JPS59229155A - dryness control expansion valve - Google Patents

dryness control expansion valve

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Publication number
JPS59229155A
JPS59229155A JP10077383A JP10077383A JPS59229155A JP S59229155 A JPS59229155 A JP S59229155A JP 10077383 A JP10077383 A JP 10077383A JP 10077383 A JP10077383 A JP 10077383A JP S59229155 A JPS59229155 A JP S59229155A
Authority
JP
Japan
Prior art keywords
expansion valve
electrodes
refrigerant
evaporator
dryness
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
Application number
JP10077383A
Other languages
Japanese (ja)
Other versions
JPH0232542B2 (en
Inventor
畑田 敏夫
弘 安田
千秋 隆雄
望月 武利
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 JP10077383A priority Critical patent/JPS59229155A/en
Publication of JPS59229155A publication Critical patent/JPS59229155A/en
Publication of JPH0232542B2 publication Critical patent/JPH0232542B2/ja
Granted legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

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】 用 〔発明のオV野〕 本発明は、冷凍機、空気調和機などの冷凍装置に用いら
れる膨張弁に係り、特に、流通冷媒の乾き度を検知して
弁開度を制御する乾き度制御膨張弁に関する。
DETAILED DESCRIPTION OF THE INVENTION [Aspects of the Invention] The present invention relates to an expansion valve used in refrigeration equipment such as refrigerators and air conditioners. This invention relates to a dryness control expansion valve that controls dryness.

〔発明の背景〕[Background of the invention]

冷凍機空気調和機等の冷媒回路に設けられる膨張弁は、
蒸発器の出口側冷媒湯度を検知して、該温度が適宜な過
熱度を維持するように弁開度が調整され、冷媒流量が制
御される。
The expansion valve installed in the refrigerant circuit of refrigerators, air conditioners, etc.
The temperature of the refrigerant at the exit side of the evaporator is detected, the valve opening degree is adjusted, and the refrigerant flow rate is controlled so that the temperature is maintained at an appropriate degree of superheat.

第1図は冷凍機、空気調和機に用いられる最も基本的な
冷媒回路を示したものである。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、上記各機器は
図示の如く順次配管接続して冷媒回路が形成されている
Figure 1 shows the most basic refrigerant circuit used in refrigerators and air conditioners. 1 is a compressor, 2 is a condenser, 3 is a thermostatic automatic expansion valve, and 4 is an evaporator. The above-mentioned devices are sequentially connected through piping to form a refrigerant circuit as shown in the figure.

ガス冷媒は、圧縮機1で高温、高EEにされ、冷媒配管
5を通って凝縮器2に導かれる。凝縮器で放熱しながら
液化した冷媒は膨張弁3の弁通路を経て断熱膨張し低流
、低圧になる。次いで、蒸発器4に導かれた冷媒は、周
囲よυ熱を奪って気化し、再び圧縮機1に戻る。ここで
膨張弁3の開度は感熱筒6で得られる蒸発器4の゛出口
側冷媒温度を検出して信号とし、該温度が適当な過熱度
を維持するように制御される。一般に、この種の膨張弁
を安定して動作させるには、感熱筒6で検出する温度を
安定にする必要がある。このため従来の膨張弁では蒸発
器4の出口冷媒をある程度以上過熱させざるを得なかっ
た。しかして、この制約は次のような問題点“を生じさ
せていた。第1点は蒸発器4の性能低下である。ガス冷
媒の熱伝達率は二相冷媒(蒸発を伴なう)の熱伝達ボに
比較して極めて小さいので、スーパヒート領域が増すと
いうことは蒸発器の平均熱通過出を低下させた使い方に
なる。第2点は冷媒の質量流量の低下であ企が低下する
。このことは熱交換量の低下を来す。
The gas refrigerant is heated to high temperature and high EE by the compressor 1, and is led to the condenser 2 through the refrigerant pipe 5. The refrigerant liquefied while dissipating heat in the condenser undergoes adiabatic expansion through the valve passage of the expansion valve 3, resulting in low flow and low pressure. Next, the refrigerant led to the evaporator 4 absorbs heat from the surroundings, vaporizes, and returns to the compressor 1 again. Here, the opening degree of the expansion valve 3 is controlled by detecting the temperature of the refrigerant on the exit side of the evaporator 4 obtained by the heat-sensitive tube 6 and using it as a signal to maintain the temperature at an appropriate degree of superheat. Generally, in order to operate this type of expansion valve stably, it is necessary to stabilize the temperature detected by the heat sensitive cylinder 6. For this reason, in the conventional expansion valve, the refrigerant at the outlet of the evaporator 4 has to be overheated to a certain degree or more. However, this restriction has caused the following problems. The first point is a decrease in the performance of the evaporator 4. The heat transfer coefficient of the gas refrigerant is Since it is extremely small compared to the heat transfer volume, the increase in the superheat area means that the average heat transfer rate of the evaporator is reduced.The second point is that the mass flow rate of the refrigerant is reduced, which reduces the efficiency. This results in a reduction in the amount of heat exchange.

冷媒質量流量を維持(あるいは増加)するためには圧縮
機の容量増加が必要である。
In order to maintain (or increase) the refrigerant mass flow rate, an increase in compressor capacity is required.

上記のごとき二つの問題点が存在していた。There were two problems as described above.

〔発明の目的〕[Purpose of the invention]

本発明は上記問題点に鑑みて発明されたもので、冷媒の
乾き度を検出し、この乾き度を任意に制御できる膨張弁
を提供することを目的とする。
The present invention was invented in view of the above problems, and an object of the present invention is to provide an expansion valve that can detect the degree of dryness of a refrigerant and arbitrarily control this degree of dryness.

〔発明の概要〕[Summary of the invention]

乾き産制#膨張弁を実現するには、冷媒の乾き度を、い
かにして正確に検出するかが重要点である。数種類のセ
ンシング方式について、理論的、実験的に検討し、冷媒
のガスと液との誘電率の違いに着目した静電容量変化法
が有効であることを解明した。本発明はその目的を達成
するため、上記静電容量変化法に着目し、冷媒回路の蒸
発器よシ圧縮機に至る通路に、一対の電極からなる乾き
度検出センサを設け、とのセンサの検出した静電容量信
号を、変換器を介し電圧あるいは電流に変換し、この電
圧あるいは電流を膨張弁の開度を駆動する駆動機構に導
びき弁開度を制御することを特徴とする。
In order to realize a dry production #expansion valve, it is important to accurately detect the degree of dryness of the refrigerant. We theoretically and experimentally investigated several types of sensing methods and found that the capacitance variation method, which focuses on the difference in dielectric constant between refrigerant gas and liquid, is effective. In order to achieve the object, the present invention focuses on the above-mentioned capacitance change method, and provides a dryness detection sensor consisting of a pair of electrodes in the passage from the evaporator to the compressor of the refrigerant circuit. It is characterized in that the detected capacitance signal is converted into voltage or current via a converter, and this voltage or current is introduced to a drive mechanism that drives the opening of the expansion valve to control the opening of the expansion valve.

