JPH0333983B2 - - Google Patents

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Publication number
JPH0333983B2
JPH0333983B2 JP57040709A JP4070982A JPH0333983B2 JP H0333983 B2 JPH0333983 B2 JP H0333983B2 JP 57040709 A JP57040709 A JP 57040709A JP 4070982 A JP4070982 A JP 4070982A JP H0333983 B2 JPH0333983 B2 JP H0333983B2
Authority
JP
Japan
Prior art keywords
gas
screw
temperature
screw compressor
pressure
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
JP57040709A
Other languages
Japanese (ja)
Other versions
JPS58158460A (en
Inventor
Masaki Moto
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.)
Ebara Corp
Original Assignee
Ebara Corp
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 Ebara Corp filed Critical Ebara Corp
Priority to JP4070982A priority Critical patent/JPS58158460A/en
Publication of JPS58158460A publication Critical patent/JPS58158460A/en
Publication of JPH0333983B2 publication Critical patent/JPH0333983B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、油噴射式スクリユー圧縮機で冷凍サ
イクルを形成するスクリユー冷凍機に関するもの
である。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a screw refrigerator whose refrigeration cycle is formed by an oil injection screw compressor.

〔従来の技術〕[Conventional technology]

従来の油噴射式スクリユー圧縮機においては、
ロータ室に潤滑油を噴射し、オス・メスロータの
間及びロータとケーシングとの間の隙間のシール
作用を行わしめて体積効率の向上を図ると共に、
冷媒の冷却を行つて圧縮による冷媒過熱を除去し
ている。
In conventional oil injection screw compressors,
Lubricating oil is injected into the rotor chamber to seal the gaps between the male and female rotors and between the rotor and the casing, thereby improving volumetric efficiency.
The refrigerant is cooled to remove overheating of the refrigerant due to compression.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

しかしながら、従来のスクリユー冷凍機では蒸
発器よりの冷媒の液ミストが圧縮機に吸入された
場合、潤滑油中に多量の冷媒が溶け込み潤滑油の
粘性が低下する。このような潤滑油が軸受に給油
されると軸受の損傷事故を招く。また、圧縮機吐
出側に接続された油分離器での油分離効率が低下
し、冷媒中に含まれた油が凝縮器及び蒸発器に多
量に流入し、伝熱の低下を来す。また、この現象
が長期にわたれば油分離器内の油が不足し、潤滑
不足による事故を招く欠点があつて問題であつ
た。
However, in conventional screw refrigerators, when liquid mist of refrigerant from the evaporator is sucked into the compressor, a large amount of refrigerant dissolves into the lubricating oil, reducing the viscosity of the lubricating oil. If such lubricating oil is supplied to the bearing, damage to the bearing may occur. Furthermore, the oil separation efficiency in the oil separator connected to the compressor discharge side is reduced, and a large amount of oil contained in the refrigerant flows into the condenser and evaporator, resulting in a reduction in heat transfer. Furthermore, if this phenomenon continues for a long period of time, there will be a shortage of oil in the oil separator, which has the disadvantage of causing accidents due to insufficient lubrication.

発明者は、この欠点を改良するために研究を重
ね、冷媒ミストが圧縮機に多く吸入されると吐出
温度が低下することに着目し、本発明をなすに至
つた。
In order to improve this drawback, the inventor conducted repeated research and focused on the fact that the discharge temperature decreases when a large amount of refrigerant mist is sucked into the compressor, leading to the present invention.

即ち、第1図のモリエール線図上でサイクルa
−b−c−dは標準サイクルを示す。サイクル
a′−b′−c−dは冷凍ミストが吸入された場合を
示す。蒸発圧力Pe及び凝縮圧力Pcを一定にとる
と、吐出ガスの凝縮圧力飽和温度Teに対する過
熱度に差が生ずる。通常の運転においては吐出ガ
ス温度Tbは60〜80℃程度となり、温度差(過熱
度)は△Tbとなる。ところが液ミストが吸入さ
れた場合には吐出ガス温度Tb´は50℃程度もしく
はそれ以上に低下し、温度差は減少して△Tbと
なる。
That is, on the Molière diagram in Figure 1, cycle a
-b-c-d indicates standard cycle. cycle
a'-b'-c-d show the case where frozen mist is inhaled. When the evaporation pressure Pe and the condensation pressure Pc are kept constant, a difference occurs in the degree of superheating of the discharged gas with respect to the condensation pressure saturation temperature Te. In normal operation, the discharge gas temperature Tb is about 60 to 80°C, and the temperature difference (degree of superheating) is ΔTb. However, when the liquid mist is inhaled, the discharge gas temperature Tb' drops to about 50°C or more, and the temperature difference decreases to ΔTb.

本発明は、これらの現象に基づき実用的に許容
される限度の冷媒ミスト吸入量に対応する過熱度
(温度差)△Tsを設定温度差となし、温度差が設
定温度差△Ts以下になつた場合に、凝縮器から
のホツトガスを圧縮機の吸入口に導くことによつ
て吐出ガスの温度を高め、潤滑油の中に溶け込む
冷媒の量を抑制する。
Based on these phenomena, the present invention sets the degree of superheating (temperature difference) △Ts corresponding to the practically allowable limit of refrigerant mist intake amount as the set temperature difference, and sets the temperature difference to be equal to or less than the set temperature difference △Ts. In this case, hot gas from the condenser is guided to the suction port of the compressor to increase the temperature of the discharged gas and suppress the amount of refrigerant that dissolves into the lubricating oil.

即ち、第4図に示すように、蒸発器から多量の
ミストを含んだ吸込ガスが圧縮機に吸込まれると
吐出温度(T2)が低くなり、過熱度(T2−T3
が小さくなる。従つて、凝縮器から吐出ガス
(T5)をスクリユー圧縮機の吸込部にバイパスさ
せると、蒸発器からの温度T1のミストを含むガ
スとバイパスガスの温度T6がミツクスされ温度
T1′で圧縮機に吸込まれ、吐出温度はT2′に上昇す
るので、吸込ガスが加熱による急激な温度上昇が
抑えられて開閉弁のハンチングが防止でき、潤滑
油への冷媒溶解の防止と安定した制御が可能とな
り、従来の問題点を排除することができるスクリ
ユー冷凍機を提供できることを目的としたもので
ある。
That is, as shown in FIG. 4, when suction gas containing a large amount of mist is sucked into the compressor from the evaporator, the discharge temperature (T 2 ) decreases, and the degree of superheat (T 2 - T 3 ) decreases.
becomes smaller. Therefore, when the discharge gas (T 5 ) from the condenser is bypassed to the suction section of the screw compressor, the gas containing mist from the evaporator at temperature T 1 and the bypass gas at temperature T 6 are mixed and the temperature increases.
The refrigerant is sucked into the compressor at T 1 ' and the discharge temperature rises to T 2 ', which suppresses the sudden temperature rise due to heating of the suction gas, prevents hunting of the on-off valve, and prevents refrigerant from dissolving in the lubricating oil. The purpose of this invention is to provide a screw refrigerator that enables stable control and eliminates the problems of conventional methods.

〔課題を解決するための手段〕[Means to solve the problem]

本発明は、スクリユー圧縮機、油分離装置、凝
縮器、蒸発器及びこれら機器を接続する冷媒経路
を備えたスクリユー冷凍機において、前記凝縮器
と、前記蒸発器からスクリユー圧縮機の吸入口に
連なる低圧冷媒ガス経路との間に開閉装置のある
ガスバイパス路を設けて前記凝縮器内の高圧冷媒
ガスの一部を蒸発器内の低圧冷媒ガスに減圧導入
し、圧縮機への吸込低圧冷媒ガスを加熱する機構
として備え、前記スクリユー圧縮機の吐出圧力
と、該スクリユー圧縮機より出される吐出流体の
温度とを検出する圧力センサと温度センサとをス
クリユー圧縮機の吐出側経路に備え、この両セン
サを吐出圧力と吐出流体の温度の相対関係を演算
処理する演算器に接続し、吐出ガスの過熱度を検
出すると共に、該演算器を前記開閉装置に接続配
備して前記凝縮器4から前記バイパス路を経てス
クリユー圧縮機吸入口へ導かれるホツトガスのバ
イパス量を吐出ガスの過熱度に対してほぼ反比例
的に制御する構成としたことを特徴とするスクリ
ユー冷凍機である。
The present invention provides a screw refrigerator equipped with a screw compressor, an oil separator, a condenser, an evaporator, and a refrigerant path connecting these devices. A gas bypass path with a switch is provided between the low-pressure refrigerant gas path and a part of the high-pressure refrigerant gas in the condenser is introduced under reduced pressure into the low-pressure refrigerant gas in the evaporator, and the low-pressure refrigerant gas is sucked into the compressor. A pressure sensor and a temperature sensor are provided in the discharge side path of the screw compressor to detect the discharge pressure of the screw compressor and the temperature of the discharge fluid discharged from the screw compressor, and both The sensor is connected to a computing unit that computes the relative relationship between the discharge pressure and the temperature of the discharged fluid, and the degree of superheat of the discharged gas is detected. This screw refrigerator is characterized in that the bypass amount of hot gas guided to the screw compressor suction port via the bypass path is controlled in substantially inverse proportion to the degree of superheat of the discharged gas.

