JPS60126545A - Refrigeration cycle - Google Patents
Refrigeration cycleInfo
- Publication number
- JPS60126545A JPS60126545A JP23392283A JP23392283A JPS60126545A JP S60126545 A JPS60126545 A JP S60126545A JP 23392283 A JP23392283 A JP 23392283A JP 23392283 A JP23392283 A JP 23392283A JP S60126545 A JPS60126545 A JP S60126545A
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- boiling point
- container
- valve
- refrigeration cycle
- 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.)
- Granted
Links
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〔発明の技術分野〕
この発明は、非共沸混合冷媒を用いた冷凍サイクルの改
良に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to an improvement in a refrigeration cycle using a non-azeotropic mixed refrigerant.
2つの温度を設定できるように非共沸混合冷媒を使用し
たいわゆる2温度コントロール冷凍サイクルの従来例と
して例えば特願昭58−70954号が提案されている
。As a conventional example of a so-called two-temperature control refrigeration cycle using a non-azeotropic mixed refrigerant so that two temperatures can be set, for example, Japanese Patent Application No. 1987-70954 has been proposed.
この例では、通常の使用温度に設定する時は、冷媒を冷
媒容器内において低沸点成分の多い冷媒ガスと高沸点成
分の多い冷媒液とに分離させて高沸点成分の多い冷媒液
を回路に流すようなされており、急速冷凍等のため低い
方の温度に設定しよざ
うとする時には、分1ずに封入した混合比で冷凍サイク
ルを構成していた。In this example, when setting the normal operating temperature, the refrigerant is separated into a refrigerant gas containing many low-boiling components and a refrigerant liquid containing many high-boiling components in the refrigerant container, and the refrigerant liquid containing many high-boiling components is sent to the circuit. When it was desired to set a lower temperature for rapid freezing, etc., the refrigeration cycle was configured with the mixed ratio sealed without mixing.
従って、通常の使用温度を設定するには低沸点成分の多
い冷媒ガスを容器内に蓄える必要がhD、この容器に非
常に大きな容積のものを必要とした。Therefore, in order to set the normal operating temperature, it is necessary to store a refrigerant gas containing many low boiling point components in a container, which requires a very large capacity.
第1図はこの従来例を示すもので、図において(1)は
圧縮機、(2)は凝縮器、13 a)、(30は減圧装
置、(4)は蒸発器、(5)は電磁弁6(6)は冷媒容
器である。Figure 1 shows a conventional example of this. Valve 6 (6) is a refrigerant container.
通常の運転においては電磁弁(5)を開き凝縮器(2)
にて冷却された非共沸混合冷媒のうち一力は減圧装置(
3α)を通って蒸発器(4ンに流れ込むが、他力の冷媒
は鶏9磁弁(5)を通って冷媒容器(6)に流れ、ここ
で低沸点成分の多い冷媒ガスと高沸点成分の多い冷媒液
とに分離され、低沸点成分の多い冷媒ガスは冷媒容器の
上方に蓄えられ、高沸点成分の多い冷媒′le1.Vi
、冷媒容器(6)の下方より減圧装置(3b)に流れる
。従って回路内には高沸点成分の多い冷媒が流れること
から蒸発器(4)の温度は比較的高い温度に設定される
。During normal operation, open the solenoid valve (5) and open the condenser (2).
One of the non-azeotropic mixed refrigerants cooled in the depressurizer (
The refrigerant flows through the evaporator (4) through the evaporator (3α), but the external refrigerant flows through the magnetic valve (5) to the refrigerant container (6), where it separates the refrigerant gas containing many low-boiling components and the high-boiling components. The refrigerant gas containing many low-boiling components is stored above the refrigerant container, and the refrigerant gas containing many high-boiling components is
, flows from below the refrigerant container (6) to the pressure reducing device (3b). Therefore, the temperature of the evaporator (4) is set to a relatively high temperature because a refrigerant containing many high boiling point components flows in the circuit.
次に電磁弁(5)を閉じた時には冷媒容器(6)内は低
圧となり、今まで蓄えられていた低沸点成分の多い冷媒
ガスは冷媒容器(6)内よりはき出され、封入した混合
比、すなわち低沸点成分の多い冷媒ガスが回路を循環す
ることから蒸発器(4)の温度は低くか、通常の運転時
、低沸点成分の多い冷媒ガスを冷媒容器(6)の中に蓄
えなければならず非常に太きな容積の耐圧容器が必要で
あった。Next, when the solenoid valve (5) is closed, the pressure inside the refrigerant container (6) becomes low, and the refrigerant gas containing many low boiling point components that has been stored up to now is expelled from the inside of the refrigerant container (6), and the mixture ratio of the sealed mixture is changed. In other words, since the refrigerant gas containing many low boiling point components circulates through the circuit, the temperature of the evaporator (4) must be low, or the refrigerant gas containing many low boiling point components must be stored in the refrigerant container (6) during normal operation. Therefore, a pressure-resistant container with an extremely large capacity was required.
