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JPH0136025B2 - - Google Patents
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JPH0136025B2 - - Google Patents

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Publication number
JPH0136025B2
JPH0136025B2 JP57155815A JP15581582A JPH0136025B2 JP H0136025 B2 JPH0136025 B2 JP H0136025B2 JP 57155815 A JP57155815 A JP 57155815A JP 15581582 A JP15581582 A JP 15581582A JP H0136025 B2 JPH0136025 B2 JP H0136025B2
Authority
JP
Japan
Prior art keywords
refrigerant
temperature
evaporator
expansion valve
sealed
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
Application number
JP57155815A
Other languages
Japanese (ja)
Other versions
JPS5946469A (en
Inventor
Taketoshi Mochizuki
Hideyuki Kimura
Takao Chiaki
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hitachi Ltd
Original Assignee
Hitachi Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP57155815A priority Critical patent/JPS5946469A/en
Publication of JPS5946469A publication Critical patent/JPS5946469A/en
Publication of JPH0136025B2 publication Critical patent/JPH0136025B2/ja
Granted legal-status Critical Current

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  • Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
  • Devices That Are Associated With Refrigeration Equipment (AREA)

Description

【発明の詳細な説明】 〔発明の利用分野〕 本発明は、温度式自動膨張弁を備えた冷凍サイ
クルに係り、特に温度式自動膨張弁に封入する作
動媒体と冷凍サイクル内に封入する循環冷媒に関
するものである。
[Detailed Description of the Invention] [Field of Application of the Invention] The present invention relates to a refrigeration cycle equipped with a thermostatic automatic expansion valve, and particularly relates to a working medium sealed in the thermostatic automatic expansion valve and a circulating refrigerant sealed in the refrigeration cycle. It is related to.

〔従来技術〕[Prior art]

通常の冷凍装置に使用されている温度式自動膨
張弁の感温筒には、冷凍サイクルで使用している
冷媒と同一の冷媒が封入されているのが一般的で
ある。このような冷凍サイクルで、蒸発器に流入
する冷媒の分流状態や熱負荷の不均衡などにより
冷凍系統にしばしば圧力あるいは温度等の周期的
な不安定現象(以下、ハンチングという)が発生
する。従来、このハンチングを回避する手段とし
ては膨張弁の調節ばねを強めて静止スーパーヒー
トを大きくし、蒸発器のスーパーヒートを増して
蒸発器出口に設けた感温筒部の温度を安定させ膨
張弁の周期的な弁の開閉を減衰させて、ハンチン
グをとめることが行われている。しかし、このよ
うな方法では蒸発器の能力を減殺し、冷凍能力を
大幅に減少させてしまう。さらにこの方法でハン
チングが止まらないときは、膨張弁を容量の小さ
なものと交換したり、感温筒に特殊ガスを封入す
るか、あるいは特公昭47−23825で開示されてい
るように、温度変動に対する感温筒の応答速度の
時定数を変えるなどの対策が取られている。
The temperature-sensitive cylinder of a thermostatic automatic expansion valve used in ordinary refrigeration equipment is generally filled with the same refrigerant as that used in the refrigeration cycle. In such a refrigeration cycle, periodic unstable phenomena such as pressure or temperature (hereinafter referred to as hunting) often occur in the refrigeration system due to branching of the refrigerant flowing into the evaporator or imbalance in heat load. Conventionally, as a means to avoid this hunting, the adjustment spring of the expansion valve is strengthened to increase the stationary superheat, and the superheat of the evaporator is increased to stabilize the temperature of the temperature-sensitive tube provided at the evaporator outlet. Hunting is stopped by damping the periodic opening and closing of the valve. However, such a method reduces the capacity of the evaporator and significantly reduces the refrigeration capacity. Furthermore, if this method does not stop hunting, you may need to replace the expansion valve with one with a smaller capacity, fill the thermosensor with a special gas, or reduce temperature fluctuations as disclosed in Japanese Patent Publication No. 47-23825. Countermeasures have been taken, such as changing the time constant of the response speed of the thermosensor.

