイクルは受液器2へ放熱器6からの液冷
媒を溜めてそれを間欠的に気液分離器3へ供給するとい
う間欠動作サイクルである。ここで開閉弁4は冷媒加熱
器出口管8と受液器2の間に均圧管10を介し配設してい
るため受液器2内へ液冷媒が溜り、開閉弁を開にして受
液器2内液冷媒を気液分離器3内へ流入させる際、受液
器2内には冷媒加熱器出口管8より噴出する気液2相冷
媒の動圧成分が重力作用以外にも加わるため、受液器2
内の液冷媒を気液分離室3内へ流出させる時間を短くす
ることができ、冷媒循環量の増大が図れ、その結果熱搬
送量のアップが図れる効果がある。In the above structure, the refrigerant heated by the refrigerant heater 1 passes through the refrigerant heater outlet pipe 8 and flows into the gas-liquid separator 3 in a two-phase state, and the liquid refrigerant component of the two-phase refrigerant is again introduced into the refrigerant heater inlet. It flows into the refrigerant heater 1 through the pipe 7. On the other hand, the gas refrigerant of the two-phase refrigerant that has flowed into the gas-liquid separator 3 from the refrigerant heater 1 passes through the gas outflow pipe 11 and is condensed by the radiator 6 to cool the refrigerant to a supercooled state. At this time, when the on-off valve 4 is closed, the first check valve 5 is closed because the pressure inside the gas-liquid separator 3 is high, and the liquid refrigerant circuit condensed by the radiator 6 is in a state of being blocked for a moment. When the pressure of the supercooled liquid refrigerant becomes slightly higher than the pressure in the liquid receiver 2, the supercooled refrigerant enters the liquid receiver 2 through the liquid return pipe 12 and the second check valve 9. Since the liquid refrigerant that has entered the liquid receiver 2 condenses the gaseous refrigerant inside the liquid receiver 2, the pressure inside the liquid receiver 2 is rapidly reduced. For example, in the receiver 2
When there is a saturated gas of 60 ° C and liquid refrigerant of 30 ° C (supercooling degree of 30deg) flows into the receiver 2 from the radiator 6, the saturation pressure of 60 ° C is 5kg to 6kg from 24kg / cm 2 G (HCFC22). / cm 2 receiver 2
To the pressure of. Then, the liquid refrigerant of the radiator 6 passes through the liquid return pipe 12 and the second check valve 9, and the pressure of the receiver 2 decreases.
The liquid is sucked in and the inside of the liquid receiver 2 is filled with the liquid refrigerant. When the on-off valve 4 is opened after a certain period of time, the gas-liquid two-phase refrigerant ejected from the refrigerant heater outlet pipe 8 is guided to the liquid receiver 2, and the movement of the two-phase refrigerant from the refrigerant heater outlet pipe 8 is further affected by gravity. A pressure component is added, and the liquid refrigerant in the liquid receiver 2 flows out into the gas-liquid separator 3 through the first check valve 5 in a short time. At this time, the second check valve 9
Is closed because the pressure of the liquid receiver 2 is high. Next, when the on-off valve 4 is closed for a certain period of time, the first check valve 5 is closed again, the supercooled liquid refrigerant flows into the receiver 2 from the radiator 6, and the inside of the receiver 2 is cooled by the liquid refrigerant. After a certain period of time, the operation of opening the on-off valve 4 is repeated. That is, the cycle between the gas-liquid separator 3 and the refrigerant heating 1 is the natural circulation cycle,
In the cycle of the gas-liquid separator 3, the radiator 6, the second check valve 9, the receiver 2 and the first check valve 5, the liquid refrigerant from the radiator 6 is accumulated in the receiver 2 and is intermittently stored. This is an intermittent operation cycle in which the gas-liquid separator 3 is supplied first. Since the on-off valve 4 is disposed between the refrigerant heater outlet pipe 8 and the liquid receiver 2 via the pressure equalizing pipe 10, liquid refrigerant accumulates in the liquid receiver 2, and the on-off valve is opened to receive the liquid. When the liquid refrigerant in the container 2 is caused to flow into the gas-liquid separator 3, the dynamic pressure component of the gas-liquid two-phase refrigerant ejected from the refrigerant heater outlet pipe 8 is added to the inside of the liquid receiver 2 in addition to the action of gravity. , Receiver 2
It is possible to shorten the time taken for the liquid refrigerant inside to flow into the gas-liquid separation chamber 3, and to increase the refrigerant circulation amount, and as a result, the heat transfer amount can be increased.