この発明は、冷媒容器の上端と下端に夫々上方弁と下方
弁を設け、上方弁を開、下方弁を閉としたとき、冷媒容
器内に高沸点冷媒の多い冷媒液を蓄えることによシ低沸
点冷媒の多い冷媒ガスを回路に流し、急速冷凍を行うも
のである。This invention provides an upper valve and a lower valve at the upper and lower ends of a refrigerant container, respectively, and when the upper valve is opened and the lower valve is closed, a refrigerant liquid containing a high boiling point refrigerant is stored in the refrigerant container. A refrigerant gas containing a large amount of low boiling point refrigerant is passed through the circuit to perform rapid freezing.
第2図はこの発明の一実施例を示す冷媒回路図である。 FIG. 2 is a refrigerant circuit diagram showing one embodiment of the present invention.
図において、(1)は圧縮機、(2CL)は主凝縮器、
(2b)は副凝縮器、(3)は減圧装置、(4)は蒸発
器、(5α)、(5b)は電磁弁よりなる上刃弁と下方
弁、(7)は冷媒容器である。In the figure, (1) is a compressor, (2CL) is a main condenser,
(2b) is a sub-condenser, (3) is a pressure reducing device, (4) is an evaporator, (5α) and (5b) are an upper blade valve and a lower valve consisting of electromagnetic valves, and (7) is a refrigerant container.
通常の運転においては上方弁(5a)を閉じ、下方弁(
5b)を開くことによって主凝縮器(2α)にて冷却さ
れた非共沸混合冷媒ガスは配管(8)を通り、冷媒容器
(7)に上方から入シ冷媒容器(7)の下端に設けられ
た配管(9)及び下方弁(5b)を通って副凝縮器(2
b)に流れ、封入時の混合比で非共沸混合冷媒は冷媒回
路を流れる。During normal operation, the upper valve (5a) is closed and the lower valve (5a) is closed.
5b), the non-azeotropic mixed refrigerant gas cooled in the main condenser (2α) passes through the pipe (8) and enters the refrigerant container (7) from above. The sub condenser (2) passes through the pipe (9) and the lower valve (5b).
b), and the non-azeotropic mixed refrigerant flows through the refrigerant circuit at the mixing ratio at the time of sealing.
一方低温を要するときには、上方弁(5a)を開き下方
弁(5b)を閉じることによって、主凝縮器(2(L)
にて冷却された冷媒ガスは冷媒容器(7)の中で低沸点
成分の多い冷媒ガスと高沸点成分の多い冷媒液とに分離
され、冷媒液は冷媒容器(7)の下部に蓄えられる。一
方低沸点成分の多い冷媒ガスは冷媒容器(7)の上端に
設けられた配管α1、上方弁(5α)を通って副I#:
縮器(2b)に流れることから冷媒回路には低沸点成分
の多い冷媒が流れることになシ低温が得られる。On the other hand, when low temperature is required, the upper valve (5a) is opened and the lower valve (5b) is closed.
The cooled refrigerant gas is separated into a refrigerant gas containing many low boiling point components and a refrigerant liquid containing many high boiling point components in the refrigerant container (7), and the refrigerant liquid is stored in the lower part of the refrigerant container (7). On the other hand, the refrigerant gas containing many low boiling point components passes through the pipe α1 provided at the upper end of the refrigerant container (7) and the upper valve (5α) to the sub I#:
Since the refrigerant flows to the condenser (2b), a refrigerant containing many low boiling point components flows into the refrigerant circuit, thereby obtaining a low temperature.
す、上h9、明したごとく、従来例では意図した温度に
対し、不要とする冷媒ガスを気体の状態で蓄えていたの
に対し、この発明では液体の状態で蓄えるようにしたの
で、容器の大きさを著しく小さくすることができる効果
がある。As mentioned above, in the conventional example, the unnecessary refrigerant gas was stored in a gaseous state at the intended temperature, but in this invention, it is stored in a liquid state, so the container This has the effect of significantly reducing the size.