以下本発明の一実施例を図面に基ずき説明する。第2図
゛において、圧縮機1、凝縮器2、膨張弁3、蒸発器4
は第1図と同様に順次配管嶋続され冷媒回路が形成され
ている。蒸発器4よシ圧縮機1に至る吸入通路1oには
センサ12が設けられ、このセンサ12は変換器13に
連絡され、更に、駆動機構14を介し膨張弁3に連絡さ
れている。変換器13はセンサ12がら得られる静電容
量の情報に対して、これを電圧あるいは電流に変換する
機構である。本変換器13は独立して存在することには
特に意味はなく、センサ12あるいは駆動機構14に付
随する形式でも何ら支障はない。駆動機構14は変換器
13から送られてくる電圧、電流の大きさに応じて膨張
弁3の開度を変える機構である。膨張弁3は、その開度
が駆動機構14により変化させられる。センサ12の構
造について第3図〜第6図に示す。第3図、第4図の例
は円筒電極21と棒状電極22の組合せで構成される。
An embodiment of the present invention will be described below with reference to the drawings. In Fig. 2, a compressor 1, a condenser 2, an expansion valve 3, an evaporator 4
As in FIG. 1, the pipes are successively connected to form a refrigerant circuit. A sensor 12 is provided in the suction passage 1o leading from the evaporator 4 to the compressor 1, and this sensor 12 is connected to a converter 13 and further connected to the expansion valve 3 via a drive mechanism 14. The converter 13 is a mechanism that converts capacitance information obtained from the sensor 12 into voltage or current. There is no particular meaning in the present converter 13 existing independently, and there is no problem in having it attached to the sensor 12 or the drive mechanism 14. The drive mechanism 14 is a mechanism that changes the opening degree of the expansion valve 3 according to the magnitude of the voltage and current sent from the converter 13. The opening degree of the expansion valve 3 is changed by a drive mechanism 14 . The structure of the sensor 12 is shown in FIGS. 3 to 6. The examples shown in FIGS. 3 and 4 are composed of a combination of a cylindrical electrode 21 and a rod-shaped electrode 22.

通路10の適宜長さ範囲を絶縁物10aで形成し、この
絶縁通路10aの内壁あるいは絶縁通路の中間に適宜長
さの円筒状の電極21を配置し、通蕗・1011−の軸
心方向に円筒状電極21よシやや長い長さの棒状電極2
2を配置している。
An appropriate length range of the passage 10 is formed with an insulator 10a, and a cylindrical electrode 21 of an appropriate length is arranged on the inner wall of the insulating passage 10a or in the middle of the insulating passage. A rod-shaped electrode 2 having a slightly longer length than the cylindrical electrode 21
2 is placed.

棒状電極22の棒径は流体の流動に影響を及ぼさない程
度の径とする。21a122aは両電極の端子を示す。
The rod diameter of the rod-shaped electrode 22 is set to a diameter that does not affect the flow of the fluid. 21a122a indicates terminals of both electrodes.

第5図、第6図はセンサの他の実施例を示し、一対の円
弧状電極23.24で形成される例を示す。通路1oの
適宜長さ範囲を絶縁物10aで形成し、絶縁通路10a
の内壁に、あるいは通路の一部を一対の円弧状の電極2
3.24を両電極間に間隙を設けて対向配置する。23
&、24aは両電極の端子を示す。第7図はセンサの更
に他の実施例を示し、一対の円弧状電極23.24と同
様の一対の円弧状電極25.26を90°位置をずらし
て配置している。
FIGS. 5 and 6 show another embodiment of the sensor, in which it is formed by a pair of arcuate electrodes 23, 24. An appropriate length range of the passage 1o is formed with an insulator 10a, and the insulating passage 10a is
A pair of arc-shaped electrodes 2 are installed on the inner wall of the
3.24 are placed facing each other with a gap between both electrodes. 23
&, 24a indicate terminals of both electrodes. FIG. 7 shows yet another embodiment of the sensor, in which a pair of arcuate electrodes 23, 24 and a similar pair of arcuate electrodes 25, 26 are arranged 90 degrees apart.

上記二対の電極対の配置は通路10aの適宜長さの範囲
内に流体の流通方向に直角方向の平面全範囲を覆って配
置され、即ち間隙27の通路軸方向の延長部分に他の電
極対の電極が位置するように配置されている。
The above-mentioned two pairs of electrodes are disposed within an appropriate length range of the passage 10a, covering the entire range of the plane perpendicular to the direction of fluid flow. The pair of electrodes is located at the same position.

次に本実施例の動作について説明する。第2図の冷媒回
路において、蒸発器4の後流部に設けられたセンサ12
は、内部の冷媒がガス100%か、液100%か、二相
流かによって、異なった信号を発生させる。その原理は
、ガス冷媒と液冷媒の誘電率が異なるためである。いま
、ガス冷媒の誘電率を6g1液冷媒の誘電率をεgとす
ると、ガスと液の静電容量Cg、C1は、 Cg=εg−A/Lg・・・・・・・・・・・・・・・
(1)CI−εg −A/L l・・・・・・・・・・
・・・・・(2)で光わされる。ここで、Aは電極板面
積、Lg。
Next, the operation of this embodiment will be explained. In the refrigerant circuit shown in FIG.
generates different signals depending on whether the internal refrigerant is 100% gas, 100% liquid, or a two-phase flow. The principle is that the dielectric constants of gas refrigerant and liquid refrigerant are different. Now, assuming that the dielectric constant of the gas refrigerant is 6g and the dielectric constant of the liquid refrigerant is εg, the capacitances of the gas and liquid Cg and C1 are as follows: Cg=εg−A/Lg・・・・・・・・・・・・・・・...
(1) CI-εg -A/L l・・・・・・・・・
...It is illuminated by (2). Here, A is the electrode plate area, Lg.

Llはそれぞれガス層と液層の厚さである(以上の関係
は平行平板電極を仮定したとき)。ガス層と液層が分離
して上下に分れているとすると、総合した静電容量Cは
式(1)、(2)を用いて、C=1/(↓□十土) 0g  C1 =εg、εd−A/(ε#−Lg+εg−L6)−εg
−εl−A/〔(εeO+εg−(1−2)) L)=
εg−εg −;/ (εe−a+εtx、CA−2)
)・−−−−・(3)となる。ここでL=Lg+L11
0(ボイドぶ)=Lg/Lである。冷媒の場合εg>>
εgであるので67=negとおくと式(3)は次のよ
うになる。(n>1) すなわち、静電容量Cとボイド宅(気体体積率)0は式
(4)に示すように反比例的関係にある。
Ll is the thickness of the gas layer and the liquid layer, respectively (the above relationship assumes parallel plate electrodes). Assuming that the gas layer and liquid layer are separated into upper and lower parts, the total capacitance C can be calculated using equations (1) and (2) as follows: C=1/(↓□Judo) 0g C1 = εg, εd-A/(ε#-Lg+εg-L6)-εg
-εl-A/[(εeO+εg-(1-2)) L)=
εg−εg −;/ (εe−a+εtx, CA-2)
)・----・(3). Here L=Lg+L11
0 (void)=Lg/L. For refrigerant εg >>
Since εg, by setting 67=neg, equation (3) becomes as follows. (n>1) That is, the capacitance C and the void volume (gas volume fraction) 0 have an inversely proportional relationship as shown in equation (4).

電極の形状が変ると式(4)の形は変るが、Cとαの関
係に対する傾向は変らない。そこで、Cとαの関係の例
を図示したものが第8図である。第8図は電極の形状に
対して理論的に定まるが、計算に入らない要因もあシ得
るので実験で確認しておけば良い。
When the shape of the electrode changes, the form of equation (4) changes, but the tendency for the relationship between C and α does not change. Therefore, FIG. 8 shows an example of the relationship between C and α. Although FIG. 8 is determined theoretically with respect to the shape of the electrode, there may be factors that are not included in the calculation, so it is best to confirm it by experiment.

センサ12によシ得られる上記静電容量の情報は変換器
13によ!ll電圧あるいは電流に変換されて駆動機構
14に伝わる。駆動機構14ではとの情報がかわき度の
初期設定に等しくなるように膨張弁の開度を調整する。
The information on the capacitance obtained by the sensor 12 is sent to the converter 13! It is converted into a voltage or current and transmitted to the drive mechanism 14. The drive mechanism 14 adjusts the opening degree of the expansion valve so that the information becomes equal to the initial setting of the degree of freshness.

以上の動作により、蒸発器出口冷媒のかわき度を任意に
調整できる膨張弁が実現できる。
By the above-described operation, an expansion valve that can arbitrarily adjust the degree of freshness of the refrigerant at the evaporator outlet can be realized.