発明の効果 以上のように本発明の暖房装置によれば受液器と冷媒
加熱出口管との間に開閉弁を設け、前記開閉弁を開にし
て受液器内液冷媒を気液分離器内へ流入させる際、冷媒
加熱器で蒸発した冷媒の動圧成分を受液器内へ作用させ
るため受液器内液冷媒が完全に気液分離器内へ流入する
迄の時間の短縮化ができ、システムの熱搬送量アップが
図れる効果がある。As described above, according to the heating device of the present invention, an opening / closing valve is provided between the liquid receiver and the refrigerant heating outlet pipe, and the opening / closing valve is opened to separate the liquid refrigerant in the liquid receiver into the gas-liquid separator. When flowing into the interior, since the dynamic pressure component of the refrigerant evaporated in the refrigerant heater acts on the inside of the receiver, the time until the liquid refrigerant inside the receiver completely flows into the gas-liquid separator can be shortened. This has the effect of increasing the heat transfer amount of the system.
第1図は本発明の一実施例による暖房装置の回路構成
図、第2図は従来の暖房装置の回路構成図である。 1……冷媒加熱器、2……受液器、3……気液分離器、
4……開閉弁、5……第1逆止弁、6……放熱器、7…
…冷媒加熱器入口管、8……冷媒加熱器出口管、9……
第2逆止弁、10……均圧管。FIG. 1 is a circuit configuration diagram of a heating device according to an embodiment of the present invention, and FIG. 2 is a circuit configuration diagram of a conventional heating device. 1 ... Refrigerant heater, 2 ... Liquid receiver, 3 ... Gas-liquid separator,
4 ... on-off valve, 5 ... first check valve, 6 ... radiator, 7 ...
… Refrigerant heater inlet pipe, 8 …… Refrigerant heater outlet pipe, 9 ……
2nd check valve, 10 ... Pressure equalizing pipe.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 雀堂 純一 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (72)発明者 山口 紘一郎 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Junichi Jakudo 1006 Kadoma, Kadoma City, Osaka Prefecture Matsushita Electric Industrial Co., Ltd. (72) Koichiro Yamaguchi, 1006 Kadoma, Kadoma City, Osaka Matsushita Electric Industrial Co., Ltd.
Claims (1)
し、前記冷媒加熱器と気液分離器とを冷媒加熱器入口管
と冷媒加熱器の出口管とでループ状に配管接続する一
方、前記気液分離器、放熱器、第2逆止弁、前記気液分
離器より上方に配設した受液器、第1逆止弁、前記気液
分離器を順次配管接続した冷媒回路を有し、前記受液器
と前記冷媒加熱器出口管との間に開閉弁を有する均圧管
を設けた暖房装置。1. A refrigerant heater is disposed below a gas-liquid separator, and the refrigerant heater and the gas-liquid separator are connected in a loop by a refrigerant heater inlet pipe and a refrigerant heater outlet pipe. On the other hand, the gas-liquid separator, the radiator, the second check valve, the liquid receiver disposed above the gas-liquid separator, the first check valve, and the refrigerant in which the gas-liquid separator is sequentially connected by piping. A heating device having a circuit, wherein a pressure equalizing pipe having an opening / closing valve is provided between the liquid receiver and the refrigerant heater outlet pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15712188A JPH0827005B2 (en) | 1988-06-24 | 1988-06-24 | Heating system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15712188A JPH0827005B2 (en) | 1988-06-24 | 1988-06-24 | Heating system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH028630A JPH028630A (en) | 1990-01-12 |
| JPH0827005B2 true JPH0827005B2 (en) | 1996-03-21 |
Family
ID=15642671
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15712188A Expired - Fee Related JPH0827005B2 (en) | 1988-06-24 | 1988-06-24 | Heating system |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0827005B2 (en) |
-
1988
- 1988-06-24 JP JP15712188A patent/JPH0827005B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH028630A (en) | 1990-01-12 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |