JPH0578739B2 - - Google Patents

Info

Publication number
JPH0578739B2
JPH0578739B2 JP269688A JP269688A JPH0578739B2 JP H0578739 B2 JPH0578739 B2 JP H0578739B2 JP 269688 A JP269688 A JP 269688A JP 269688 A JP269688 A JP 269688A JP H0578739 B2 JPH0578739 B2 JP H0578739B2
Authority
JP
Japan
Prior art keywords
evaporator
condenser
refrigerant
saturation temperature
expansion valve
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
Application number
JP269688A
Other languages
Japanese (ja)
Other versions
JPH01179877A (en
Inventor
Masami Kaji
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.)
TOYO KYARIA KOGYO KK
Original Assignee
TOYO KYARIA KOGYO KK
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 TOYO KYARIA KOGYO KK filed Critical TOYO KYARIA KOGYO KK
Priority to JP63002696A priority Critical patent/JPH01179877A/en
Publication of JPH01179877A publication Critical patent/JPH01179877A/en
Publication of JPH0578739B2 publication Critical patent/JPH0578739B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05FORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F11/00Other organic fertilisers
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05FORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F17/00Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
    • C05F17/20Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation using specific microorganisms or substances, e.g. enzymes, for activating or stimulating the treatment
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/141Feedstock
    • Y02P20/145Feedstock the feedstock being materials of biological origin
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/40Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Tropical Medicine & Parasitology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Biochemistry (AREA)
  • Biotechnology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Microbiology (AREA)
  • Molecular Biology (AREA)
  • Compression-Type Refrigeration Machines With Reversible Cycles (AREA)

Description

【発明の詳細な説明】 (イ) 産業上の利用分野 本発明は飽和温度検出回路を有する冷凍装置に
関するものである。
DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application The present invention relates to a refrigeration system having a saturation temperature detection circuit.

(ロ) 従来の技術 従来の冷凍装置は第10図に示す如く、圧縮機
aから吐出された高温高圧の冷媒は、四方弁bを
通り凝縮器cに導かれ外部の熱と熱交換し、高圧
の凝縮液となる。該凝縮液は、膨張弁dによつて
絞られ、低温低圧になり蒸発器eに導かれ蒸発す
る。蒸発器eで外部の熱と熱交換した冷媒は気化
し、圧縮器aの吸入側に至る。このように冷凍サ
イクルが形成されるが、通常、圧縮器aの吸入側
の気体の温度は、吸入圧力の飽和温度よりわずか
に高く保つことが望ましい。そこで圧縮機aの吸
入側の温度を、吸入温度検出器hによつて検出
し、又、飽和温度検出器iによつて吸入圧力の飽
和温度を検出し、その二つの信号を受けて温度差
調整器jが膨張弁dの開度を調整し圧縮機aの吸
入側の温度を吸入圧力の飽和温度よりわずかに高
くし適正な冷凍サイクルを維持している。この吸
入圧力の飽和温度を知る従来の方法は、凝縮機c
によつて凝縮した高圧の液冷媒をキヤピラリチユ
ーブfで圧縮機aの吸入側に導き、そこで蒸発さ
せ、吸入圧力に相当する飽和温度を検出してい
た。
(B) Prior art As shown in Fig. 10, in a conventional refrigeration system, high temperature and high pressure refrigerant discharged from a compressor a is led to a condenser c through a four-way valve b, where it exchanges heat with external heat. It becomes a high pressure condensate. The condensed liquid is throttled by an expansion valve d, becomes low temperature and low pressure, and is led to an evaporator e where it is evaporated. The refrigerant that has exchanged heat with external heat in the evaporator e is vaporized and reaches the suction side of the compressor a. Although a refrigeration cycle is thus formed, it is usually desirable to maintain the temperature of the gas on the suction side of the compressor a slightly higher than the saturation temperature of the suction pressure. Therefore, the temperature on the suction side of the compressor a is detected by the suction temperature detector h, and the saturation temperature of the suction pressure is detected by the saturation temperature detector i, and the temperature difference is detected by receiving these two signals. A regulator j adjusts the opening degree of the expansion valve d to maintain a proper refrigeration cycle by making the temperature on the suction side of the compressor a slightly higher than the saturation temperature of the suction pressure. The conventional method of finding the saturation temperature of this suction pressure is to
The high-pressure liquid refrigerant condensed by the capillary tube f is led to the suction side of the compressor a, where it is evaporated, and the saturation temperature corresponding to the suction pressure is detected.

(ハ) 発明が解決しようとする課題 従来の技術では、凝縮器によつて凝縮した高圧
の液冷媒を、キヤピラリチユーブで圧縮機の吸入
側に導き、そこで蒸発させることにより、飽和温
度を検出していた。これは、冷凍サイクルの高圧
と低圧をバイパスすることであり、高圧の液を、
直接低圧側で蒸発させるので飽和温度を検出する
為に使用される冷媒量は多く、運転効率の低下を
招き、又、圧縮機の停止時において、膨張弁を締
めても、キヤピラリチユーブを通じて冷媒の移動
があり低圧側に冷媒液の蓄積が起こり、圧縮機の
起動時に、液圧縮に至る等の不都合を生ずる。本
発明は上記に鑑みてなされたもので、高圧液冷媒
を直接、低圧側に導くことなく、又、少ない冷媒
量により、蒸発器飽和温度と凝縮器飽和温度を検
出し、冷凍サイクルの制御に供することを第一の
目的とし、さらに、冷媒回路の高圧側と低圧側と
を、膨張弁を締めることによつて分離し、停止時
における冷媒の移動による課題を解決することを
第二の目的とするものである。
(c) Problems to be solved by the invention In the conventional technology, the saturation temperature is detected by guiding the high-pressure liquid refrigerant condensed in the condenser to the suction side of the compressor through a capillary tube and evaporating it there. Was. This bypasses the high and low pressures of the refrigeration cycle, allowing the high pressure liquid to
Since the refrigerant is directly evaporated on the low-pressure side, a large amount of refrigerant is used to detect the saturation temperature, leading to a decrease in operating efficiency.Also, when the compressor is stopped, even if the expansion valve is closed, the refrigerant does not pass through the capillary tube. This movement causes refrigerant liquid to accumulate on the low pressure side, causing problems such as liquid compression when the compressor is started. The present invention has been made in view of the above, and is capable of detecting evaporator saturation temperature and condenser saturation temperature without directly guiding high-pressure liquid refrigerant to the low-pressure side and with a small amount of refrigerant, and is useful for controlling the refrigeration cycle. The first purpose is to provide high-pressure and low-pressure sides of the refrigerant circuit by tightening the expansion valve, and the second purpose is to solve problems caused by refrigerant movement during stoppage. That is.

(ニ) 課題を解決するための手段 本発明は上記のような課題に着目してなされた
もので、圧縮機、四方弁、凝縮器、膨張弁、蒸発
器を環状に接続した冷凍装置において、凝縮器入
口側から、凝縮器熱交換部、凝縮器液溜部の上
部、凝縮器液溜部の下部、凝縮器キヤピラリチユ
ーブを順次接続し、凝縮器出口と膨張弁入口間の
配管に至るように構成した凝縮器飽和温度検出回
路と、膨張弁出口と蒸発器入口間の配管から、蒸
発器キヤピラリチユーブ、蒸発器液溜部の下部、
蒸発器液溜部の上部、蒸発器熱交換部を順次接続
し、蒸発器出口側に至るように構成した蒸発器飽
和温度検出回路を有する冷凍装置を提供しようと
するものである。
(d) Means for Solving the Problems The present invention has been made in view of the problems described above, and includes a refrigeration system in which a compressor, a four-way valve, a condenser, an expansion valve, and an evaporator are connected in a ring. From the condenser inlet side, connect the condenser heat exchange part, the upper part of the condenser liquid reservoir part, the lower part of the condenser liquid reservoir part, and the condenser capillary tube in order, leading to the piping between the condenser outlet and the expansion valve inlet. From the condenser saturation temperature detection circuit configured as above, the piping between the expansion valve outlet and the evaporator inlet, the evaporator capillary tube, the lower part of the evaporator liquid reservoir,
It is an object of the present invention to provide a refrigeration system having an evaporator saturation temperature detection circuit configured to connect an upper part of an evaporator liquid storage part and an evaporator heat exchange part in sequence to reach the evaporator outlet side.

(ホ) 作用 次に、この冷凍装置の作用について第1図に示
す基本回路構成図に基づいて説明する。図中、実
線矢印で示す冷媒の流れを、冷媒サイクルの代表
例とすると、圧縮機1から吐出された高温高圧の
冷媒は、四方弁2を通り、凝縮器3に導かれ、外
部の熱と熱交換し、高圧の凝縮液となり、凝縮器
3の出口に至る。この時、凝縮器飽和温度検出回
路は、凝縮器3の出入口間に並列に接続されてい
るので、凝縮器飽和温度検出回路にも、四方弁2
と凝縮器3を結ぶ配管から分流した高温高圧の気
体冷媒が流入する。この冷媒は、凝縮器熱交換部
6にて外部の熱と熱交換し、気液混合状態となつ
て凝縮器液溜部7の上部から流入する。
(E) Function Next, the function of this refrigeration system will be explained based on the basic circuit configuration diagram shown in FIG. Assuming that the refrigerant flow indicated by the solid arrow in the figure is a typical example of a refrigerant cycle, the high temperature and high pressure refrigerant discharged from the compressor 1 passes through the four-way valve 2, is led to the condenser 3, and is absorbed by external heat. It exchanges heat, becomes a high-pressure condensate, and reaches the outlet of the condenser 3. At this time, since the condenser saturation temperature detection circuit is connected in parallel between the inlet and outlet of the condenser 3, the condenser saturation temperature detection circuit also connects the four-way valve 2.
A high-temperature, high-pressure gas refrigerant branched from a pipe connecting the condenser 3 and the condenser 3 flows into the condenser 3. This refrigerant exchanges heat with external heat in the condenser heat exchange section 6, becomes a gas-liquid mixture, and flows from the upper part of the condenser liquid reservoir section 7.

凝縮器液溜部7の下部には、凝縮器キヤピラリ
チユーブ8が接続されており、気液混合状態の冷
媒は、凝縮器3と膨張弁4を結ぶ配管に流出す
る。
A condenser capillary tube 8 is connected to the lower part of the condenser liquid reservoir 7, and the refrigerant in a gas-liquid mixed state flows out into a pipe connecting the condenser 3 and the expansion valve 4.

この凝縮器飽和温度検出回路を流れる冷媒の流
量は凝縮器飽和温度検出回路の出入口間の圧力
と、凝縮器キヤピラリチユーブ8の長さ、内径、
及び凝縮器キヤピラリチユーブ8に流入する冷媒
の乾き度で決定される。
The flow rate of the refrigerant flowing through this condenser saturation temperature detection circuit is determined by the pressure between the inlet and outlet of the condenser saturation temperature detection circuit, the length and inner diameter of the condenser capillary tube 8,
and the dryness of the refrigerant flowing into the condenser capillary tube 8.

又、凝縮器キヤピラリチユーブ8は乾き度の大
きい冷媒では大きな抵抗となり、乾き度の小さい
冷媒では小さな抵抗となる。これは凝縮器液溜部
7に滞留する冷媒を一定の気液混合状態にする効
果を奏する。
Further, the condenser capillary tube 8 has a large resistance when the refrigerant has a high degree of dryness, and has a small resistance when the refrigerant has a low degree of dryness. This has the effect of bringing the refrigerant staying in the condenser liquid reservoir 7 into a constant gas-liquid mixed state.

この様に冷媒が気液混合状態を保ちつつ流入流
出している凝縮器液溜部7の温度は凝縮器3の飽
和温度を示すこととなる。
The temperature of the condenser liquid reservoir section 7 through which the refrigerant flows in and out while maintaining the gas-liquid mixed state in this manner indicates the saturation temperature of the condenser 3.

又、凝縮器3により凝縮した高圧の液冷媒は、
膨張弁4により絞られ、低温低圧の気液混合状態
となり蒸発器5内に流入し、該蒸発器5内で蒸発
し気体となり、蒸発器5の出口に至る。
In addition, the high pressure liquid refrigerant condensed by the condenser 3 is
The gas is throttled by the expansion valve 4, becomes a low-temperature, low-pressure, gas-liquid mixed state, and flows into the evaporator 5, where it evaporates to become a gas and reaches the outlet of the evaporator 5.

この時、蒸発器飽和温度検出回路にも、膨張弁
4と蒸発器5を結ぶ配管から分流した気液混合状
態の冷媒が流入する。この冷媒は、蒸発器キヤピ
ラリチユーブ9を通り、蒸発器液溜部10の下部
より蒸発器液溜部10内に流入する。
At this time, the refrigerant in a gas-liquid mixed state that has been separated from the pipe connecting the expansion valve 4 and the evaporator 5 also flows into the evaporator saturation temperature detection circuit. This refrigerant passes through the evaporator capillary tube 9 and flows into the evaporator reservoir 10 from the lower part of the evaporator reservoir 10 .

この蒸発器飽和温度検出回路を流れる冷媒の流
量は、蒸発器飽和温度検出回路の出入口間の圧力
と、蒸発器キヤピラリチユーブ9の長さ、内径、
及び蒸発器キヤピラリチユーブ9に流入する冷媒
の乾き度で決定される。
The flow rate of the refrigerant flowing through this evaporator saturation temperature detection circuit is determined by the pressure between the inlet and outlet of the evaporator saturation temperature detection circuit, the length and inner diameter of the evaporator capillary tube 9,
and the dryness of the refrigerant flowing into the evaporator capillary tube 9.

又、蒸発器キヤピラリチユーブ9に導かれた気
液混合状態の冷媒が、蒸発器キヤピラリチユーブ
9の内径に比べ十分に大きい径の蒸発器液溜部1
0に流入する時、流速は極めて低下し、それが為
に冷媒は気体と液体に分離し、液冷媒は、その重
量のゆえに蒸発器液溜部10の下部に蓄積し、気
体冷媒は蒸発器液溜部10の上部に移動する。蒸
発器液溜部10の下部に蓄積した液冷媒が増加し
てくると、蒸発器キヤピラリチユーブ9より蒸発
器液溜部10に流入してくる冷媒にとつて抵抗と
なり、流入が抑制される。これは蒸発器液溜部1
0内の液冷媒の量を一定にする効果を奏する。
Further, the refrigerant in a gas-liquid mixed state led to the evaporator capillary tube 9 is transferred to the evaporator liquid reservoir 1 having a diameter sufficiently larger than the inner diameter of the evaporator capillary tube 9.
0, the flow rate is extremely low, so that the refrigerant separates into gas and liquid, the liquid refrigerant accumulates at the bottom of the evaporator reservoir 10 due to its weight, and the gas refrigerant accumulates at the bottom of the evaporator reservoir 10. Move to the upper part of the liquid reservoir 10. When the liquid refrigerant accumulated in the lower part of the evaporator liquid reservoir 10 increases, it becomes a resistance to the refrigerant flowing into the evaporator liquid reservoir 10 from the evaporator capillary tube 9, and the inflow is suppressed. . This is the evaporator liquid reservoir section 1
This has the effect of keeping the amount of liquid refrigerant within 0 constant.

又、蒸発器液溜部10の上部には蒸発器熱交換
部11が接続されている為に、蒸発器液溜部10
内の圧力は、蒸発器5と四方弁2を結ぶ配管内の
圧力と同一となり、蒸発器液溜部10内の液冷媒
は該配管内の圧力で蒸発し蒸発器液溜部10の温
度は、蒸発器飽和温度を示すこととなる。また蒸
発器5の出口の冷媒は四方弁2を通り圧縮機1の
吸入側に至る。
Further, since the evaporator heat exchange section 11 is connected to the upper part of the evaporator liquid reservoir section 10, the evaporator liquid reservoir section 10
The pressure inside is the same as the pressure inside the pipe connecting the evaporator 5 and the four-way valve 2, and the liquid refrigerant inside the evaporator reservoir 10 evaporates under the pressure inside the pipe, and the temperature of the evaporator reservoir 10 is , which indicates the evaporator saturation temperature. Further, the refrigerant at the outlet of the evaporator 5 passes through the four-way valve 2 and reaches the suction side of the compressor 1.

以上の様に圧縮機1から吐出した冷媒が該圧縮
機1の吸入側に循環する冷凍サイクルを形成して
いる。なお以上の説明は図面第1図において、実
線矢印で示す冷媒の流れの冷凍サイクルについて
行なつたが、四方弁2によつて冷媒の流を破線矢
印で示す冷凍サイクルに切り換えると、冷媒の流
れ、及び冷凍サイクルを構成している機能は逆転
するが、作用は同様であり、各々の飽和温度検出
回路は可逆的動作を行なうので、破線矢印で示す
冷凍サイクルについての説明は省略する。
As described above, a refrigeration cycle is formed in which the refrigerant discharged from the compressor 1 circulates to the suction side of the compressor 1. The above explanation has been made regarding the refrigeration cycle in which the refrigerant flow is indicated by the solid line arrow in FIG. Although the functions constituting , and the refrigeration cycle are reversed, the operations are the same, and each saturation temperature detection circuit performs a reversible operation, so a description of the refrigeration cycle indicated by the broken line arrow will be omitted.

(ヘ) 実施例 以下、本発明の実施例を図面に基づいて詳述す
れば、第2図は、圧縮機1、四方弁2、凝縮器
3、膨張弁4、蒸発器5により構成される空気調
和機の冷媒回路であり、実線矢印は、冷房運転の
冷媒の循環を示し、破線矢印は、暖房運転の冷媒
の循環を示す。膨張弁4としては、電気信号によ
つて、その弁開度が調節可能な機構を具備する可
逆式膨張弁である。第3図は、膨張弁の一種であ
る電気式膨張弁の一例を示すもので、ステツピン
グモーター11の回転動作は、ギア部12に伝達
されギア部12の出力シヤフトに嵌合接続された
駆動ネジ13の回転動作はネジにより上下運動に
変換される。駆動ネジ13の先端は弁14の上端
に対しピポツト軸受状に接触しており、駆動ネジ
13の上下動が該弁14を開閉する。弁14は弁
本体15にベローズ16にとつて気密に組み付け
られている。
(F) Embodiment Hereinafter, an embodiment of the present invention will be described in detail based on the drawings. FIG. This is a refrigerant circuit of an air conditioner, where solid arrows indicate refrigerant circulation during cooling operation, and dashed arrows indicate refrigerant circulation during heating operation. The expansion valve 4 is a reversible expansion valve equipped with a mechanism whose opening degree can be adjusted by an electric signal. FIG. 3 shows an example of an electric expansion valve, which is a type of expansion valve. The rotational movement of the screw 13 is converted into vertical movement by the screw. The tip of the drive screw 13 contacts the upper end of the valve 14 like a pivot bearing, and the vertical movement of the drive screw 13 opens and closes the valve 14. The valve 14 is airtightly assembled to a valve body 15 with a bellows 16.

上記のごとく構成された冷凍回路において、四
方弁2と凝縮器3を結ぶ配管に接続された凝縮器
熱交換部6は外部の熱と熱交換するように裸管の
断熱されていない導管であり、凝縮器3と熱交換
する外部の熱と同じ雰囲気におかれている。
In the refrigeration circuit configured as described above, the condenser heat exchange section 6 connected to the pipe connecting the four-way valve 2 and the condenser 3 is a bare, uninsulated conduit so as to exchange heat with external heat. , is placed in the same atmosphere as the external heat exchanging heat with the condenser 3.

凝縮器熱交換部6の内部に、圧縮機1より吐出
された高温のガス冷媒が流入すると外部の熱と熱
交換し、高温のガスの一部は液化し、凝縮器熱交
換部6と連接する凝縮器液溜部7の上部から凝縮
器液溜部7内に流入する。該凝縮器熱交換部6で
の熱交換量が多いほど液化する冷媒量は多くな
り、凝縮器液溜部7に流入する液冷媒も増加す
る。
When the high-temperature gas refrigerant discharged from the compressor 1 flows into the condenser heat exchange section 6, it exchanges heat with external heat, a part of the high-temperature gas is liquefied, and is connected to the condenser heat exchange section 6. It flows into the condenser liquid reservoir 7 from the upper part of the condenser liquid reservoir 7. As the amount of heat exchanged in the condenser heat exchange section 6 increases, the amount of refrigerant that is liquefied increases, and the amount of liquid refrigerant that flows into the condenser liquid reservoir section 7 also increases.

凝縮器液溜部7の下部には凝縮器キヤピラリチ
ユーブ8が連接されており、該凝縮器キヤピラリ
チユーブ8は凝縮器3の出口と膨張弁4の入口間
の配管に接続されている。よつて凝縮器液溜部7
内に滞留する液冷媒は凝縮器キヤピラリチユーブ
8を通つて、凝縮器3の出口と膨張弁4の入口間
の配管に流出する。
A condenser capillary tube 8 is connected to the lower part of the condenser liquid reservoir 7, and the condenser capillary tube 8 is connected to a pipe between the outlet of the condenser 3 and the inlet of the expansion valve 4. Therefore, condenser liquid reservoir section 7
The liquid refrigerant retained therein flows out through the condenser capillary tube 8 into the piping between the outlet of the condenser 3 and the inlet of the expansion valve 4.

このとき、凝縮器キヤピラリチユーブ8は、液
冷媒に対しては小さな抵抗となり冷媒の流量は多
いが、冷媒中の気相域が増加するに従つて凝縮器
キヤピラリチユーブ8の抵抗は増加し冷媒の流量
は減少する。したがつて凝縮器熱交換部6での熱
交換量の多少にかかわらず凝縮器液溜部7内冷媒
は、一定の気液混合状態となり、該凝縮器液溜部
7の温度は凝縮器飽和温度を示すこととなる。
At this time, the condenser capillary tube 8 has a small resistance to the liquid refrigerant and the flow rate of the refrigerant is large, but as the gas phase region in the refrigerant increases, the resistance of the condenser capillary tube 8 increases. Refrigerant flow rate decreases. Therefore, regardless of the amount of heat exchanged in the condenser heat exchange section 6, the refrigerant in the condenser reservoir section 7 is in a constant gas-liquid mixed state, and the temperature of the condenser reservoir section 7 is at the condenser saturation level. It will show the temperature.

なお凝縮器熱交換部6の高温冷媒の取入口は四
方弁2と凝縮器3の間に設置される分配器の一部
から取り出してもよく、凝縮器キヤピラリチユー
ブ8の出口は、凝縮器3と膨張弁4の間に設置さ
れる分配器の一部に接続してもよい。
Note that the high-temperature refrigerant intake of the condenser heat exchange section 6 may be taken out from a part of the distributor installed between the four-way valve 2 and the condenser 3, and the outlet of the condenser capillary tube 8 is connected to the condenser. It may be connected to a part of the distributor installed between the expansion valve 3 and the expansion valve 4.

また膨張弁4と蒸発器5の間に配管に接続され
た蒸発器キヤピラリチユーブ9には、膨張弁4を
出た冷媒が分流し、該冷媒は蒸発器キヤピラリチ
ユーブ9を通り、蒸発器液溜部10の下部より流
入するが蒸発器キヤピラリチユーブ9の内径に比
べ蒸発器液溜部10の内径は十分に大きいので、
流入する冷媒の流速は極めて低下し、それが為に
冷媒は気体と液体に分離し、液冷媒は、その重量
のゆえに蒸発器液溜部10の下部に蓄積し、気体
冷媒は蒸発器液溜部10の上部に移動する。
Further, the refrigerant that has exited the expansion valve 4 is diverted to an evaporator capillary tube 9 connected to a pipe between the expansion valve 4 and the evaporator 5, and the refrigerant passes through the evaporator capillary tube 9 and passes through the evaporator capillary tube 9. The liquid flows into the liquid reservoir 10 from the lower part, and since the inner diameter of the evaporator liquid reservoir 10 is sufficiently larger than the inner diameter of the evaporator capillary tube 9,
The flow rate of the incoming refrigerant is extremely reduced, which causes the refrigerant to separate into gas and liquid, the liquid refrigerant accumulating at the bottom of the evaporator sump 10 due to its weight, and the gas refrigerant accumulating at the bottom of the evaporator sump 10. Move to the top of section 10.

蒸発器液溜部10の下部に蓄積した液冷媒が増
加してくると、蒸発器キヤピラリチユーブ9より
蒸発器液溜部10内に流入してくる冷媒にとつて
抵抗となり、流入が抑制される。
When the liquid refrigerant accumulated in the lower part of the evaporator liquid reservoir 10 increases, it becomes a resistance to the refrigerant flowing into the evaporator liquid reservoir 10 from the evaporator capillary tube 9, and the inflow is suppressed. Ru.

これは蒸発器液溜部10内の液冷媒の量を一定
にする効果を奏する。
This has the effect of keeping the amount of liquid refrigerant in the evaporator liquid reservoir 10 constant.

また、蒸発器液溜部10の上部には蒸発器熱交
換部11が接続されている為に、蒸発器液溜部1
0内の圧力は、蒸発器5と四方弁2を結ぶ配管内
の圧力と同一となり、蒸発器液溜部10内の液冷
媒は該配管内の圧力で蒸発し蒸発器液溜部10の
温度は、蒸発器飽和温度を示すこととなる。
In addition, since the evaporator heat exchange section 11 is connected to the upper part of the evaporator liquid reservoir section 10, the evaporator liquid reservoir section 10
The pressure inside 0 is the same as the pressure inside the pipe connecting the evaporator 5 and the four-way valve 2, and the liquid refrigerant inside the evaporator reservoir 10 evaporates under the pressure inside the pipe, and the temperature of the evaporator reservoir 10 increases. represents the evaporator saturation temperature.

なお蒸発器キヤピラリチユーブ9の取り入れ口
は、膨張弁4と蒸発器5の配管の間に設置される
分配器の一部から取り出してもよく、蒸発器熱交
換部11の出口は蒸発器5と四方弁2の間の配管
に配置される分配器の一部に接続してもよい。
Note that the intake of the evaporator capillary tube 9 may be taken out from a part of the distributor installed between the expansion valve 4 and the piping of the evaporator 5, and the outlet of the evaporator heat exchange section 11 is connected to the evaporator 5. It may be connected to a part of the distributor arranged in the piping between the four-way valve 2 and the four-way valve 2.

又、凝縮器液溜部7にはサーミスタ等により温
度を検知する凝縮器飽和温度検出器13を密接
し、凝縮器飽和温度に対応した電気信号を発生さ
せる。
Further, a condenser saturation temperature detector 13 that detects temperature using a thermistor or the like is closely connected to the condenser liquid reservoir 7, and generates an electric signal corresponding to the condenser saturation temperature.

又、蒸発器液溜部10にはサーミスタ等により
温度を検知する蒸発器飽和温度検出器14を密接
し、蒸発器飽和温度に対応した電気信号を発生さ
せる。
Further, an evaporator saturation temperature detector 14 for detecting temperature using a thermistor or the like is closely connected to the evaporator liquid reservoir 10 to generate an electric signal corresponding to the evaporator saturation temperature.

又、圧縮機1の吸入側の配管には、サーミスタ
等により温度を検知する吸入ガス温度検出器15
を密接し、吸入ガス温度に対応した電気信号を発
生させる。
In addition, on the suction side piping of the compressor 1, there is a suction gas temperature detector 15 that detects the temperature using a thermistor or the like.
in close contact with each other to generate an electrical signal corresponding to the intake gas temperature.

