JPH062994A - Method and apparatus for adjusting temperature and pressure for recovery of refrigerant - Google Patents

Method and apparatus for adjusting temperature and pressure for recovery of refrigerant

Info

Publication number
JPH062994A
JPH062994A JP16115892A JP16115892A JPH062994A JP H062994 A JPH062994 A JP H062994A JP 16115892 A JP16115892 A JP 16115892A JP 16115892 A JP16115892 A JP 16115892A JP H062994 A JPH062994 A JP H062994A
Authority
JP
Japan
Prior art keywords
refrigerant
gas
temperature
portable
liquid
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.)
Pending
Application number
JP16115892A
Other languages
Japanese (ja)
Inventor
Keiji Tachibana
慶二 立花
Susumu Ishii
進 石井
Michio Kumaki
美知雄 熊木
Takeo Genba
武夫 玄葉
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 Building Systems Engineering Co Ltd
Original Assignee
Hitachi Building Systems Engineering Co 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 Building Systems Engineering Co Ltd filed Critical Hitachi Building Systems Engineering Co Ltd
Priority to JP16115892A priority Critical patent/JPH062994A/en
Publication of JPH062994A publication Critical patent/JPH062994A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2345/00Details for charging or discharging refrigerants; Service stations therefor
    • F25B2345/002Collecting refrigerant from a cycle

Abstract

PURPOSE:To prevent a refrigerant gas from being diffused to an atmosphere even when outside temperature is high or a refrigerant liquid temperature filled in a portable can is high by improving a technique for sucking and discharging a refrigerant sealed in a refrigerator by a compressor (or vacuum pump) and recovering it as the refrigerant liquid in the portable can by a filling pipe through a condenser and a gas-liquid separator. CONSTITUTION:A filling pipe 8 and a vaporizing pipe 9 are passed through the cover 7a of a portable can 7. The other end of the vaporizing pipe 9 is connected to the intake side of a compressor 2. The pressure of the vaporizing pipe is detected by a pressure sensor 11 and the temperature of a refrigerant liquid in a portable can is detected by a temperature sensor 12. A solenoid valve 14 interposed and connected to the middle of the vaporizing pipe 9 is so controlled as to be opened and closed by a control circuit 13 to which these detecting signals are input. An air sealed in the portable can 7 is sucked and discharged by a compressor 2 and discharged from a discharge valve 4b.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、冷凍機内に封入されて
いる冷媒を機外の冷媒容器に移して回収する場合、回収
系統内の温度,圧力を制御して回収作業を円滑に行うこ
とができ、しかも冷媒ガスを大気中に放出する虞れ無か
らしめるようにするための装置、および方法に関するも
のである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention, when the refrigerant enclosed in a refrigerator is transferred to a refrigerant container outside the machine and recovered, controls the temperature and pressure in the recovery system to smoothly carry out the recovery work. The present invention relates to an apparatus and a method for preventing the refrigerant gas from being released into the atmosphere.

【0002】[0002]

【従来の技術】冷凍機は冷媒物質(例えばフロン・R1
1)を封入密閉して、蒸発→圧縮→凝縮→減圧→(蒸
発)の冷凍サイクルを行わせる。この冷凍機を点検,整
備するために分解(部分分解を含む)すると冷媒が大気
中に放散されるので、これを防止するため冷凍機の冷凍
系から冷媒流体を抜き取って冷媒タンク内に回収,一時
保管しておき、点検,整備を終えた後、冷媒タンク内の
冷媒流体を冷凍機に戻すことが行われている。図4は従
来例の回収装置を示す系統図であって、冷凍機1は凝縮
器1aと蒸発器1bと圧縮機1cとによって冷凍系を構
成し、冷媒(例えばフロン・R11)を封入,密閉して
いる。上記の冷媒系から冷媒タンク等に冷媒液を移した
後、冷媒系の中に残っている冷媒ガスを冷媒タンク5に
移すため、冷媒機1内の冷媒ガスを圧縮機2によって吸
入,圧送し、凝縮器3で冷却して冷媒ガスを液化させ
る。例えば冷媒としてフロンR11などの低圧系フロン
を使用している場合、冷凍機1内には空気などの非凝縮
性ガスが混入しており、さらに該空気は多少の水蒸気を
含んでいる。上記の凝縮器3で冷却した冷媒などの流体
を気液分離器4に導いて液状成分のみをフロート弁4a
から冷媒タンク5に回収し、気体成分は放出弁4bから
大気中に放出する。wは水分の溜り具合を観察するため
の覗き窓、vは排水用の弁である。
2. Description of the Related Art Refrigerators are used as a refrigerant material (for example, Freon R1).
1) is sealed and sealed, and a refrigeration cycle of evaporation → compression → condensation → decompression → (evaporation) is performed. When disassembling (including partial disassembling) to inspect and maintain this refrigerator, the refrigerant is diffused into the atmosphere. To prevent this, the refrigerant fluid is drawn from the refrigeration system of the refrigerator and collected in the refrigerant tank. After being temporarily stored, and after completing inspection and maintenance, the refrigerant fluid in the refrigerant tank is returned to the refrigerator. FIG. 4 is a system diagram showing a conventional recovery device, in which the refrigerator 1 comprises a condenser 1a, an evaporator 1b, and a compressor 1c to constitute a refrigeration system, and a refrigerant (for example, CFC / R11) is sealed and hermetically sealed. is doing. After the refrigerant liquid is transferred from the above refrigerant system to the refrigerant tank or the like, the refrigerant gas remaining in the refrigerant system is transferred to the refrigerant tank 5, so that the refrigerant gas in the refrigerant machine 1 is sucked and pumped by the compressor 2. The condenser 3 is cooled to liquefy the refrigerant gas. For example, when a low-pressure chlorofluorocarbon such as chlorofluorocarbon R11 is used as the refrigerant, a non-condensable gas such as air is mixed in the refrigerator 1, and the air contains some water vapor. A fluid such as a refrigerant cooled by the condenser 3 is guided to a gas-liquid separator 4 so that only a liquid component is float valve 4a.
Is collected in the refrigerant tank 5 and the gas component is discharged into the atmosphere through the discharge valve 4b. Reference numeral w is a viewing window for observing the amount of water accumulated, and v is a drain valve.