〔実施例〕〔Example〕

本発明の実施例を第2図例で説明すると、スク
リユー圧縮機1、油分離装置3、凝縮器4、蒸発
器5及びこれら機器を接続する冷媒経路を備えた
スクリユー冷凍機において、前記凝縮器4と、前
記蒸発器5からスクリユー圧縮機1の吸入口に連
なる低圧冷媒ガス経路との間に開閉装置8のある
ガスバイパス路7を設けて前記凝縮器4内の高圧
冷媒ガスの一部を蒸発器5内の低圧冷媒ガスに減
圧導入し、圧縮機への吸込低圧冷媒ガスを加熱す
る機構として備え、前記スクリユー圧縮機1の吐
出圧力と、該スクリユー圧縮機1より出される吐
出流体の温度とを検出する圧力センサ11と温度
センサ12とをスクリユー圧縮機1の吐出側経路
に備え、この両センサ11,12を吐出圧力と吐
出流体の温度の相対関係を演算処理する演算器1
3に接続し、吐出ガスの過熱度を検出すると共
に、該演算器13を前記開閉装置8に接続配備し
て前記凝縮器4から前記バイパス路7を経てスク
リユー圧縮機吸入口へ導かれるホツトガスのバイ
パス量を吐出ガスの過熱度に対してほぼ反比例的
に制御する構成としたことを特徴とするスクリユ
ー冷凍機としてある。
An embodiment of the present invention will be described with reference to FIG. 4 and a low-pressure refrigerant gas path leading from the evaporator 5 to the suction port of the screw compressor 1. It is provided as a mechanism for introducing reduced pressure into the low-pressure refrigerant gas in the evaporator 5 and heating the low-pressure refrigerant gas sucked into the compressor. A pressure sensor 11 and a temperature sensor 12 are provided in the discharge side path of the screw compressor 1, and a computing unit 1 that uses these sensors 11 and 12 to calculate the relative relationship between the discharge pressure and the temperature of the discharged fluid.
3 to detect the degree of superheating of the discharged gas, and the computing unit 13 is connected to the switching device 8 to detect the hot gas that is led from the condenser 4 to the screw compressor suction port via the bypass path 7. The screw refrigerator is characterized in that the amount of bypass is controlled in substantially inverse proportion to the degree of superheating of discharged gas.

この場合、或る状態における過熱度(温度差)
を検出するのに種々な方法が用いられるが、例え
ば、凝縮圧力を検出する圧力センサ11と、吐出
ガス温度を検出する温度ガスセンサ12を設け、
圧力センサ11で検出した圧力に相当する飽和温
度と、温度センサ12により検出した吐出ガス温
度の差を演算器13で演算して求めて、その値に
よつてガスバイパス路7の開閉装置8の操作を行
うものである。
In this case, the degree of superheating (temperature difference) in a certain state
Various methods are used to detect this, but for example, a pressure sensor 11 that detects the condensation pressure and a temperature gas sensor 12 that detects the discharge gas temperature are provided,
The difference between the saturation temperature corresponding to the pressure detected by the pressure sensor 11 and the discharge gas temperature detected by the temperature sensor 12 is calculated by the calculator 13, and the opening/closing device 8 of the gas bypass path 7 is controlled based on the calculated value. It is something that performs operations.