このように発生させた凝縮器飽和温度、蒸発器
飽和温度、吸入ガス温度の信号を、電気式膨張弁
駆動回路12に入力し、実線矢印で示す冷房運転
時においては、蒸発器飽和温度検出器14の信号
と吸入ガス温度検出器15の信号の差が一定とな
るように電気式膨張弁駆動回路12より電気式膨
張弁4に信号を送り、電気式膨張弁4の弁を開閉
することにより、スーパーヒート制御を行なう。
The signals of the condenser saturation temperature, evaporator saturation temperature, and intake gas temperature thus generated are input to the electric expansion valve drive circuit 12, and during the cooling operation shown by the solid line arrow, the evaporator saturation temperature detector By sending a signal from the electric expansion valve drive circuit 12 to the electric expansion valve 4 and opening and closing the valve of the electric expansion valve 4 so that the difference between the signal of the electric expansion valve 14 and the signal of the intake gas temperature detector 15 becomes constant. , performs super heat control.

さらに破線矢印で示す暖房運転時においては、
蒸発器5は凝縮器になり、凝縮器3は蒸発器とな
り、その機能は逆転し冷媒の流れも逆転するの
で、凝縮器飽和温度検出器13の信号が蒸発器飽
和温度の信号となりその信号と吸入ガス温度検出
器15の信号の差が一定となるように上記同様ス
ーパーヒート制御を行なう。
Furthermore, during heating operation as indicated by the dashed arrow,
The evaporator 5 becomes a condenser, and the condenser 3 becomes an evaporator, and their functions are reversed and the flow of refrigerant is also reversed, so the signal from the condenser saturation temperature detector 13 becomes the evaporator saturation temperature signal, and the signal is Superheat control is performed in the same manner as described above so that the difference in the signals of the intake gas temperature detector 15 is constant.

第4図は他の実施例であり、凝縮器熱交換部6
と蒸発器熱交換部11を密接させ各々の熱を熱交
換することにより外部の熱と熱交換せずとも検出
回路の機能を兼ねたものであり、凝縮器飽和温度
と蒸発器飽和温度を集中して検出できるので飽和
温度検出回路の構成を簡素化できるなどの効果を
奏する。
FIG. 4 shows another embodiment, in which the condenser heat exchange section 6
By bringing the evaporator heat exchange section 11 and the evaporator heat exchange section 11 into close contact with each other and exchanging heat from each other, it also functions as a detection circuit without exchanging heat with external heat, and centralizes the condenser saturation temperature and evaporator saturation temperature. Since the saturation temperature detection circuit can be detected with the same temperature, the structure of the saturation temperature detection circuit can be simplified.

第5図は他の実施例であり、膨張弁4と蒸発器
5の間の配管から蒸発器キヤピラリチユーブ9を
接続する配管の間に第二の蒸発器熱交換部16を
設け、該第二の熱交換部16を冷凍回路中の高温
部配管に密接させ、第二の蒸発器熱交換部16中
を流れる冷媒を加熱することにより、該冷媒の乾
き度を増加させ、蒸発器キヤピラリチユーブ9を
流れる冷媒量を抑制し、蒸発器液溜部10に流入
する冷媒量を適正なものとする効果を奏する。
FIG. 5 shows another embodiment, in which a second evaporator heat exchange section 16 is provided between the pipe between the expansion valve 4 and the evaporator 5 and the pipe connecting the evaporator capillary tube 9. By bringing the second heat exchange section 16 into close contact with the high temperature section piping in the refrigeration circuit and heating the refrigerant flowing through the second evaporator heat exchange section 16, the dryness of the refrigerant is increased and the evaporator capillary is heated. This has the effect of suppressing the amount of refrigerant flowing through the tube 9 and making the amount of refrigerant flowing into the evaporator reservoir 10 appropriate.

第6図は他の実施例であり、凝縮器キヤピラリ
チユーブ8の蒸発器キヤピラリチユーブ9とを密
接させ凝縮器キヤピラリチユーブ8により蒸発器
キヤピラリチユーブ9中を流れる冷媒を加熱する
ことにより、該冷媒の乾き度を増加させ、蒸発器
キヤピラリチユーブ9を流れる冷媒量を抑制し、
蒸発器液溜部10に流入する冷媒量を適正なもの
とする効果を奏する。
FIG. 6 shows another embodiment in which the condenser capillary tube 8 is brought into close contact with the evaporator capillary tube 9, and the refrigerant flowing through the evaporator capillary tube 9 is heated by the condenser capillary tube 8. , increasing the dryness of the refrigerant and suppressing the amount of refrigerant flowing through the evaporator capillary tube 9;
This has the effect of optimizing the amount of refrigerant flowing into the evaporator liquid reservoir 10.

第7図は他の実施例であり、膨張弁4と蒸発器
5の間の配管から蒸発器キヤピラリチユーブ9を
接続する配管の間に第二の熱交換部16を設け、
該第二の熱交換部16を冷媒回路中の高温部配管
に密接させ、第二の蒸発器熱交換部16を流れる
冷媒を加熱することにより、該冷媒の乾き度を増
加させ、蒸発器キヤピラリチユーブ9を流れる冷
媒量を抑制し、蒸発器液溜部10に流入する冷媒
量を適正なものとする効果を奏する。
FIG. 7 shows another embodiment, in which a second heat exchange section 16 is provided between the pipe between the expansion valve 4 and the evaporator 5 and the pipe connecting the evaporator capillary tube 9,
By bringing the second heat exchange section 16 into close contact with the high temperature section piping in the refrigerant circuit and heating the refrigerant flowing through the second evaporator heat exchange section 16, the dryness of the refrigerant is increased and the evaporator carrier is heated. This has the effect of suppressing the amount of refrigerant flowing through the pillar tube 9 and making the amount of refrigerant flowing into the evaporator reservoir 10 appropriate.