【0003】往時(例えば昭和30年代の高度経済成長
以前)においては冷媒が高価であったため、これを放散
させることなく回収しようというのが経済・技術の思潮
であった。このため図4に示した従来例のようにして冷
媒の回収が図られたのであるが、この考え方に立つ限り
においては、回収する冷媒よりも高い費用を費やしてま
で徹底回収するという努力は為されなかった。
Since the refrigerant was expensive in the past (for example, before the high economic growth in the 1955's), it was an economic and technical idea to recover the refrigerant without dissipating it. For this reason, the refrigerant was recovered as in the conventional example shown in FIG. 4, but as far as this idea is concerned, efforts are made to thoroughly collect the refrigerant even at a higher cost than the refrigerant to be recovered. Was not done.

【0004】昭和40年代に入って各種の公害が社会問
題化し、さらに昭和60年代になると、フロンなどの冷
媒や溶剤によるオゾン層破壊という地球規模の環境問題
が国際的に論じられるようになり、回収フロンの金銭的
価値以上の費用をかけてでもフロンは1滴たりとも大気
中に放散させてはならないという時代になった。こうし
た観点から図4の従来技術を見ると、圧縮機2によって
冷凍機1内の冷媒ガスを精一杯排出しても、機内ガス圧
は−650mmHg程度にしか下がらない。この−65
0mmHgの冷媒ガスは分解整備に際して大気中に放散
されてしまう。この機内残留ガス圧を−750〜750
mmHgまで下げるため、図5に示すように真空ポンプ
9を用いる技術も公知である。
In the 1940s, various kinds of pollution became social problems, and in the 1960s, the global environmental problem of ozone layer depletion caused by refrigerants and solvents such as CFCs was discussed internationally. It has become an era in which even one drop of CFC must not be dissipated into the atmosphere even if it costs more than the monetary value of the recovered CFC. From this point of view, when the prior art of FIG. 4 is viewed, even if the compressor 2 discharges the refrigerant gas in the refrigerator 1 to the maximum, the gas pressure inside the machine falls only to about −650 mmHg. This -65
Refrigerant gas of 0 mmHg is released into the atmosphere during disassembly and maintenance. The residual gas pressure inside this machine is -750 to 750.
A technique using a vacuum pump 9 as shown in FIG. 5 to reduce the pressure to mmHg is also known.

【0005】[0005]