圧力センサの位置は、油分離器に限らず、スク
リユー圧縮機1の吐出ケーシングから凝縮器内ま
での、どの高圧ガス部分に設けてもよい。また温
度センサ12はスクリユー圧縮機1の吐出ケーシ
ングから凝縮器内までの冷媒流路、及び油分離器
から油冷却器までの油流路のうち適宜の場所に設
けてもよい。
The position of the pressure sensor is not limited to the oil separator, but may be provided in any high-pressure gas section from the discharge casing of the screw compressor 1 to the inside of the condenser. Further, the temperature sensor 12 may be provided at an appropriate location in the refrigerant flow path from the discharge casing of the screw compressor 1 to the inside of the condenser, and the oil flow path from the oil separator to the oil cooler.

前記凝縮器4からのホツトガスをスクリユー圧
縮機1の吸込口に導くガスバイパス路7には、開
閉装置8(例えば開閉弁)を設けて、吸込みミス
ト量に応じて、即ち、過熱度の温度差に応じて、
バイパス流量を制御するようにする。即ち、例え
ば温度差が設定温度差以下にならない場合は開閉
弁は閉とし、温度差が設定温度差以下になるに従
い、その低下の度合に応じてほぼ逆比例的に開閉
弁の開度を開き、温度差ゼロのときに全開として
もよい。或いは簡単にオン・オフとしてもよい。
The gas bypass passage 7 that guides the hot gas from the condenser 4 to the suction port of the screw compressor 1 is provided with an opening/closing device 8 (for example, an opening/closing valve) to adjust the temperature difference according to the amount of suction mist, that is, the temperature difference in the degree of superheating. In response to the,
Bypass flow should be controlled. That is, for example, if the temperature difference does not fall below the set temperature difference, the on-off valve is closed, and as the temperature difference falls below the set temperature difference, the opening of the on-off valve is opened in approximately inverse proportion to the degree of decrease. , it may be fully opened when the temperature difference is zero. Alternatively, it may be simply turned on and off.

演算器から開閉弁への信号は電流、電圧、抵
抗、オン・オフ接点信号などの手段が用いられ
る。
Current, voltage, resistance, on/off contact signals, and other means are used for signals from the computing unit to the on-off valve.

また、この開閉弁は、低負荷時のホツトガスバ
イパス装置を兼用することができる。低負荷なる
ことを、圧縮機吸入量(スライドバルブストロー
クなどで)を検出することなどにより検出し、前
述の温度差による開閉弁の操作よりも優先させ
て、開閉弁を全開させるようにしてもよい。
Further, this on-off valve can also be used as a hot gas bypass device during low load. Even if the low load is detected by detecting the compressor suction amount (by slide valve stroke, etc.), the on-off valve is fully opened, giving priority to the on-off valve operation based on the temperature difference mentioned above. good.

なお、前記スクリユー圧縮機1は、駆動機2に
より駆動される。3は油分離装置としての油分離
器、4は凝縮器、5は蒸発器、6は減圧弁であ
り、これらの機器を冷媒経路が接続している。ま
たガスバイパス路7は、凝縮器4と、圧縮機1の
吸入口に連なる低圧冷媒ガス経路とを接続するも
のであり、途中に開閉装置8としての開閉弁が設
けられている。
Note that the screw compressor 1 is driven by a driving machine 2. 3 is an oil separator as an oil separation device, 4 is a condenser, 5 is an evaporator, and 6 is a pressure reducing valve, and a refrigerant path connects these devices. Further, the gas bypass path 7 connects the condenser 4 and a low-pressure refrigerant gas path connected to the suction port of the compressor 1, and is provided with an on-off valve as an on-off device 8 in the middle.

9は油冷却器、10は油ポンプであり、分離回
収した潤滑油をスクリユー圧縮機1の軸受及びロ
ータ室に供給する。
9 is an oil cooler, and 10 is an oil pump, which supplies separated and recovered lubricating oil to the bearing and rotor chamber of the screw compressor 1.