第1図は従来例の冷媒回路図、第2図はこの発明の一実
施例を示す冷媒回路図である。
図において、(1)は圧縮機、(2)は凝縮器、(2(
L’)は主凝縮器、(2b)は副凝縮器、(3入(3α
)、(3b)は減圧装置、(4)は蒸発器、(5)、(
5a)、(5b)は電磁弁、(6L (7)は冷媒容器
である。
なお、図中同一符号は同一または相当部分を示すものと
する。FIG. 1 is a refrigerant circuit diagram of a conventional example, and FIG. 2 is a refrigerant circuit diagram showing an embodiment of the present invention. In the figure, (1) is a compressor, (2) is a condenser, (2(
L') is the main condenser, (2b) is the sub-condenser, (3-in (3α
), (3b) are pressure reducing devices, (4) are evaporators, (5), (
5a) and (5b) are electromagnetic valves, and (6L (7) is a refrigerant container. The same reference numerals in the figures indicate the same or corresponding parts.
Claims (1)
器の上端及び下端に夫々上方弁と下方弁とを介して副凝
縮器を接続し、この副凝縮器、減圧装置及び蒸発器を経
て上記圧縮機に接続してなる冷媒回路を備え、冷媒ガス
として非共沸混合冷媒を使用し、通常の冷凍サイクル時
に上記上方弁を閉、下方弁を開にし℃非共沸混合冷媒と
して封入した混合比□で冷凍サイクルを形成し、急速冷
凍時に上記上方弁を開、下方弁を閉とし、上”記冷媒容
器内で高沸点冷媒の多い冷媒液と低沸点冷媒の多い冷媒
カスとを分離させ、高沸点冷媒の多い冷媒液を上記冷媒
容器の下部に蓄え、低沸点冷媒の多い冷媒カスが上記回
路内を流れるようにしたことを牛[徴とする冷凍サイク
ル。A compressor, a main condenser, and a refrigerant container are connected in sequence, and a sub-condenser is connected to the upper and lower ends of the refrigerant container via an upper valve and a lower valve, respectively, and the sub-condenser, a pressure reducing device, and an evaporator are connected to each other. The refrigerant circuit is connected to the compressor through the refrigerant circuit, and a non-azeotropic mixed refrigerant is used as the refrigerant gas. During a normal refrigeration cycle, the upper valve is closed and the lower valve is opened to seal in the non-azeotropic mixed refrigerant at °C. A refrigeration cycle is formed with the mixture ratio □, and during rapid freezing, the above-mentioned upper valve is opened and the lower valve is closed, and the refrigerant liquid containing a high boiling point refrigerant and the refrigerant scum containing a low boiling point refrigerant are separated in the above-mentioned refrigerant container. A refrigeration cycle characterized by separating the refrigerant liquid containing a high boiling point refrigerant and storing it in the lower part of the refrigerant container, and allowing the refrigerant scum containing a low boiling point refrigerant to flow through the circuit.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23392283A JPH0247672B2 (en) | 1983-12-12 | 1983-12-12 | REITOSAIKURU |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23392283A JPH0247672B2 (en) | 1983-12-12 | 1983-12-12 | REITOSAIKURU |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60126545A true JPS60126545A (en) | 1985-07-06 |
JPH0247672B2 JPH0247672B2 (en) | 1990-10-22 |
Family
ID=16962698
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP23392283A Expired - Lifetime JPH0247672B2 (en) | 1983-12-12 | 1983-12-12 | REITOSAIKURU |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0247672B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1150076A2 (en) * | 2000-04-26 | 2001-10-31 | Denso Corporation | Refrigerant cycle system |
US6698236B2 (en) | 2002-03-22 | 2004-03-02 | Denso Corporation | Refrigerant cycle system and condenser |
-
1983
- 1983-12-12 JP JP23392283A patent/JPH0247672B2/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1150076A2 (en) * | 2000-04-26 | 2001-10-31 | Denso Corporation | Refrigerant cycle system |
EP1150076A3 (en) * | 2000-04-26 | 2002-02-06 | Denso Corporation | Refrigerant cycle system |
US6427480B1 (en) | 2000-04-26 | 2002-08-06 | Denso Corporation | Refrigerant cycle system |
US6698236B2 (en) | 2002-03-22 | 2004-03-02 | Denso Corporation | Refrigerant cycle system and condenser |
Also Published As
Publication number | Publication date |
---|---|
JPH0247672B2 (en) | 1990-10-22 |
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