【発明が解決しようとする課題】図4,図5の従来技術
において放出弁4bから放出される非凝縮性ガス中に冷
媒ガスが含まれていて、非凝縮性ガスと冷媒ガスとの混
合気体が大気中に放散されるという問題に関しては、気
液分離器4内の上部空間に溜った混合気体をそのまま放
出弁4bから放出することなく、再度精溜して冷媒ガス
を完全に回収する技術が最近開発されて著しい成果を挙
げつつある。しかしながら、冷凍機1内の冷媒を回収す
る作業に関して、さらに次に述べるような問題が有る。
冷凍機1の容量が例えば300冷凍トン(1冷凍トン=
3024キロカロリー/時)の場合、約500キログラ
ムの冷媒が収蔵されている。従って、図4,図5に示し
た冷媒タンク5は500キログラムの容量を必要とす
る。ところが、フロン公害が社会問題化する以前に設置
された冷凍機には、この冷媒タンク5を備えていない例
が多く、図6に示すように気液分離器4の底部に注入管
8を接続してポータブル缶7に冷媒液を移すことが行わ
れる。このポータブル缶は、冷媒メーカーから冷凍機設
置現場へ冷媒を供給するために用いられたもので、例え
ば冷媒がR−11の場合、容量は100キログラム若し
くは50キログラムであり、冷凍機の傍に置かれたりさ
れている。図7(A)に示すように、注入管8の先端を
ポータブル缶7の口に差し込んで冷媒液を注入すると、
注入した冷媒液の温度が大気圧に相当する沸騰点よりも
高い場合はこの冷媒液の温度が沸騰点に下がるまで冷媒
液の一部が蒸発し、蒸発した冷媒ガスが矢印aのごとく
大気中に放散されてしまう。また、該ポータブル缶の周
囲の温度が冷媒の沸騰点よりも高く、該ポータブル缶の
温度も冷媒の沸騰点よりも高い場合も、冷媒液の一部が
蒸発して大気中に放散されてしまう。上記の冷媒ガスの
放散(矢印a)を防止するため図7(B)のように蓋7
aを設けると、ポータブル缶7内に閉じ込められた空気
の逃げ場が無いので冷媒液の注入が阻止されてしまう。
その上、冷媒の沸騰点よりも気温が高い場合、また、注
入される冷媒液の温度が高い場合にはポータブル缶内の
圧力が大気圧以上になるので、別段の冷却手段を備えて
いないポータブル缶7の内へ冷媒液を注入することは不
適当である。本発明は上述の事情に鑑みて為されたもの
であって、外気温が冷媒の沸点よりも高い場合であって
も、また、流入する冷媒液温度が沸騰点以上の場合であ
っても冷媒ガスを大気中に漏出させること無く、ポータ
ブル缶の中へ冷媒液を回収できるように温度,圧力を調
整する簡単で安価な装置、および、同温度,圧力の調整
方法を提供することを目的とする。
In the prior art of FIGS. 4 and 5, the non-condensable gas discharged from the discharge valve 4b contains the refrigerant gas, and the mixed gas of the non-condensable gas and the refrigerant gas. With respect to the problem that the gas is diffused into the atmosphere, a technique of completely rectifying the refrigerant gas by rectifying the mixed gas accumulated in the upper space of the gas-liquid separator 4 without directly discharging it from the discharge valve 4b. Has been recently developed and is achieving significant results. However, the work of recovering the refrigerant in the refrigerator 1 has the following problems.
The capacity of the refrigerator 1 is, for example, 300 refrigeration tons (1 refrigeration ton =
In the case of 3024 kcal / hour), about 500 kg of refrigerant is stored. Therefore, the refrigerant tank 5 shown in FIGS. 4 and 5 requires a capacity of 500 kilograms. However, there are many cases where the refrigerator installed before the pollution of CFCs becomes a social problem is not provided with this refrigerant tank 5, and the injection pipe 8 is connected to the bottom of the gas-liquid separator 4 as shown in FIG. Then, the refrigerant liquid is transferred to the portable can 7. This portable can was used to supply the refrigerant from the refrigerant manufacturer to the refrigerator installation site. For example, when the refrigerant is R-11, the capacity is 100 kilograms or 50 kilograms, and it is placed near the refrigerator. It has been done. As shown in FIG. 7A, when the tip of the injection pipe 8 is inserted into the mouth of the portable can 7 and the refrigerant liquid is injected,
When the temperature of the injected refrigerant liquid is higher than the boiling point corresponding to the atmospheric pressure, a part of the refrigerant liquid evaporates until the temperature of the refrigerant liquid drops to the boiling point, and the evaporated refrigerant gas is in the atmosphere as indicated by arrow a. Will be dissipated. Also, when the ambient temperature of the portable can is higher than the boiling point of the refrigerant and the temperature of the portable can is also higher than the boiling point of the refrigerant, a part of the refrigerant liquid evaporates and is diffused into the atmosphere. . As shown in FIG. 7 (B), the lid 7 is provided to prevent the above refrigerant gas from being diffused (arrow a).
When a is provided, there is no escape area for the air trapped in the portable can 7, so that the injection of the refrigerant liquid is blocked.
In addition, when the temperature is higher than the boiling point of the refrigerant, or when the temperature of the injected refrigerant liquid is high, the pressure inside the portable can becomes atmospheric pressure or higher, so a portable device without a separate cooling means is provided. It is inappropriate to inject the refrigerant liquid into the can 7. The present invention has been made in view of the above circumstances, even when the outside air temperature is higher than the boiling point of the refrigerant, or even when the refrigerant liquid temperature flowing in is above the boiling point An object is to provide a simple and inexpensive device for adjusting the temperature and pressure so that the refrigerant liquid can be collected in a portable can without leaking the gas into the atmosphere, and a method for adjusting the temperature and pressure. To do.

【0006】[0006]

【課題を解決するための手段】上記の目的を達成するた
めに創作した本発明の基本的原理について、その実施例
に対応する図1を参照しつつ略述すると、ポータブル缶
7に適合する蓋7aを設けるとともに、冷媒の注入管
8、および、缶内のエア抜き管としても作用する気化管
9を上記の蓋7aに貫通させ、上記の気化管9の他端は
圧縮機2の吸入側に連通させる。そして、冷媒液の温度
を温度センサ12で検出し、気化管内圧力を圧力センサ
11で検出する。さらに、これらの検出信号に基づいて
電磁弁14を開閉させる制御回路13を設ける。
The basic principle of the present invention created to achieve the above objects will be briefly described with reference to FIG. 1 corresponding to the embodiment. A lid that fits a portable can 7 will be described. 7a is provided, and a refrigerant injection pipe 8 and a vaporization pipe 9 that also functions as an air vent pipe in the can are penetrated through the lid 7a, and the other end of the vaporization pipe 9 is on the suction side of the compressor 2. Communicate with. Then, the temperature of the refrigerant liquid is detected by the temperature sensor 12, and the pressure inside the vaporizing pipe is detected by the pressure sensor 11. Further, a control circuit 13 for opening and closing the solenoid valve 14 based on these detection signals is provided.

【0007】[0007]

【作用】上述の手段よれば、ポータブル缶7内の空気を
気化管9で圧縮機2に吸い込ませて排出できるので、注
入管8からの冷媒液注入が円滑に行われる。さらに、ポ
ータブル缶7内の冷媒を蒸発させると気化熱を奪われる
ので缶内の冷媒液が冷却される。また、圧力センサ11
による検出圧力がポータブル缶の耐圧限度に近づくと電
磁弁14が開かれて、安全弁としての機能も兼ねる。
According to the above-mentioned means, the air in the portable can 7 can be sucked into the compressor 2 by the vaporization pipe 9 and discharged, so that the refrigerant liquid can be smoothly injected from the injection pipe 8. Further, when the refrigerant in the portable can 7 is evaporated, the heat of vaporization is removed, so that the refrigerant liquid in the can is cooled. In addition, the pressure sensor 11
When the pressure detected by is approaching the pressure limit of the portable can, the solenoid valve 14 is opened and also functions as a safety valve.