油分離器3の気相部には圧力センサ11が設け
られ、吐出ガスの圧力を検出し、液相部には温度
センサ12が設けられ、分離した油の温度(即
ち、吐出ガスの温度にほぼ等しい)を検出する。
13は演算器であり、圧力センサ11による吐出
ガス圧力に対応する飽和温度を求め、これに対す
る温度センサ12により検出した吐出ガス温度の
温度差を求め、この温度差が設定温度差以下にな
らない開閉装置8に閉の信号を与え、設定温度差
以下になつた場合に設定温度差からの低下量に逆
比例的な開度を与える開の信号を与えて開閉装置
8を開く。
A pressure sensor 11 is provided in the gas phase of the oil separator 3 to detect the pressure of the discharged gas, and a temperature sensor 12 is provided in the liquid phase to detect the temperature of the separated oil (i.e., the temperature of the discharged gas). approximately equal).
Reference numeral 13 denotes a calculation unit, which calculates the saturation temperature corresponding to the discharge gas pressure measured by the pressure sensor 11, calculates the temperature difference between the temperature of the discharge gas detected by the temperature sensor 12, and controls the opening/closing operation so that this temperature difference does not become less than the set temperature difference. A close signal is given to the device 8, and when the temperature difference falls below the set temperature difference, an open signal is given that gives an opening degree inversely proportional to the amount of decrease from the set temperature difference to open the opening/closing device 8.

作用につき述べれば、正常運転時にはスクリユ
ー圧縮機1の吸入ミスト量は許容値以下であり、
圧力センサ11による吐出ガス圧力及び温度セン
サ12による吐出ガス温度に基づいて演算器13
により求められた温度差は設定温度差よりも大な
ので開閉装置8は閉じられたままである。吸入ミ
スト量が許容値を越えると、温度差が設定温度差
以下となり演算器13からの信号により設定温度
差からの低下量に応じて開閉装置8の開度が選択
され、凝縮器4のホツトガスが圧縮機1に吸入さ
れ、吐出ガスの温度が高められ、油中にとめこむ
冷媒量を最小とすることができる。
Regarding the operation, during normal operation, the amount of mist sucked into the screw compressor 1 is below the allowable value.
Based on the discharge gas pressure determined by the pressure sensor 11 and the discharge gas temperature determined by the temperature sensor 12, the calculation unit 13
Since the temperature difference determined by is larger than the set temperature difference, the switching device 8 remains closed. When the intake mist amount exceeds the allowable value, the temperature difference becomes less than the set temperature difference, and the opening degree of the switching device 8 is selected according to the amount of decrease from the set temperature difference by a signal from the calculator 13, and the hot gas in the condenser 4 is is drawn into the compressor 1, the temperature of the discharged gas is increased, and the amount of refrigerant trapped in the oil can be minimized.

従つて、吐出ガスから分離された油には冷媒の
含有量が少なく、粘度の低下が殆どなく、良好な
潤滑作用を行うことができる。また、油分離器で
の分離効率がよくなり、凝縮器4、蒸発器5に付
着する油が少なくなり、伝熱効果を損なうことを
防ぎ、さらに油タンクの油量の減少を防ぎ、蒸発
器5に達する油の量が少ないので油戻し装置が不
要となり構造が簡単であり、さらに、蒸発器5か
らの液ミストの吸入を防止する目的の気液分離
器、液ガス熱交換器などの高価な装置が不要とな
る。
Therefore, the oil separated from the discharged gas has a low refrigerant content, has almost no decrease in viscosity, and can perform a good lubricating effect. In addition, the separation efficiency in the oil separator is improved, the amount of oil adhering to the condenser 4 and evaporator 5 is reduced, and the heat transfer effect is prevented from being impaired, and the oil amount in the oil tank is prevented from decreasing. Since the amount of oil that reaches the temperature of This eliminates the need for additional equipment.

第2図における圧力センサ11、温度センサ1
2の代わりに温度圧力スイツチを用いて、温度及
び圧力を検出し、開閉装置8として電磁弁を用
い、オン・オフ接点信号による電磁弁の開閉を行
うようにしてもよい。
Pressure sensor 11 and temperature sensor 1 in Fig. 2
2, a temperature and pressure switch may be used to detect the temperature and pressure, and a solenoid valve may be used as the opening/closing device 8, and the solenoid valve may be opened and closed by an on/off contact signal.