〔発明の目的〕[Purpose of the invention]

本発明は上記に鑑みて発明されたもので、冷凍
装置の蒸発器能力および成積係数の向上をはかる
と共に温度式自動膨張弁のハンチングを防止する
冷凍装置を提供することを目的とする。
The present invention was invented in view of the above, and an object of the present invention is to provide a refrigeration system that improves the evaporator capacity and growth coefficient of the refrigeration system, and prevents hunting of a thermostatic automatic expansion valve.

〔発明の概要〕 上記目的を達成するため本発明は、温度式自動
膨張弁の封入作動媒体として単一のフロン冷媒を
封入し、冷凍サイクルの封入循環冷媒としては上
記感熱筒封入冷媒と同冷媒を主体に、これより高
沸点の非共沸性冷媒を混合した非共沸混合冷媒を
封入したことを特徴とする。
[Summary of the Invention] In order to achieve the above object, the present invention includes a single fluorocarbon refrigerant sealed as a working medium in a thermostatic automatic expansion valve, and the same refrigerant as the heat-sensitive cylinder sealed refrigerant as the sealed circulating refrigerant in a refrigeration cycle. The refrigerant is characterized by containing a non-azeotropic mixed refrigerant consisting mainly of , and a non-azeotropic refrigerant with a higher boiling point.

ある冷媒に非共沸性の高沸点冷媒を加えると、
同一圧力条件では蒸発温度が高くなる。しかもこ
の混合冷媒の蒸発温度は一定せず、蒸発作用が進
むにつれて蒸発温度が上昇する特性がある。この
混合冷媒サイクルに、低沸点成分のみの冷媒を感
温筒に封入した温度式自動膨張弁を用いると、蒸
発器出口の過熱度を小さくすることができる。こ
のような特性を利用して冷凍サイクルには低沸点
成分の主冷媒にサイクルの運転効率を向上させる
特性をもつ非共沸高沸点冷媒を追加封入するとと
もに、温度式自動膨張弁には、感温筒に上記低沸
点成分の主冷媒のみを封入したものを用いると、
蒸発器出口の過熱度を小さくして成績係数を高め
る一方、蒸発器出口に多少液戻りしても主冷媒の
みの場合に比べて感温筒の感知温度レベルが高
く、したがつて感知温度変化が小さく押えられる
ため、ハンチングを起こしにくくすることができ
る。
When a non-azeotropic high boiling point refrigerant is added to a certain refrigerant,
Under the same pressure conditions, the evaporation temperature becomes higher. Moreover, the evaporation temperature of this mixed refrigerant is not constant, and as the evaporation action progresses, the evaporation temperature increases. If a thermostatic automatic expansion valve in which refrigerant containing only low boiling point components is sealed in a temperature-sensitive tube is used in this mixed refrigerant cycle, the degree of superheat at the evaporator outlet can be reduced. Taking advantage of these characteristics, the refrigeration cycle is additionally filled with a non-azeotropic high-boiling refrigerant that has characteristics that improve cycle operating efficiency in addition to the main refrigerant with low-boiling components, and the temperature-type automatic expansion valve is equipped with a thermostatic expansion valve. If you use a hot cylinder filled with only the main refrigerant with the above-mentioned low boiling point components,
While the degree of superheating at the evaporator outlet is reduced to increase the coefficient of performance, even if some liquid returns to the evaporator outlet, the sensing temperature level of the thermosensor tube is higher than when only the main refrigerant is used, and therefore the sensing temperature changes. Since it is held down small, hunting is less likely to occur.

〔発明の実施例〕[Embodiments of the invention]

以下本発明の一実施例を図面に基ずき説明す
る。
An embodiment of the present invention will be described below with reference to the drawings.

第1図において、1は圧縮機、2は凝縮器、3
は温度式自動膨張弁、4は蒸発器で上記各機器を
順次配管接続して冷凍サイクルが形成されてい
る。ここで、温度式自動膨張弁3の感温筒3′に
は単一成分のフロン冷媒が封入されており、また
冷凍サイクル内には感温筒内と同一冷媒を主体
に、これより高沸点の非共沸性冷媒を追加した、
いわゆる非共沸混合冷媒が封入されている。ここ
では、一例として感温筒3′にはフロン冷媒R22
が、また冷凍サイクルにはフロン冷媒R22を主体
にフロンR114がn%追加封入されている場合を
考える。この冷凍サイクルでは、圧縮機1の圧縮
作用で圧縮され高温高圧となつたガス冷媒は凝縮
器2に入り凝縮液化し、次いで膨張弁3により減
圧されて蒸発器4に導かれ、冷却作用を行う。こ
こで自らは蒸発気化し、再び圧縮機1の吸入側に
戻つて冷媒回路を形成する。冷凍サイクル内の冷
媒循環量は蒸発器4の出口配管7に取付けた感温
筒3′により制御される。蒸発器4の圧力をP0
(=一定)とすると、膨張弁3の二次側や感温筒
3′内、および蒸発器4内の冷媒の状態は、第2
図、第3図のように表わされる。第2図におい
て、曲線イはR22の飽和蒸気圧線を示し、曲線ロ
は曲線イに膨張弁の調節ばね力に相当する圧力分
を加えた圧力を示す。膨張弁3は感温筒3′の検
知温度t1による感温筒内圧力P1(A1点)、および
膨張弁3の二次側圧力P0(A0点)に調節ばね力に
相当する圧力分を加えた圧力(A0′点)がそれぞ
れ弁の開口力、止力を形成し、これが均衡するこ
とにより一定の弁開度に保持される。このとき、
冷凍サイクル内には混合冷媒が封入されているた
め、蒸発器内圧力P0(蒸発器内では圧力損失はな
く、蒸発器の入口から出口まで同一圧力P0と仮
定する。)の飽和温度は、R22の圧力P0における
飽和温度t0とは異なり、より高い値となる。した
がつて、蒸発器4出口の冷媒過熱度はt1−t0より
小さい値となる。このときの過熱度は第3図によ
り説明される。ここで曲線ハ,ニは混合冷媒R22
−R114系の圧力P0一定における飽和液線および
飽和蒸気線を示す。冷凍サイクル内に封入された
R22中のR114濃度n%の液化混合冷媒は、膨張
弁3で減圧され一部ガスを含む温度tmのxm状態
となつて蒸発器4に流入する。温度tmは、圧力
P0におけるR22の飽和温度t0より高く、R114の飽
和温度t10より低い。この冷媒は、蒸発器4内で
冷却作用し、自らは蒸発温度を上昇しながらガス
化していく。温度tgのxg状態でガス化を完了し、
以後は温度の上昇に対応してガスの過熱度を増し
ていく。今、蒸発器4の出口温度をt′g(x′g状態)
とすると、冷媒の過熱度はtg′−tgとなる。温度
t′gは前述した第2図の感温筒感知温度t1と等しい
ため、冷凍サイクル中の混合冷媒は、冷媒がR22
のみの場合の過熱度t1−t0(またはtg′−t0)に比べ
てかなり小さい。
In Fig. 1, 1 is a compressor, 2 is a condenser, and 3 is a compressor.
Reference numeral 4 indicates a thermostatic automatic expansion valve, and 4 indicates an evaporator, and a refrigeration cycle is formed by sequentially connecting each of the above-mentioned devices with piping. Here, the temperature-sensitive cylinder 3' of the thermostatic automatic expansion valve 3 is filled with a single-component fluorocarbon refrigerant, and the refrigeration cycle mainly contains the same refrigerant as in the temperature-sensitive cylinder, but with a higher boiling point than this. with the addition of a non-azeotropic refrigerant of
A so-called non-azeotropic mixed refrigerant is enclosed. Here, as an example, the thermosensor tube 3' is equipped with fluorocarbon refrigerant R22.
However, let us also consider a case where the refrigeration cycle is mainly filled with fluorocarbon refrigerant R22 and an additional n% of fluorocarbon R114. In this refrigeration cycle, gas refrigerant compressed to high temperature and high pressure by the compression action of the compressor 1 enters the condenser 2 and is condensed and liquefied.Then, the pressure is reduced by the expansion valve 3 and guided to the evaporator 4, where it performs a cooling action. . Here, it evaporates and vaporizes, and returns to the suction side of the compressor 1 to form a refrigerant circuit. The amount of refrigerant circulated within the refrigeration cycle is controlled by a temperature sensing cylinder 3' attached to the outlet pipe 7 of the evaporator 4. The pressure of evaporator 4 is P 0
(=constant), the state of the refrigerant on the secondary side of the expansion valve 3, inside the temperature sensing cylinder 3', and inside the evaporator 4 is
It is expressed as shown in Fig. 3. In FIG. 2, curve A shows the saturated vapor pressure line of R22, and curve B shows the pressure obtained by adding pressure corresponding to the adjustment spring force of the expansion valve to curve A. The expansion valve 3 corresponds to the spring force that adjusts the temperature-sensitive cylinder internal pressure P 1 (A 1 point) due to the detected temperature t 1 of the temperature-sensing cylinder 3', and the secondary side pressure P 0 (A 0 point) of the expansion valve 3. The pressure (point A 0 ') that is the sum of this pressure forms the opening force and stopping force of the valve, respectively, and when these are balanced, the valve opening is maintained at a constant degree. At this time,
Since a mixed refrigerant is sealed in the refrigeration cycle, the saturation temperature of the evaporator internal pressure P 0 (assuming there is no pressure loss in the evaporator and the same pressure P 0 from the evaporator inlet to the outlet) is , is different from the saturation temperature t 0 at the pressure P 0 of R22, and has a higher value. Therefore, the degree of superheating of the refrigerant at the outlet of the evaporator 4 has a value smaller than t 1 −t 0 . The degree of superheating at this time is explained with reference to FIG. Here, curves C and D are mixed refrigerant R22
- Shows the saturated liquid line and saturated vapor line at constant pressure P 0 of the R114 system. enclosed within the refrigeration cycle
The liquefied mixed refrigerant having an R114 concentration of n% in R22 is depressurized by the expansion valve 3 and flows into the evaporator 4 in a state xm at a temperature tm containing some gas. temperature tm pressure
Higher than the saturation temperature t 0 of R22 at P 0 and lower than the saturation temperature t 10 of R114. This refrigerant acts as a cooling agent within the evaporator 4 and gasifies itself while increasing its evaporation temperature. Gasification is completed at xg state with temperature tg,
Thereafter, the degree of superheating of the gas increases in response to the rise in temperature. Now, the outlet temperature of evaporator 4 is t′g (x′g state)
Then, the degree of superheat of the refrigerant is tg' - tg. temperature
Since t′g is equal to the sensing temperature t 1 of the thermosensor tube in Fig. 2, the refrigerant mixture in the refrigeration cycle is R22.
This is considerably smaller than the superheat degree t 1 −t 0 (or tg′−t 0 ) in the case of

このように、本実施例の冷凍サイクルでは、負
荷の変動や冷媒の分流状態の不均衡により蒸発器
出口で、なお液成分が残るようなことが起こつて
も、飽和ガス温度のtgから大幅に低下することは
ない。また、万一ハンチングを起こしても、その
幅は概略tg′−tgとなり、従来のR22100%の冷凍
サイクルの場合のtg′−t0に比べて非常に小さく押
えることができる。同時に、蒸発器の能力を減殺
することなく伝熱面積を有効に使うことができ
る。また、R22(約90%)、R114(約10%)等適当
な冷媒の組合せ、および混合割合の混合冷媒を封
入することにより成績係数を向上させることもで
きる。
In this way, in the refrigeration cycle of this embodiment, even if liquid components still remain at the evaporator outlet due to load fluctuations or imbalances in the refrigerant distribution state, the refrigeration cycle can be significantly reduced from the saturated gas temperature tg. There will be no decline. Furthermore, even if hunting should occur, its width will be approximately tg' - tg, which can be kept much smaller than tg' - t 0 in the case of a conventional R22 100% refrigeration cycle. At the same time, the heat transfer area can be used effectively without reducing the capacity of the evaporator. Furthermore, the coefficient of performance can be improved by enclosing a suitable combination of refrigerants such as R22 (approximately 90%) and R114 (approximately 10%) and a mixed refrigerant at a mixed ratio.

〔発明の結果〕[Results of the invention]

以上説明したように本発明によれば、適宜な組
合せの混合冷媒の使用と、蒸発器出口の過熱度の
低下により下記の効果を奏する。
As explained above, according to the present invention, the following effects are achieved by using an appropriate combination of mixed refrigerants and reducing the degree of superheating at the evaporator outlet.