第8図は他の実施例であり、膨張弁4の出口と
蒸発器5の入口の間の配管に接続された蒸発器飽
和温度検出回路の取出口と、膨張弁4の間に、第
二の膨張弁17を設け膨張弁4の開度により第二
の膨張弁17の入口の圧力を調整し適正なスーパ
ーヒート制御を行なうものであり、膨張弁4の出
口と、第二の膨張弁17の間の配管を延長し、さ
らに蒸発器5と四方弁2の間を結ぶ配管を延長す
ることも自由である。
FIG. 8 shows another embodiment, in which a second An expansion valve 17 is provided, and the pressure at the inlet of the second expansion valve 17 is adjusted according to the opening degree of the expansion valve 4 to perform appropriate superheat control. It is also free to extend the piping between the evaporator 5 and the four-way valve 2.

第9図は他の実施例であり、膨張弁4の出口と
蒸発器5の入口の間の配管に接続された蒸発器飽
和温度検出回路の取出口と、蒸発器5の入口の間
に第二の膨張弁17を設け、膨張弁4の開度によ
り第二の膨張弁17の入口の圧力を調整し適正な
スーパーヒート制御を行なうものであり、蒸発器
飽和温度検出回路の取出口と第二の膨張弁17の
入口の間の配管を延長し、さらに蒸発器5と四方
弁2の間を結ぶ配管を延長することも自由であ
る。
FIG. 9 shows another embodiment, in which a pipe is connected between the outlet of the evaporator saturation temperature detection circuit connected to the pipe between the outlet of the expansion valve 4 and the inlet of the evaporator 5, and the inlet of the evaporator 5. A second expansion valve 17 is provided, and the pressure at the inlet of the second expansion valve 17 is adjusted according to the opening degree of the expansion valve 4 to perform appropriate superheat control. It is also possible to extend the piping between the inlets of the two expansion valves 17 and further extend the piping connecting the evaporator 5 and the four-way valve 2.

(ト) 発明の効果 以上の説明により明らかなように、本発明によ
る蒸発器飽和温度検出器は液溜部を設けているの
で、無駄な液冷媒の低圧側への流出を防止し、さ
らに液溜部に供給すべき冷媒は、低圧側へ蒸発す
る冷媒量を補給するのみでよい。したがつて、従
来の如き高圧の液冷媒を直接低圧側に噴出させ、
その液冷媒の蒸発により飽和温度を検出する方法
に比べ、はるかに少ない冷媒量であり、冷凍サイ
クル中の、飽和温度検出の為に使用される冷媒に
よるバイパス量を抑えられ運転効率の向上が図れ
る。また凝縮器飽和温度と蒸発器飽和温度を検出
可能としたことで冷凍サイクルの冷媒の状態を知
ることができ、検出した凝縮器飽和温度と蒸発器
飽和温度を利用し、高圧維持制御、スーパーヒー
ト制御等広範囲の用途がある。また、凝縮器飽和
温度検出回路と蒸発器飽和温度検出回路は同一の
構成であり、冷媒の流れ方向によつて凝縮器飽和
温度検出回路としても蒸発器飽和温度検出回路と
しても作用するので飽和温度検出回路が簡単に構
成できる。特に、制御手段にマイクロコンピユー
ター等の電子回路を使用する時、該電子回路への
入力として、飽和温度を知る為の圧力変換器が不
要となり、サーミスタ等の温度検出器のみで冷媒
の状態を知り得るので、該電子回路への入力が簡
素化されるなどの効果を奏する。さらにこの発明
によれば、冷媒回路を膨張弁を境に高圧側と低圧
側に完全に分離出来るので、膨張弁を締めること
により、圧縮機の停止時において、特に蒸発器側
が低温の状態にあり、凝縮器側が高温の状態であ
つた場合、均圧動作による冷媒の蒸発器側への冷
媒の移動の他に、温度による冷媒の移動もあり、
蒸発器側には液冷媒の蓄積が起こり、圧縮機の再
起動時に液圧縮に至る等の弊害を未然に防止し得
る等、冷凍サイクルの適正な運転に著しい効果が
ある。
(g) Effects of the Invention As is clear from the above explanation, the evaporator saturation temperature detector according to the present invention is provided with a liquid reservoir, which prevents wasteful liquid refrigerant from flowing out to the low pressure side, and further reduces the amount of liquid refrigerant. As for the refrigerant to be supplied to the reservoir, it is only necessary to replenish the amount of refrigerant that evaporates to the low pressure side. Therefore, the conventional high-pressure liquid refrigerant is injected directly to the low-pressure side,
Compared to the method of detecting saturation temperature by evaporation of liquid refrigerant, the amount of refrigerant is much smaller, and the amount of bypass by refrigerant used to detect saturation temperature during the refrigeration cycle can be suppressed, improving operational efficiency. . In addition, by making it possible to detect the condenser saturation temperature and evaporator saturation temperature, it is possible to know the state of the refrigerant in the refrigeration cycle.Using the detected condenser saturation temperature and evaporator saturation temperature, high pressure maintenance control, superheat It has a wide range of uses such as control. In addition, the condenser saturation temperature detection circuit and the evaporator saturation temperature detection circuit have the same configuration, and depending on the flow direction of the refrigerant, they function as either a condenser saturation temperature detection circuit or an evaporator saturation temperature detection circuit, so the saturation temperature The detection circuit can be easily configured. In particular, when using an electronic circuit such as a microcomputer as a control means, there is no need for a pressure transducer to determine the saturation temperature as an input to the electronic circuit, and the state of the refrigerant can be determined only by a temperature detector such as a thermistor. Therefore, the input to the electronic circuit is simplified. Furthermore, according to this invention, the refrigerant circuit can be completely separated into a high pressure side and a low pressure side with the expansion valve as the boundary, so by tightening the expansion valve, the evaporator side in particular remains in a low temperature state when the compressor is stopped. When the condenser side is at a high temperature, in addition to the movement of refrigerant to the evaporator side due to pressure equalization, there is also movement of refrigerant due to temperature.
This has a significant effect on proper operation of the refrigeration cycle, such as preventing the accumulation of liquid refrigerant on the evaporator side and causing liquid compression when the compressor is restarted.