なお、前記開閉装置8は、低負荷時のホツトガ
スバイパス装置として、兼用することができる。
即ち、負荷検出機構により、負荷が、所定の設定
負荷よりも小さい、アンロード或いはそれに近い
低負荷時に信号を発して、前述の温度差による信
号よりも優先して開閉装置8を開放してホツトガ
スを導入する。このように兼用することにより装
置が簡単となる。
Note that the opening/closing device 8 can also be used as a hot gas bypass device during low load.
That is, the load detection mechanism generates a signal when the load is smaller than a predetermined set load, is unloaded, or is a low load close to it, and the switchgear 8 is opened with priority over the signal due to the temperature difference described above, and the hot gas is released. will be introduced. This dual use simplifies the device.

即ち、温度センサ12で吐出ガスの温度検出を
行い、同時に圧力センサ11で吐出ガスの圧力検
出を行つて、その吐出ガス圧力の飽和ガス温度に
換算して演算器13において前記吐出ガス温度の
相対関係、例えば(吐出ガス温度−飽和ガス温度
=過熱度)として演算処理し、出力部で、この過
熱度に見合う制御量を出力し、その制御量出力値
に応じてガスバイパス路7中の開閉装置8を所定
開度に保つ、即ち過熱度大のとき弁開度閉で、ま
た過熱度小のときには弁開度開のようにほぼ反比
例的な状態で操作制御するものである。
That is, the temperature sensor 12 detects the temperature of the discharged gas, and the pressure sensor 11 simultaneously detects the pressure of the discharged gas, converts the discharged gas pressure into a saturated gas temperature, and calculates the relative value of the discharged gas temperature in the calculator 13. For example, the relationship is calculated as (discharge gas temperature - saturated gas temperature = degree of superheat), the output section outputs a control amount corresponding to this degree of superheat, and the gas bypass path 7 is opened or closed according to the control amount output value. The device 8 is maintained at a predetermined opening degree, that is, the valve opening degree is closed when the degree of superheating is high, and the valve opening degree is open when the degree of superheating is small.

第3図例では、負荷検出機構の実施例を示すも
のである。負荷検出機構としては、圧縮機1の吸
入ガス量を検出すればよいが、この例では、吸入
ガス量をスライドバルブ14のストロークにより
検出しようとするものである。即ち、スライドバ
ルブ14にロツド15を設け、その端部のストラ
イカ16によりリミツトスイツチ17を作動せし
め、スライドバルブ14がストロークエンド、即
ちアンロードの位置の付近に来たことを検出して
吸入量を検出し、負荷を検出する。18は吸込
口、19は吐出口、20はロータである。
The example in FIG. 3 shows an embodiment of the load detection mechanism. The load detection mechanism may detect the intake gas amount of the compressor 1, but in this example, the intake gas amount is detected by the stroke of the slide valve 14. That is, a rod 15 is provided on the slide valve 14, a limit switch 17 is actuated by a striker 16 at the end of the rod 15, and the suction amount is detected by detecting when the slide valve 14 has reached the stroke end, that is, near the unloading position. and detect the load. 18 is a suction port, 19 is a discharge port, and 20 is a rotor.

〔発明の効果〕〔Effect of the invention〕

本発明により、従来の欠点を適確に除去でき、
潤滑油の粘度低下を防いで良好な潤滑を行い、し
かも凝縮器、蒸発器の伝熱の低下を防ぎ、さらに
油タンクの油量減少を防いで、高い性能でスクリ
ユー冷凍機を運転することができ、実用上極めて
大なる効果を奏することができる。
According to the present invention, the drawbacks of the conventional technology can be accurately eliminated.
It prevents the viscosity of the lubricating oil from decreasing to provide good lubrication, prevents a decrease in heat transfer in the condenser and evaporator, and prevents a decrease in the amount of oil in the oil tank, allowing screw refrigerators to operate at high performance. It is possible to achieve extremely great practical effects.