【0008】[0008]

【実施例】図1は本発明の1実施例を示し、図4に示し
た従来例の回収装置に本発明を適用したものである。ポ
ータブル缶7に適合する蓋7aに注入管8,ストップバ
ルブ15、および気化管9を気密に貫通させる。この気
化管とは排気兼気化管を略した呼称であって、圧縮機2
の吸入側に接続するとともに、その途中にストップバル
ブ10および電磁弁14を設けてある。そして、圧力セ
ンサ11によって気化管内の圧力を検出するとともに温
度センサ12によって冷媒液の温度を検出し、これらの
検出信号を制御回路13に入力させ、この制御回路によ
って前記の電磁弁14を開閉制御する。本例の温度セン
サ12は、20℃以上で閉となる常開形の温度感応スイ
ッチによって構成され、圧力センサ11は1kgf/c
2G以上で閉じる圧力感応スイッチで構成され、本例
の制御回路13は図2のように構成されている。すなわ
ち、温度感応スイッチ12と圧力感応スイッチ11とは
並列に接続されていて、温度が20℃以上になるか又は
圧力が1kgf/cm2Gを越えると電磁弁14がソレ
ノイドコイルに通電されて開弁作動する。図1から容易
に理解されるように圧縮機2の吐出圧力は凝縮器3を介
して気液分離器4に加えられ、注入管8を介してポータ
ブル缶7に及ぶ。このため、該ポータブル缶に冷媒液が
注入され始めると缶内の上部空間に閉じ込められている
空気が昇圧し、圧力センサ11が圧力上昇を検出して電
磁弁14を開かせる。これにより、ポータブル缶内の空
気は気化管9を経て圧縮機2に吸入され、ポータブル缶
内が降圧して冷媒液の注入を妨げなくなる。また、この
作用のもう一つの効果として、ポータブル缶7内の圧力
が該ポータブル缶の耐圧限度を越える虞れが無い。
FIG. 1 shows an embodiment of the present invention, in which the present invention is applied to the conventional recovery device shown in FIG. The injection pipe 8, the stop valve 15, and the vaporization pipe 9 are hermetically penetrated through the lid 7a that fits the portable can 7. This vaporization pipe is an abbreviation for an exhaust and vaporization pipe, and is used for the compressor 2
The stop valve 10 and the solenoid valve 14 are provided in the middle of the connection. Then, the pressure sensor 11 detects the pressure in the vaporization pipe, the temperature sensor 12 detects the temperature of the refrigerant liquid, and these detection signals are input to the control circuit 13, and the control circuit controls the opening / closing of the solenoid valve 14. To do. The temperature sensor 12 of this example is constituted by a normally open type temperature sensitive switch that closes at 20 ° C. or higher, and the pressure sensor 11 has a pressure of 1 kgf / c.
It is composed of a pressure sensitive switch that is closed at m 2 G or more, and the control circuit 13 of this example is structured as shown in FIG. That is, the temperature sensitive switch 12 and the pressure sensitive switch 11 are connected in parallel, and when the temperature rises above 20 ° C. or the pressure exceeds 1 kgf / cm 2 G, the solenoid valve 14 is energized to open the solenoid coil. The valve operates. As can be easily understood from FIG. 1, the discharge pressure of the compressor 2 is applied to the gas-liquid separator 4 via the condenser 3 and reaches the portable can 7 via the injection pipe 8. For this reason, when the refrigerant liquid starts to be injected into the portable can, the air trapped in the upper space inside the can rises in pressure, and the pressure sensor 11 detects the pressure increase and opens the solenoid valve 14. As a result, the air in the portable can is sucked into the compressor 2 through the vaporization tube 9, and the pressure inside the portable can is reduced so that the injection of the refrigerant liquid is not hindered. Further, as another effect of this action, there is no fear that the pressure in the portable can 7 will exceed the pressure limit of the portable can.

【0009】また、外気温が高く、またはポータブル缶
内の冷媒液温度が高くて温度センサ12を構成している
温度感応スイッチ12が閉じると電磁弁14が開弁さ
れ、ポータブル缶7内は負圧となり、缶内の冷媒液の一
部が気化して気化熱を奪い、缶内温度を下げる。本発明
を実施するとき、温度センサ12の検出温度Tは大気圧
に相当する冷媒の沸騰点よりも高くならないように、温
度−圧力関係を制御する。図3は前記と異なる実施例を
示し、図5の従来例に本発明を適用したものである。基
本的な構成は図1の実施例と類似であるが、真空ポンプ
6は一般に吐出圧が低いので、圧力センサ11は0.1
kgf/cm2G以上で閉じる圧力感応スイッチで構成
する。本例の場合、ポータブル缶内圧力が耐圧限度に達
することは考慮に入れなくても良いので、圧力センサ1
1の設置目的は専ら「ポータブル缶7内空気が閉じ込め
られて冷媒液の注入を阻止している状態」の検出であ
る。本例(図3)においても前例と同様に、ポータブル
缶内の冷媒液温度を沸騰点以下にしておかねばならな
い。本例においても前例においても、ポータブル缶7内
へ冷媒液を注入している間は、缶内温度における冷媒の
蒸気圧<缶内圧力 となるように制御すれば良いが、ポ
ータブル缶7を冷媒液で満たし終えた後、圧力センサ1
1の検出圧力の如何に拘らず、温度センサ12の検出温
度における冷媒の蒸気圧が大気圧以下、つまりその時の
大気圧における沸騰点以下となるように温度調整してお
くことが必要である。そうでないと本発明装置の蓋7a
を取り外したとき缶内冷媒液が(ビール瓶の蓋を取った
時のように)沸騰してしまう虞れが有る。
Further, when the temperature sensitive switch 12 constituting the temperature sensor 12 is closed when the outside air temperature is high or the temperature of the refrigerant liquid in the portable can is high, the electromagnetic valve 14 is opened and the inside of the portable can 7 is negative. A pressure is generated, and a part of the refrigerant liquid in the can vaporizes to take heat of vaporization, lowering the temperature inside the can. When carrying out the present invention, the temperature-pressure relationship is controlled so that the temperature T detected by the temperature sensor 12 does not become higher than the boiling point of the refrigerant corresponding to the atmospheric pressure. FIG. 3 shows an embodiment different from the above, and the present invention is applied to the conventional example of FIG. The basic configuration is similar to that of the embodiment shown in FIG. 1, but the vacuum pump 6 generally has a low discharge pressure, so that the pressure sensor 11 is 0.1
Consists of a pressure sensitive switch that closes at kgf / cm 2 G or higher. In the case of this example, it is not necessary to take into account that the pressure inside the portable can reaches the pressure limit, so the pressure sensor 1
The purpose of installation of No. 1 is exclusively to detect "a state in which the air in the portable can 7 is trapped and the injection of the refrigerant liquid is blocked". In this example (FIG. 3) as well, as in the previous example, the temperature of the refrigerant liquid in the portable can must be kept below the boiling point. In both the present example and the previous example, while the refrigerant liquid is being injected into the portable can 7, it may be controlled so that the vapor pressure of the refrigerant at the can internal temperature <the can internal pressure. After filling with liquid, pressure sensor 1
Regardless of the detected pressure of No. 1, it is necessary to adjust the temperature so that the vapor pressure of the refrigerant at the temperature detected by the temperature sensor 12 is below atmospheric pressure, that is, below the boiling point at atmospheric pressure at that time. Otherwise, the lid 7a of the device of the present invention
When the is removed, the refrigerant liquid in the can may boil (as when removing the beer bottle lid).

【0010】前記の温度センサ12は、ポータブル缶7
の側面に取つける。この取付個所は、冷媒液の液面より
も下方でなければならない。取付方法は任意に選定する
ことができ、例えば粘着テープで押さえて貼着しても良
いが、本例ではマグネット(図示せず)を組み付けてあ
ってポータブル缶に磁力吸着させるようになっている。
このように構成すると取付け取外し操作を迅速かつ容易
に行うことができて便利である。
The temperature sensor 12 is a portable can 7
To the side of. This mounting point must be below the level of the refrigerant liquid. The mounting method can be selected arbitrarily. For example, it may be attached by pressing with an adhesive tape, but in this example, a magnet (not shown) is attached so that the magnetic force is attracted to the portable can. .
This structure is convenient because the mounting / removing operation can be performed quickly and easily.

【0011】また、図3に仮想線で示した温度センサ1
2′のように、温度センサを注入管8の下端付近に取つ
けておくこともできる。この場合、該温度センサ12′
の信号電線12aは、蓋7aを気密に貫通させる。この
ように構成すると温度センサ12′が直接的に冷媒液と
接触するので、温度変化の感知に遅れを生じない。
Further, the temperature sensor 1 shown in phantom in FIG.
It is also possible to attach the temperature sensor near the lower end of the injection pipe 8 as in 2 '. In this case, the temperature sensor 12 '
The signal electric wire 12a makes the lid 7a penetrate airtightly. With this structure, the temperature sensor 12 'comes into direct contact with the refrigerant liquid, so that there is no delay in sensing the temperature change.

【0012】[0012]

【発明の効果】以上に実施例を挙げて説明したように、
本発明の装置を用いて本発明の方法を実施すると、外気
温が冷媒の沸騰点よりも高い場合であっても、冷媒ガス
を大気中に漏出させることなく、冷媒液をポータブル缶
の中へ回収することができる。
As described above with reference to the embodiments,
When the method of the present invention is carried out using the apparatus of the present invention, even when the outside air temperature is higher than the boiling point of the refrigerant, the refrigerant liquid is introduced into the portable can without leaking the refrigerant gas into the atmosphere. Can be collected.

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

【図1】本発明装置の1実施例を示す系統図である。FIG. 1 is a system diagram showing one embodiment of a device of the present invention.

【図2】上記実施例における制御回路の説明図である。FIG. 2 is an explanatory diagram of a control circuit in the above embodiment.

【図3】前記と異なる実施例の系統図である。FIG. 3 is a system diagram of an embodiment different from the above.

【図4】冷凍機に封入されている冷媒を回収する装置の
従来例を示す系統図である。
FIG. 4 is a system diagram showing a conventional example of a device for recovering a refrigerant enclosed in a refrigerator.

【図5】上記と異なる従来例の系統図である。FIG. 5 is a system diagram of a conventional example different from the above.

【図6】冷媒をポータブル缶に回収する作業の従来技術
を示す系統図である。
FIG. 6 is a system diagram showing a conventional technique for collecting refrigerant in a portable can.

【図7】上記従来技術における課題の説明図である。FIG. 7 is an explanatory diagram of a problem in the above conventional technique.

