JPH0247672B2 - REITOSAIKURU - Google Patents
REITOSAIKURUInfo
- Publication number
- JPH0247672B2 JPH0247672B2 JP23392283A JP23392283A JPH0247672B2 JP H0247672 B2 JPH0247672 B2 JP H0247672B2 JP 23392283 A JP23392283 A JP 23392283A JP 23392283 A JP23392283 A JP 23392283A JP H0247672 B2 JPH0247672 B2 JP H0247672B2
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- boiling point
- condenser
- container
- freezing
- 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
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
- Saccharide Compounds (AREA)
- Fats And Perfumes (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
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
(特開昭59−197762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. 70954/1982 (Japanese Patent Application Laid-open No. 197762/1982) 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
うとする時には、分離させ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 point components and a refrigerant liquid containing many high boiling point components in the refrigerant container, and the refrigerant liquid containing many high boiling point components is passed through the circuit. When trying to set the temperature, the refrigeration cycle was constructed using a mixture ratio that was sealed without separation.
従つて、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あ
り、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 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、3a,3bは減圧装
置、4は蒸発器、5は電磁弁、6は冷媒容器であ
る。 FIG. 1 shows this conventional example, in which 1 is a compressor, 2 is a condenser, 3a and 3b are pressure reducing devices, 4 is an evaporator, 5 is a solenoid valve, and 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方は減圧
装置3aを通つて蒸発器4に流れ込むが、他方の
冷媒は電磁弁5を通つて冷媒容器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
冷媒液は冷媒容器6の下方より減圧装置3bに流
れる。従つ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, the solenoid valve 5 is opened and the condenser 2
One of the cooled non-azeotropic refrigerants flows into the evaporator 4 through the pressure reducing device 3a, while the other refrigerant flows into the refrigerant container 6 through the solenoid valve 5, where it It is separated into refrigerant gas and refrigerant liquid containing many high boiling point components, the refrigerant gas containing many low boiling point components is stored above the refrigerant container, and the refrigerant liquid containing many high boiling point components 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
することができる。このように電磁弁5の操作に
より蒸発器4の温度を2段階に設定することがで
きるが、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
大きな容積の耐圧容器が必要であつた。 Next, when the electromagnetic 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 until now is discharged from the inside of the refrigerant container 6, and the mixture ratio of the sealed mixture, that is, the amount of low-boiling components is high. Since the refrigerant gas circulates through the circuit, the temperature of the evaporator 4 can be lowered. In this way, the temperature of the evaporator 4 can be set in two stages by operating the solenoid valve 5, but during normal operation, the refrigerant gas containing many low boiling point components must be stored in the refrigerant container 6, which causes an emergency. A pressure-resistant container with a 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
蓄えることにより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 the 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, thereby reducing the boiling point. A refrigerant gas containing a large amount of 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、2aは主凝縮器、2
bは副凝縮器、3は減圧装置、4は蒸発器、5
a,5bは電磁弁よりなる上方弁と下方弁、7は
冷媒容器である。 In the figure, 1 is a compressor, 2a is a main condenser, 2
b is a sub-condenser, 3 is a pressure reducing device, 4 is an evaporator, 5
A and 5b are upper and lower valves which are 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を開くことによつて主凝縮器2a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に上方から入り冷媒容器7の下端に設けら
れた配管9及び下方弁5bを通つて副凝縮器2b
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。 In normal operation, by closing the upper valve 5a and opening the lower valve 5b, the non-azeotropic mixed refrigerant gas cooled in the main condenser 2a passes through the pipe 8 and enters the refrigerant container 7 from above. 7 and the sub-condenser 2b through the lower valve 5b.
The non-azeotropic refrigerant mixture 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を閉じることによつて、主凝縮器2a
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10、上方弁5aを
通つて副凝縮器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り低温
が得られる。 On the other hand, when low temperature is required, the main condenser 2a is heated by opening the upper valve 5a and closing the lower valve 5b.
The cooled refrigerant gas is separated in the refrigerant container 7 into a refrigerant gas containing many low-boiling components and a refrigerant liquid containing many high-boiling components, 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 components flows through the pipe 10 provided at the upper end of the refrigerant container 7 and the upper valve 5a to the sub-condenser 2b, so that the refrigerant containing many low-boiling components flows into the refrigerant circuit. Low temperatures are obtained.
以上説明したごとく、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 explained 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, which significantly reduces the size of the container. It has the effect of making it smaller.
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、2aは
主凝縮器、2bは副凝縮器、3,3a,3bは減
圧装置、4は蒸発器、5,5a,5bは電磁弁、
6,7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, 2a is a main condenser, 2b is a sub-condenser, 3, 3a, 3b are pressure reducing devices, 4 is an evaporator, 5, 5a, 5b are solenoid valves,
6 and 7 are refrigerant containers. Note that the same reference numerals in the figures indicate the same or corresponding parts.
Claims (1)
入した非共沸混合冷媒を使用し、通常冷凍時には
冷媒ガスとして上記所定混合比の非共沸混合冷媒
を、急速冷凍時には上記低沸点冷媒の多い冷媒ガ
スを、それぞれ冷媒回路内に流すよう構成した冷
凍サイクルにおいて、上記冷媒回路を、圧縮機、
主凝縮器、冷媒液冷媒ガス分離用冷媒容器を順次
接続し、この冷媒容器出口側の上端及び下端に、
通常冷凍時に閉じられ急速冷凍時に開かれる上方
弁と、通常冷凍時に開かれ急速冷凍時に閉じられ
る下方弁とをそれぞれ介して副凝縮器を接続し、
さらにこの副凝縮器、減圧装置、蒸発器及び上記
圧縮機を順次接続して構成したことを特徴とする
冷凍サイクル。1. A non-azeotropic mixed refrigerant containing a high-boiling point refrigerant and a low-boiling point refrigerant at a predetermined mixing ratio is used. During normal freezing, the non-azeotropic mixed refrigerant at the above-mentioned predetermined mixing ratio is used as the refrigerant gas, and during rapid freezing, the above-mentioned low-boiling point refrigerant is used. In a refrigeration cycle configured to flow a large amount of refrigerant gas into each refrigerant circuit, the refrigerant circuit is connected to a compressor,
The main condenser, the refrigerant container for refrigerant liquid refrigerant gas separation are connected in sequence, and the upper and lower ends of the refrigerant container outlet side are
A sub-condenser is connected through an upper valve that is closed during normal freezing and opened during rapid freezing, and a lower valve that is opened during normal freezing and closed during rapid freezing, respectively;
Furthermore, a refrigeration cycle characterized in that the sub-condenser, the pressure reducing device, the evaporator, and the compressor are connected in sequence.
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 JPS60126545A (en) | 1985-07-06 |
| JPH0247672B2 true 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) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4078812B2 (en) * | 2000-04-26 | 2008-04-23 | 株式会社デンソー | Refrigeration cycle equipment |
| JP3941555B2 (en) | 2002-03-22 | 2007-07-04 | 株式会社デンソー | Refrigeration cycle apparatus and condenser |
-
1983
- 1983-12-12 JP JP23392283A patent/JPH0247672B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60126545A (en) | 1985-07-06 |
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