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

第1図は、吸入ミストの影響を示すモリエール
線図、第2図は本発明の実施例のフロー図、第3
図は本発明の実施例のスクリユー圧縮機の縦断面
図、第4図は本発明の特性を示すモリエール線図
である。 1……圧縮機、2……駆動機、3……油分離
器、4……凝縮器、5……蒸発器、6……減圧
弁、7……バイパス路、8……開閉装置、9……
油冷却器、10……油ポンプ、11……圧力セン
サ、12……温度センサ、13……演算器、14
……スライドバルブ、15……ロツド、16……
ストライカ、17……リミツトスイツチ、18…
…吸入口、19……吐出口、20……ロータ。
Fig. 1 is a Molière diagram showing the influence of inhalation mist, Fig. 2 is a flow diagram of an embodiment of the present invention, and Fig. 3 is a Molière diagram showing the influence of inhalation mist.
The figure is a longitudinal sectional view of a screw compressor according to an embodiment of the present invention, and FIG. 4 is a Molière diagram showing the characteristics of the present invention. DESCRIPTION OF SYMBOLS 1... Compressor, 2... Drive machine, 3... Oil separator, 4... Condenser, 5... Evaporator, 6... Pressure reducing valve, 7... Bypass path, 8... Switching device, 9 ……
Oil cooler, 10... Oil pump, 11... Pressure sensor, 12... Temperature sensor, 13... Arithmetic unit, 14
...Slide valve, 15... Rod, 16...
Striker, 17... Limit switch, 18...
...Suction port, 19...Discharge port, 20...Rotor.

Claims (1)