【符号の説明】[Explanation of symbols]

1…冷凍機、1a…凝縮器、1b…蒸発器、1c…圧縮
機、4…気液分離器、4a…フロート弁、4b…放出
弁、5…冷媒タンク、6…真空ポンプ、7…ポータブル
缶、7a…蓋、8…注入管、9…気化管、10…ストッ
プバルブ、11…圧力センサ、12,12′…温度セン
サ、12a…信号電線、13…制御回路、14…電磁
弁、15…ストップバルブ。
1 ... Refrigerator, 1a ... Condenser, 1b ... Evaporator, 1c ... Compressor, 4 ... Gas-liquid separator, 4a ... Float valve, 4b ... Release valve, 5 ... Refrigerant tank, 6 ... Vacuum pump, 7 ... Portable Can, 7a ... Lid, 8 ... Injection pipe, 9 ... Vaporization pipe, 10 ... Stop valve, 11 ... Pressure sensor, 12, 12 '... Temperature sensor, 12a ... Signal wire, 13 ... Control circuit, 14 ... Solenoid valve, 15 … Stop valve.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 玄葉 武夫 東京都千代田区神田和泉町1番地 日立ビ ル施設エンジニアリング株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Takeo Genba 1 Izumi-cho, Kanda, Chiyoda-ku, Tokyo Inside Hitachi Building Engineering Co., Ltd.

Claims (10)