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

第1図は本発明の冷凍装置の基本回路構成図、
第2図は本発明の一実施例を示す回路構成図、第
3図は電気式膨張弁の構成の一例を示す断面図、
第4図乃至第9図はそれぞれ他の実施例を示す回
路構成図、第10図は従来の構成の一例を示す回
路構成図である。
FIG. 1 is a basic circuit diagram of the refrigeration system of the present invention.
FIG. 2 is a circuit configuration diagram showing an embodiment of the present invention, FIG. 3 is a sectional view showing an example of the configuration of an electric expansion valve,
4 to 9 are circuit configuration diagrams showing other embodiments, and FIG. 10 is a circuit configuration diagram showing an example of a conventional configuration.

Claims (1)

【特許請求の範囲】 1 圧縮機、四方弁、凝縮器、膨張弁、蒸発器を
環状に接続した冷凍装置において、凝縮器入口側
から、凝縮器熱交換部、凝縮器液溜部の上部、凝
縮器液溜部の下部、凝縮器キヤピラリチユーブを
順次接続し、凝縮器出口と膨張弁入口間の配管に
至るように構成した凝縮器飽和温度検出回路と、
膨張弁出口と蒸発器入口間の配管から、蒸発器キ
ヤピラリチユーブ、蒸発器液溜部の下部、蒸発器
液溜部の上部、蒸発器熱交換部を順次接続し、蒸
発器出口側に至るように構成した蒸発器飽和温度
検出回路を有することを特徴とする冷凍装置。 2 凝縮器飽和温度検出回路における凝縮器熱交
換部と、蒸発器飽和温度検出回路における蒸発器
熱交換部とを接触させたことを特徴とする請求項
1記載の冷凍装置。 3 蒸発器飽和温度検出回路において膨張弁出口
と蒸発器入口間の配管から、蒸発器キヤピラリチ
ユーブの間に、第二の蒸発器熱交換部を設けたこ
とを特徴とする請求項2記載の冷凍装置。 4 凝縮器飽和温度検出回路における凝縮器キヤ
ピラリチユーブと蒸発器飽和温度検出回路におけ
る蒸発器キヤピラリチユーブとを接触させたこと
を特徴とする請求項2又は3記載の冷凍装置。 5 膨張弁出口と蒸発器入口間の配管に接続され
た蒸発器飽和温度検出回路の取出口と、該膨張弁
出口の間に、第二の膨張弁を設けたことを特徴と
する請求項1記載の冷凍装置。 6 膨張弁出口と蒸発器入口間の配管に接続され
た蒸発器飽和温度検出回路の取出口と、該蒸発器
入口の間に、第二の膨張弁を設けたことを特徴と
する請求項2又は3又は4記載の冷凍装置。
[Claims] 1. In a refrigeration system in which a compressor, a four-way valve, a condenser, an expansion valve, and an evaporator are connected in a ring, from the condenser inlet side, a condenser heat exchange section, an upper part of a condenser liquid reservoir section, a condenser saturation temperature detection circuit configured to sequentially connect the condenser capillary tube to the lower part of the condenser liquid reservoir and reach the piping between the condenser outlet and the expansion valve inlet;
From the piping between the expansion valve outlet and the evaporator inlet, connect the evaporator capillary tube, the lower part of the evaporator liquid reservoir, the upper part of the evaporator liquid reservoir, and the evaporator heat exchange part in sequence, and reach the evaporator outlet side. A refrigeration system comprising an evaporator saturation temperature detection circuit configured as follows. 2. The refrigeration system according to claim 1, wherein the condenser heat exchange section in the condenser saturation temperature detection circuit and the evaporator heat exchange section in the evaporator saturation temperature detection circuit are brought into contact with each other. 3. The evaporator saturation temperature detection circuit further comprises a second evaporator heat exchange section between the piping between the expansion valve outlet and the evaporator inlet and the evaporator capillary tube. Refrigeration equipment. 4. The refrigeration system according to claim 2 or 3, wherein the condenser capillary tube in the condenser saturation temperature detection circuit and the evaporator capillary tube in the evaporator saturation temperature detection circuit are brought into contact with each other. 5. Claim 1, characterized in that a second expansion valve is provided between the outlet of the evaporator saturation temperature detection circuit connected to the pipe between the expansion valve outlet and the evaporator inlet and the expansion valve outlet. Refrigeration equipment as described. 6. Claim 2, characterized in that a second expansion valve is provided between the outlet of the evaporator saturation temperature detection circuit connected to the pipe between the expansion valve outlet and the evaporator inlet and the evaporator inlet. Or the refrigeration device according to 3 or 4.
JP63002696A 1988-01-09 1988-01-09 Refrigerating device Granted JPH01179877A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63002696A JPH01179877A (en) 1988-01-09 1988-01-09 Refrigerating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63002696A JPH01179877A (en) 1988-01-09 1988-01-09 Refrigerating device

Publications (2)

Publication Number Publication Date
JPH01179877A JPH01179877A (en) 1989-07-17
JPH0578739B2 true JPH0578739B2 (en) 1993-10-29

Family

ID=11536441

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63002696A Granted JPH01179877A (en) 1988-01-09 1988-01-09 Refrigerating device

Country Status (1)

Country Link
JP (1) JPH01179877A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008078369A1 (en) * 2006-12-25 2008-07-03 Orion Machinery Company Limited Physical quantity detector for refrigeration cycle
CN106152583B (en) * 2016-08-23 2019-03-12 无锡溥汇机械科技有限公司 A kind of High-precision temperature control type heat exchange system

Also Published As

Publication number Publication date
JPH01179877A (en) 1989-07-17

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