〔発明の効果〕〔Effect of the invention〕

以上説明したように本発明によれば、冷媒回路における
蒸発器出口配管内冷媒のかわき度を膨張弁によって任意
に制御できる。この結果、次の効果が得られる。
As explained above, according to the present invention, the degree of refrigerant in the evaporator outlet pipe in the refrigerant circuit can be arbitrarily controlled by the expansion valve. As a result, the following effects can be obtained.

蒸発器内部で冷媒をスーパヒートさせないで済むので、
熱通過率が大幅に向上する。また、圧縮機吸込口の冷媒
スーパヒートを小さくできるので冷媒の質量流量が増し
、熱交換量が増加する。熱交換量が従来と同等で良い場
合は圧縮機容量を小さくでき、有電力になる。更に、吸
込口冷媒のかわき度を特定の値に設定することができる
ので、圧縮機(%定機種)の効率が向上する。
Since there is no need to superheat the refrigerant inside the evaporator,
Heat transfer rate is greatly improved. Furthermore, since the refrigerant superheat at the compressor suction port can be reduced, the mass flow rate of the refrigerant increases and the amount of heat exchange increases. If the amount of heat exchange is the same as the conventional one, the compressor capacity can be reduced and the system can be powered. Furthermore, since the degree of purity of the suction port refrigerant can be set to a specific value, the efficiency of the compressor (% fixed model) is improved.

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

第1図は従来の膨張弁を用いた冷媒回路図、第2図は本
発明の一実施例を示す乾き度制御膨張弁を設けた冷媒回
路図、第3図はセンサの一実施例を示す正面図、第4図
は第3図の■−■断面図を示す。第5図はセンサの他の
実施例を示す正面図、第6図は第5図の■−■断面図、
第7図はセンサの更に他の実施例を示す斜視図を示し、
第8図はセンサの、特性図である。 1・・・圧縮機 2・・・凝縮器 3・・・膨張弁 4
・・・蒸発器 10・・・通路 10a・・・絶縁通路
 12・・・センサ 13・・・交換器 14・・・駆
動機構 21.22.23.24.25.26・・・電
極 第1m 才2m 第q霞
Fig. 1 is a refrigerant circuit diagram using a conventional expansion valve, Fig. 2 is a refrigerant circuit diagram equipped with a dryness control expansion valve showing an embodiment of the present invention, and Fig. 3 is an embodiment of a sensor. The front view and FIG. 4 show a sectional view taken along the line ■-■ in FIG. 3. Fig. 5 is a front view showing another embodiment of the sensor, Fig. 6 is a sectional view taken along the line ■-■ of Fig. 5,
FIG. 7 shows a perspective view showing still another embodiment of the sensor,
FIG. 8 is a characteristic diagram of the sensor. 1... Compressor 2... Condenser 3... Expansion valve 4
... Evaporator 10... Passage 10a... Insulation passage 12... Sensor 13... Exchanger 14... Drive mechanism 21.22.23.24.25.26... Electrode 1st m Age 2m No. q Kasumi

Claims (1)