【特許請求の範囲】[Claims] 【請求項1】 冷凍機に接続された圧縮機(2)と、上
記圧縮機によって吐出された冷媒ガスと非凝縮性ガスと
の混合気体を冷却して冷媒ガスを液化させる凝縮器
(3)と、上記凝縮器から流出する気液混合流を分離す
る気液分離器(4)とを具備する冷媒回収装置におい
て、 上記気液分離器(4)の下部空間に溜った冷媒液を収納
するポータブル缶(7)に適合する蓋(7a)と、 上記の蓋を貫通して気密に取りつけられ、前記気液分離
器(4)の底部付近に接続される冷媒液の注入管
(8)、および該注入管に介挿接続されたストップバル
ブ(15)と、 上記の蓋を貫通して気密に取りつけられ、前記圧縮機
(2)の吸入側に接続される気化管(9)、および該気
化管に介挿接続されたストップバルブ(10)と、 上
記気化管内の圧力を検出する圧力センサ(11)、およ
び前記ポータブルバルブ缶(7)内の冷媒液の温度を検
出する温度センサ(12)と、 前記気化管(9)の途中に、前記ストップバルブ(1
0)よりも圧縮機(2)寄りに位置せしめて介挿接続さ
れた電磁弁(14)と、 前記圧力センサの出力信号および温度センサの出力信号
を入力されて、前記の電磁弁(14)を開閉制御する制
御回路13と、を具備していることを特徴とする、冷媒
回収用の温度,圧力調整装置。
1. A compressor (2) connected to a refrigerator, and a condenser (3) for liquefying a refrigerant gas by cooling a mixed gas of a refrigerant gas and a non-condensable gas discharged by the compressor. And a gas-liquid separator (4) for separating a gas-liquid mixed flow flowing out from the condenser, wherein a refrigerant liquid accumulated in a lower space of the gas-liquid separator (4) is stored. A lid (7a) that fits the portable can (7), a refrigerant liquid injection pipe (8) that penetrates through the lid and is airtightly attached, and is connected near the bottom of the gas-liquid separator (4); And a stop valve (15) inserted and connected to the injection pipe, a vaporization pipe (9) penetrating through the lid and airtightly attached, and connected to the suction side of the compressor (2), and A stop valve (10) inserted and connected to the vaporizing pipe, and the pressure in the vaporizing pipe. A pressure sensor for detecting (11), and wherein a temperature sensor for detecting the temperature of the refrigerant fluid in the portable valve can (7) (12), in the middle of the vaporizing tube (9), the stop valve (1
0) and a solenoid valve (14) which is located closer to the compressor (2) and is inserted and connected, and the output signal of the pressure sensor and the output signal of the temperature sensor are input to the solenoid valve (14). And a control circuit 13 for controlling the opening and closing of the refrigerant, the temperature and pressure adjusting device for recovering the refrigerant.
【請求項2】 冷凍機内から冷媒ガスを吸引して吐出す
る真空ポンプ(6)と、上記真空ポンプから吐出される
冷媒ガスを冷却して液化させる凝縮器(3)と、上記凝
縮器によって液化された冷媒液から該冷媒液に混合して
いる非凝縮性ガスを分離させる気液分離器(4)とを具
備する冷媒回収装置において、 上記気液分離器(4)の下部空間に溜った冷媒液を収納
するポータブル缶(7)に適合する蓋(7a)と、 上記の蓋を貫通して気密に取りつけられ、前記気液分離
器(4)の底部付近に接続される冷媒液の注入管
(8)、および該注入管に介挿接続されたストップバル
ブ(15)と、 上記の蓋を貫通して気密に取りつけられ、前記圧縮機
(2)の吸入側に接続される気化管(9)、および該気
化管に介挿接続されたストップバルブ(10)と、 上
記気化管内の圧力を検出する圧力センサ(11)、およ
び前記ポータブルバルブ缶(7)内の冷媒液の温度を検
出する温度センサ(12)と、 前記気化管(9)の途中に、前記ストップバルブ(1
0)よりも圧縮機(2)寄りに位置せしめて介挿接続さ
れた電磁弁(14)と、 前記圧力センサの出力信号および温度センサの出力信号
を入力されて、前記の電磁弁(14)を開閉制御する制
御回路13と、を具備していることを特徴とする、冷媒
回収用の温度,圧力調整装置。
2. A vacuum pump (6) for sucking and discharging a refrigerant gas from the refrigerator, a condenser (3) for cooling and liquefying the refrigerant gas discharged from the vacuum pump, and a liquefaction by the condenser. In a refrigerant recovery device comprising a gas-liquid separator (4) for separating the non-condensable gas mixed with the refrigerant liquid from the collected refrigerant liquid, the gas is collected in a space below the gas-liquid separator (4). A lid (7a) suitable for a portable can (7) for containing a refrigerant liquid, and an injection of the refrigerant liquid which is fitted airtightly through the lid and is connected near the bottom of the gas-liquid separator (4). A pipe (8), a stop valve (15) inserted and connected to the injection pipe, and a vaporization pipe (which is attached to the suction side of the compressor (2) in an airtight manner by penetrating through the lid ( 9), and a stop valve inserted and connected to the vaporization pipe ( 10), a pressure sensor (11) for detecting the pressure in the vaporization pipe, a temperature sensor (12) for detecting the temperature of the refrigerant liquid in the portable valve can (7), and the middle of the vaporization pipe (9) The stop valve (1
0) and a solenoid valve (14) which is located closer to the compressor (2) and is inserted and connected, and the output signal of the pressure sensor and the output signal of the temperature sensor are input to the solenoid valve (14). And a control circuit 13 for controlling the opening and closing of the refrigerant, the temperature and pressure adjusting device for recovering the refrigerant.
【請求項3】 前記の圧力センサは所定圧力以上で閉と
なる常開形の圧力感応スイッチであり、前記の温度セン
サは所定温度以上で閉となる常開形の温度感応スイッチ
であり、上記双方のスイッチは相互に並列に接続されて
おり、前記電磁弁は通電されたときに開弁する常時閉止
形の電磁弁であり、前記双方のスイッチは上記電磁弁の
駆動回路中に介挿接続されていることを特徴とする、請
求項1又は同2に記載した冷媒回収用の温度,圧力調整
装置。
3. The pressure sensor is a normally open pressure sensitive switch that closes at a predetermined pressure or higher, and the temperature sensor is a normally open temperature sensitive switch that closes at a predetermined temperature or higher. Both switches are connected in parallel with each other, the solenoid valve is a normally closed solenoid valve that opens when energized, and both switches are connected in the drive circuit of the solenoid valve. The temperature and pressure adjusting device for refrigerant recovery according to claim 1 or 2, characterized in that
【請求項4】 前記の温度センサは、前記ポータブル缶
に吸着させるマグネット手段を有しているものであるこ
とを特徴とする、請求項1又は同2に記載した冷媒回収
用の温度,圧力制御装置。
4. The temperature and pressure control for refrigerant recovery according to claim 1 or 2, wherein the temperature sensor has a magnet means for adsorbing to the portable can. apparatus.
【請求項5】 前記の温度センサは前記ポータブル缶の
中に入れて用いられるものであって、該温度センサの信
号電線(12a)は前記の蓋(7a)を気密に貫通して
いることを特徴とする、請求項1又は同2に記載した冷
媒回収用の温度,圧力調整装置。
5. The temperature sensor is used by being put in the portable can, and the signal wire (12a) of the temperature sensor penetrates the lid (7a) in an airtight manner. The temperature / pressure adjusting device for recovering the refrigerant according to claim 1 or 2, characterized in that
【請求項6】 冷凍機(1)内に封入されている液状の
冷媒が回収された後に該冷凍機内に残留している冷媒ガ
スを該冷凍機内に漏入している非凝縮性ガスと一緒に圧
縮機(2)で吸入,凝縮器(3)を通過させて冷媒液と
非凝縮性ガスとの気液混合流とし、この混合流を気液分
離器(4)に導いて非凝縮性ガスを分離して大気中に放
出するとともに冷媒液を該気液分離器内の下部空間に溜
める回収操作において、上記気液分離器に溜った冷媒液
をポータブル缶(7)に移す場合、 上記ポータブル缶に入っていた空気を、前記圧縮機
(2)に吸入させて排除するとともに、該ポータブル缶
内の冷媒液の一部を気化させて上記圧縮機(2)に吸入
せしめ、気化熱を奪ってポータブル缶内の温度を降下さ
せることを特徴とする、冷媒回収用の温度,圧力調整方
法。
6. The refrigerant gas remaining in the refrigerator after the liquid refrigerant sealed in the refrigerator (1) is collected together with the non-condensable gas leaking into the refrigerator. Is sucked by the compressor (2) and passed through the condenser (3) to form a gas-liquid mixed flow of the refrigerant liquid and the non-condensable gas, and the mixed flow is guided to the gas-liquid separator (4) to non-condensable. In the recovery operation of separating the gas into the atmosphere and releasing the refrigerant liquid into the lower space of the gas-liquid separator, when the refrigerant liquid accumulated in the gas-liquid separator is transferred to the portable can (7), The air contained in the portable can is sucked into the compressor (2) to be removed, and at the same time, a part of the refrigerant liquid in the portable can is vaporized and sucked into the compressor (2) to generate heat of vaporization. Refrigerant recovery temperature, characterized by depriving and lowering the temperature inside the portable can Pressure adjustment method.
【請求項7】 冷凍機(1)内の冷媒ガスを真空ポンプ
(6)で吸い出し、凝縮器(3)で冷却して液化せさ、
気液分離器(4)で冷媒液から非凝縮性ガスを分離して
該冷媒液を気液分離器の底部に溜める冷媒回収方法にお
いて、該底部に溜った冷媒液をポータブル缶(7)に移
す場合、 上記ポータブル缶に入っていた空気を前記真空ポンプ
(6)に吸入させて排除するとともに、該ポータブル缶
内の冷媒液の一部を気化させて上記圧縮機(2)に吸入
せしめ、気化熱を奪ってポータブル缶内の温度を降下さ
せることを特徴とする、冷媒回収用の温度,圧力調整方
法。
7. A refrigerant gas in a refrigerator (1) is sucked out by a vacuum pump (6), cooled by a condenser (3) and liquefied,
In a refrigerant recovery method of separating a non-condensable gas from a refrigerant liquid by a gas-liquid separator (4) and collecting the refrigerant liquid at the bottom of the gas-liquid separator, the refrigerant liquid accumulated at the bottom is stored in a portable can (7). When transferring, the air contained in the portable can is sucked into the vacuum pump (6) to be removed, and a part of the refrigerant liquid in the portable can is vaporized and sucked into the compressor (2). A method for adjusting the temperature and pressure for recovering a refrigerant, which comprises removing the heat of vaporization to lower the temperature inside the portable can.
【請求項8】 前記ポータブル缶内の冷媒液の温度をT
とし、大気圧をPとし、前記冷媒液の一部を気化させる
操作は、 冷媒液の温度Tが、上記大気圧Pにおける冷媒の沸騰点
以下となるように制御することを特徴とする、請求項6
又は同7に記載した冷媒回収用の温度,圧力調整方法。
8. The temperature of the refrigerant liquid in the portable can is set to T
Wherein the atmospheric pressure is P and the operation of vaporizing a part of the refrigerant liquid is controlled so that the temperature T of the refrigerant liquid is equal to or lower than the boiling point of the refrigerant at the atmospheric pressure P. Item 6
Alternatively, the method for adjusting the temperature and pressure for recovering the refrigerant described in 7 above.
【請求項9】 前記の温度Tを大気圧Pにおける冷媒の
沸騰点以下とする制御は、ポータブル缶(7)と圧縮機
(2)若しくは真空ポンプ(6)の吸入側とを結ぶ管路
に介挿接続した電磁弁(14)を、制御回路(13)を
介して、圧力センサ(11)と温度センサ(12)とに
より開閉制御することを特徴とする、請求項8に記載し
た冷媒回収用の温度,圧力制御方法。
9. The control for controlling the temperature T to be equal to or lower than the boiling point of the refrigerant at the atmospheric pressure P is performed in a pipe line connecting the portable can (7) and the suction side of the compressor (2) or the vacuum pump (6). Refrigerant recovery according to claim 8, characterized in that the solenoid valve (14) connected by insertion is controlled to be opened and closed by a pressure sensor (11) and a temperature sensor (12) via a control circuit (13). Temperature and pressure control method.
【請求項10】 冷媒液をポータブル缶内に移して、該
ポータブル缶の中の冷媒液が所定量に達した後、缶内冷
媒液の一部を気化させて気化熱を奪うことにより残余の
冷媒液を冷却して、缶内冷媒液の温度を沸点よりも低温
ならしめることを特徴とする、請求項6又は同7に記載
した冷媒回収用の温度,圧力調整方法。
10. The refrigerant liquid is transferred into a portable can, and after the refrigerant liquid in the portable can reaches a predetermined amount, a part of the refrigerant liquid in the can is vaporized to remove the heat of vaporization to leave the residual liquid. The temperature and pressure adjusting method for refrigerant recovery according to claim 6 or 7, wherein the temperature of the refrigerant liquid in the can is made lower than the boiling point by cooling the refrigerant liquid.
JP16115892A 1992-06-19 1992-06-19 Method and apparatus for adjusting temperature and pressure for recovery of refrigerant Pending JPH062994A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16115892A JPH062994A (en) 1992-06-19 1992-06-19 Method and apparatus for adjusting temperature and pressure for recovery of refrigerant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16115892A JPH062994A (en) 1992-06-19 1992-06-19 Method and apparatus for adjusting temperature and pressure for recovery of refrigerant