(1) 成績係数を向上することが出来る。(1) The coefficient of performance can be improved.

(2) 蒸発器の伝熱面積を有効に利用することが出
来る。
(2) The heat transfer area of the evaporator can be used effectively.

(3) 膨張弁のハンチングを防止することが出来
る。
(3) Hunting of the expansion valve can be prevented.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は、本発明の一実施例を示す冷凍サイク
ルの構成図、第2図は、第1図に示す膨張弁の作
動状態説明図、第3図は、R22−R114系混合冷
媒の状態図である。 1……圧縮機、2……凝縮器、3……温度式自
動膨張弁、3′……感温筒、4……蒸発器。
Fig. 1 is a configuration diagram of a refrigeration cycle showing an embodiment of the present invention, Fig. 2 is an explanatory diagram of the operating state of the expansion valve shown in Fig. 1, and Fig. 3 is a state of the R22-R114 mixed refrigerant. It is a diagram. 1... Compressor, 2... Condenser, 3... Temperature-type automatic expansion valve, 3'... Temperature-sensitive cylinder, 4... Evaporator.

Claims (1)

【特許請求の範囲】 1 圧縮機、凝縮器、温度式自動膨張弁、蒸発器
を順次配管接続して冷凍サイクルを形成し、蒸発
器の出口側管路に設けられた上記温度式自動膨張
弁の感熱筒内には作動媒体として、冷媒成分とし
ては単一のフロン冷媒を封入すると共に、冷凍サ
イクル内の循環冷媒としては上記感熱筒内封入冷
媒と同冷媒を主体に、これより高沸点の非共沸性
冷媒を混合した非共沸混合冷媒を封入したことを
特徴とする冷凍装置。 2 感熱筒内封入冷媒がフロンR−22である特許
請求の範囲第1項記載の冷凍装置。 3 冷凍サイクル内封入冷媒がフロンR−22を主
体にR−114を混合した非共沸性冷媒である特許
請求の範囲第1項または第2項記載の冷凍装置。
[Scope of Claims] 1 A compressor, a condenser, a temperature-type automatic expansion valve, and an evaporator are sequentially connected via piping to form a refrigeration cycle, and the above-mentioned temperature-type automatic expansion valve is provided on the outlet side pipe of the evaporator. Inside the heat-sensitive cylinder, a single fluorocarbon refrigerant is sealed as a working medium and as a refrigerant component, and the circulating refrigerant in the refrigeration cycle is mainly the same refrigerant as the above-mentioned refrigerant sealed in the heat-sensitive cylinder. A refrigeration device characterized in that a non-azeotropic mixed refrigerant mixed with a non-azeotropic refrigerant is sealed. 2. The refrigeration system according to claim 1, wherein the refrigerant sealed in the heat-sensitive cylinder is Freon R-22. 3. The refrigeration system according to claim 1 or 2, wherein the refrigerant sealed in the refrigeration cycle is a non-azeotropic refrigerant mainly composed of Freon R-22 and mixed with R-114.
JP57155815A 1982-09-09 1982-09-09 Refrigeration equipment Granted JPS5946469A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57155815A JPS5946469A (en) 1982-09-09 1982-09-09 Refrigeration equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57155815A JPS5946469A (en) 1982-09-09 1982-09-09 Refrigeration equipment

Publications (2)

Publication Number Publication Date
JPS5946469A JPS5946469A (en) 1984-03-15
JPH0136025B2 true JPH0136025B2 (en) 1989-07-28

Family

ID=15614074

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57155815A Granted JPS5946469A (en) 1982-09-09 1982-09-09 Refrigeration equipment

Country Status (1)

Country Link
JP (1) JPS5946469A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6048469A (en) * 1983-08-25 1985-03-16 ダイキン工業株式会社 Temperature automatic expansion valve
JPH0663670B2 (en) * 1984-06-12 1994-08-22 松下電器産業株式会社 Heat pump device
JP2009156543A (en) * 2007-12-27 2009-07-16 Sanden Corp Refrigeration system

Also Published As

Publication number Publication date
JPS5946469A (en) 1984-03-15

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