【特許請求の範囲】 1、  E縮機、凝縮器、膨張弁、蒸発器、を順次接続
してなる冷媒回路の蒸発器よシ王縮機に至る通路に一対
の電極からなるセンサを設け、とのセンサを変換器、駆
動機構を介在して膨張弁に連絡し、両電極間の静電容量
を恢出して上記膨張弁の開度を側脚する乾き度制御膨張
弁。 2、一対の電極が、通路壁を形成する適宜長さの円筒電
極と、円筒篭極内中央部に軸心方向に設けられた棒状電
極にてなる特許請求の範囲第1項記載の乾き度制御膨張
弁。 3、一対の電極が、適宜長さの円弧状の対向電極にて形
成されている特許請求の範囲第1項記載の乾き度制御膨
張弁。 4、一対の電極が、角度をずらして複数対設けられてい
る特許請求の範囲第3項記載の乾き度制御膨張弁。 5、変換器が、センサの信号を電圧あるいは電流に変換
するものである特許請求の範囲第1項記載の乾き度制御
膨張弁。 6、駆動機構が、膨張弁に連係され弁開度を制御するも
のである特許請求の範囲第1項記載の乾き度制御膨張弁
[Claims] 1. A sensor consisting of a pair of electrodes is provided in a passage leading from the evaporator to the evaporator of a refrigerant circuit formed by sequentially connecting an E-condenser, a condenser, an expansion valve, and an evaporator; A dryness control expansion valve that connects the sensor to the expansion valve via a converter and a drive mechanism, and controls the opening degree of the expansion valve by exploiting the capacitance between the two electrodes. 2. The dryness according to claim 1, wherein the pair of electrodes is a cylindrical electrode of an appropriate length forming a passage wall, and a rod-shaped electrode provided in the central part of the cylindrical cage in the axial direction. Controlled expansion valve. 3. The dryness control expansion valve according to claim 1, wherein the pair of electrodes is formed of arcuate opposed electrodes of appropriate length. 4. The dryness control expansion valve according to claim 3, wherein a plurality of pairs of electrodes are provided at different angles. 5. The dryness control expansion valve according to claim 1, wherein the converter converts the sensor signal into voltage or current. 6. The dryness control expansion valve according to claim 1, wherein the drive mechanism is linked to the expansion valve and controls the valve opening.
JP10077383A 1983-06-08 1983-06-08 dryness control expansion valve Granted JPS59229155A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10077383A JPS59229155A (en) 1983-06-08 1983-06-08 dryness control expansion valve

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10077383A JPS59229155A (en) 1983-06-08 1983-06-08 dryness control expansion valve

Publications (2)

Publication Number Publication Date
JPS59229155A true JPS59229155A (en) 1984-12-22
JPH0232542B2 JPH0232542B2 (en) 1990-07-20

Family

ID=14282800

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10077383A Granted JPS59229155A (en) 1983-06-08 1983-06-08 dryness control expansion valve

Country Status (1)

Country Link
JP (1) JPS59229155A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012062329A1 (en) * 2010-11-12 2012-05-18 Hb Products A/S System or method for measuring the phase of refrigerant in a cooling system
WO2020011327A1 (en) * 2018-07-11 2020-01-16 Hb Products A/S Refrigerant vapour quality measurement for optimized evaporator control and liquid distribution

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5216743A (en) * 1975-07-30 1977-02-08 Automob Antipollut & Saf Res Center Apparatus for detecting abnormal state of refrigerant
JPS55158551A (en) * 1979-05-29 1980-12-10 Mitsubishi Electric Corp Refrigerant condition detector
JPS5618873U (en) * 1979-07-23 1981-02-19

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5216743A (en) * 1975-07-30 1977-02-08 Automob Antipollut & Saf Res Center Apparatus for detecting abnormal state of refrigerant
JPS55158551A (en) * 1979-05-29 1980-12-10 Mitsubishi Electric Corp Refrigerant condition detector
JPS5618873U (en) * 1979-07-23 1981-02-19

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012062329A1 (en) * 2010-11-12 2012-05-18 Hb Products A/S System or method for measuring the phase of refrigerant in a cooling system
US9587866B2 (en) 2010-11-12 2017-03-07 HP Products A/S System or method for measuring the phase of ammonia in a cooling system
EP2638339A4 (en) * 2010-11-12 2017-05-31 HB Products A/S System or method for measuring the phase of refrigerant in a cooling system
US10174978B2 (en) 2010-11-12 2019-01-08 Hb Products A/S System or method for measuring the phase of ammonia in a cooling system
WO2020011327A1 (en) * 2018-07-11 2020-01-16 Hb Products A/S Refrigerant vapour quality measurement for optimized evaporator control and liquid distribution

Also Published As

Publication number Publication date
JPH0232542B2 (en) 1990-07-20

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