【特許請求の範囲】 1 スクリユー圧縮機1、油分離装置3、凝縮器
4、蒸発器5及びこれら機器を接続する冷媒経路
を備えたスクリユー冷凍機において、前記凝縮器
4と、前記蒸発器5からスクリユー圧縮機1の吸
入口に連なる低圧冷媒ガス経路との間に開閉装置
8のあるガスバイパス路7を設けて前記凝縮器4
内の高圧冷媒ガスの一部を蒸発器5内の低圧冷媒
ガスに減圧導入し、圧縮機への吸込低圧冷媒ガス
を加熱する機構として備え、前記スクリユー圧縮
機1の吐出圧力と、該スクリユー圧縮機1より出
される吐出流体の温度とを検出する圧力センサ1
1と温度センサ12とをスクリユー圧縮機1の吐
出側経路に備え、この両センサ11,12を吐出
圧力と吐出流体の温度の相対関係を演算処理する
演算器13に接続し、吐出ガスの過熱度を検出す
ると共に、該演算器13を前記開閉装置8に接続
配備して前記凝縮器4から前記バイパス路7を経
てスクリユー圧縮機吸入口へ導かれるホツトガス
のバイパス量を吐出ガスの過熱度に対してほぼ反
比例的に制御する構成としたことを特徴とするス
クリユー冷凍機。 2 スクリユー圧縮機1、油分離装置3、凝縮器
4、蒸発器5及びこれら機器を接続する冷媒経路
を備えたスクリユー冷凍機において、前記凝縮器
4と、前記蒸発器5からスクリユー圧縮機1の吸
入口に連なる低圧冷媒ガス経路との間に開閉装置
8のあるガスバイパス路7を設けて前記凝縮器4
内の高圧冷媒ガスの一部を蒸発器5内の低圧冷媒
ガスに減圧導入し、圧縮機への吸込低圧冷媒ガス
を加熱する機構として備え、前記スクリユー圧縮
機1の吐出圧力と、該スクリユー圧縮機1より出
される吐出流体の温度とを検出する圧力センサ1
1と温度センサ12とをスクリユー圧縮機1の吐
出側経路に備え、この両センサ11,12を吐出
圧力と吐出流体の温度の相対関係を演算処理する
演算器13に接続し、吐出ガスの過熱度を検出す
ると共に、該演算器13を前記開閉装置8に接続
配備して前記凝縮器4から前記バイパス路7を経
てスクリユー圧縮機吸入口へ導かれるホツトガス
のバイパス量を吐出ガスの過熱度に対してほぼ反
比例的に制御する構成とし、さらに前記スクリユ
ー圧縮機1の圧縮ガス量を検出する検出部を備
え、該検出部をその検出値が所定圧縮ガス量より
も小になつた場合、前記温度差による操作に優先
して開閉装置を開閉操作するように前記開閉装置
8に接続したことを特徴とするスクリユー冷凍
機。 3 前記スクリユー圧縮の圧縮ガス検出部が、容
量可変型スライドバルブを備えたスクリユー圧縮
機で前記スライドバルブのストロークにより検出
されるリミツトスイツチを備えたものである特許
請求の範囲第2項記載のスクリユー冷凍機。
[Scope of Claims] 1 In a screw refrigerator equipped with a screw compressor 1, an oil separation device 3, a condenser 4, an evaporator 5, and a refrigerant path connecting these devices, the condenser 4 and the evaporator 5 A gas bypass passage 7 with a switching device 8 is provided between the condenser 4 and the low-pressure refrigerant gas passage leading to the suction port of the screw compressor 1.
A part of the high-pressure refrigerant gas in the evaporator 5 is introduced under reduced pressure into the low-pressure refrigerant gas in the evaporator 5 to heat the low-pressure refrigerant gas sucked into the compressor. A pressure sensor 1 that detects the temperature of the fluid discharged from the machine 1
1 and a temperature sensor 12 are provided in the discharge side path of the screw compressor 1, and both sensors 11 and 12 are connected to a computing unit 13 that calculates the relative relationship between the discharge pressure and the temperature of the discharged fluid, and calculates the overheating of the discharged gas. The calculation unit 13 is connected to the switching device 8 and the bypass amount of the hot gas guided from the condenser 4 to the screw compressor suction port via the bypass path 7 is determined based on the superheat degree of the discharged gas. A screw refrigerating machine characterized by having a configuration in which control is performed almost inversely proportionally. 2 In a screw refrigerator equipped with a screw compressor 1, an oil separator 3, a condenser 4, an evaporator 5, and a refrigerant path connecting these devices, the screw compressor 1 is A gas bypass passage 7 with a switching device 8 is provided between the low-pressure refrigerant gas passage connected to the suction port, and the condenser 4
A part of the high-pressure refrigerant gas in the evaporator 5 is introduced under reduced pressure into the low-pressure refrigerant gas in the evaporator 5 to heat the low-pressure refrigerant gas sucked into the compressor. A pressure sensor 1 that detects the temperature of the fluid discharged from the machine 1
1 and a temperature sensor 12 are provided in the discharge side path of the screw compressor 1, and both sensors 11 and 12 are connected to a computing unit 13 that calculates the relative relationship between the discharge pressure and the temperature of the discharged fluid, and calculates the overheating of the discharged gas. At the same time, the computing unit 13 is connected to the switching device 8 and the bypass amount of the hot gas guided from the condenser 4 to the screw compressor suction port via the bypass path 7 is determined based on the superheat degree of the discharged gas. The screw compressor 1 is configured to control the amount of compressed gas in substantially inverse proportion to the amount of compressed gas, and further includes a detection section that detects the amount of compressed gas of the screw compressor 1, and when the detected value becomes smaller than a predetermined amount of compressed gas, the detection section detects the amount of compressed gas. A screw-through refrigerator characterized in that the screw-through refrigerator is connected to the opening/closing device 8 so that opening/closing operations of the opening/closing device are given priority to operations based on temperature differences. 3. The screw refrigeration according to claim 2, wherein the compressed gas detection unit for screw compression is a screw compressor equipped with a variable capacity slide valve, and is equipped with a limit switch that is detected by the stroke of the slide valve. Machine.
JP4070982A 1982-03-17 1982-03-17 Screw refrigerator Granted JPS58158460A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4070982A JPS58158460A (en) 1982-03-17 1982-03-17 Screw refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4070982A JPS58158460A (en) 1982-03-17 1982-03-17 Screw refrigerator

Publications (2)

Publication Number Publication Date
JPS58158460A JPS58158460A (en) 1983-09-20
JPH0333983B2 true JPH0333983B2 (en) 1991-05-21

Family

ID=12588101

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4070982A Granted JPS58158460A (en) 1982-03-17 1982-03-17 Screw refrigerator

Country Status (1)

Country Link
JP (1) JPS58158460A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102013210175A1 (en) 2013-05-31 2014-12-18 Siemens Aktiengesellschaft Heat pump for use of environmentally friendly refrigerants

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5634077A (en) * 1979-08-29 1981-04-06 Hitachi Ltd Refrigeration cycle
JPS5712260A (en) * 1980-06-24 1982-01-22 Hitachi Plant Eng & Constr Co Method of and apparatus for preventing inflow of liquid to compressor of refrigerating machine

Also Published As

Publication number Publication date
JPS58158460A (en) 1983-09-20

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