Publications (1)

Publication Number Publication Date
JPH062994A true JPH062994A (en) 1994-01-11

Family

ID=15729700

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16115892A Pending JPH062994A (en) 1992-06-19 1992-06-19 Method and apparatus for adjusting temperature and pressure for recovery of refrigerant

Country Status (1)

Country Link
JP (1) JPH062994A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005003654A1 (en) * 2003-07-04 2005-01-13 Metachem Inc. Electronic refrigerant charging-pressure display system
JP2017125661A (en) * 2016-01-15 2017-07-20 株式会社中島自動車電装 Multistage variable-type gas recovery machine and multistage variable-type refrigerant recovery machine
CN110425779A (en) * 2019-08-28 2019-11-08 威立雅(哈尔滨)热电有限公司 Recycle the device of refrigerant
JP7106030B1 (en) * 2021-09-14 2022-07-25 三菱電機ビルソリューションズ株式会社 Refrigerant recovery system and refrigerant recovery method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005003654A1 (en) * 2003-07-04 2005-01-13 Metachem Inc. Electronic refrigerant charging-pressure display system
JP2017125661A (en) * 2016-01-15 2017-07-20 株式会社中島自動車電装 Multistage variable-type gas recovery machine and multistage variable-type refrigerant recovery machine
CN110425779A (en) * 2019-08-28 2019-11-08 威立雅(哈尔滨)热电有限公司 Recycle the device of refrigerant
JP7106030B1 (en) * 2021-09-14 2022-07-25 三菱電機ビルソリューションズ株式会社 Refrigerant recovery system and refrigerant recovery method

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