JP3530592B2 - Freon gas recovery device - Google Patents

Freon gas recovery device

Info

Publication number
JP3530592B2
JP3530592B2 JP22692994A JP22692994A JP3530592B2 JP 3530592 B2 JP3530592 B2 JP 3530592B2 JP 22692994 A JP22692994 A JP 22692994A JP 22692994 A JP22692994 A JP 22692994A JP 3530592 B2 JP3530592 B2 JP 3530592B2
Authority
JP
Japan
Prior art keywords
filling
valve
recovery
liquefaction
cfc gas
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
JP22692994A
Other languages
Japanese (ja)
Other versions
JPH0893997A (en
Inventor
嗣 植田
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.)
Mitsubishi Electric Building Techno-Service Co Ltd
Original Assignee
Mitsubishi Electric Building Techno-Service 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 Mitsubishi Electric Building Techno-Service Co Ltd filed Critical Mitsubishi Electric Building Techno-Service Co Ltd
Priority to JP22692994A priority Critical patent/JP3530592B2/en
Publication of JPH0893997A publication Critical patent/JPH0893997A/en
Application granted granted Critical
Publication of JP3530592B2 publication Critical patent/JP3530592B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • 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
    • F25B2345/007Details for charging or discharging refrigerants; Service stations therefor characterised by the weighing of refrigerant or oil

Description

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

【0001】[0001]

【産業上の利用分野】この発明は、フロンガス回収装置
に関し、特に回収したフロンガスを機器に充填すること
ができるフロンガス回収装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a Freon gas recovery apparatus, and more particularly to a Freon gas recovery apparatus capable of filling recovered Freon gas into a device.

【0002】[0002]

【従来の技術】図3は従来のフロンガス回収装置の一例
を示す構成図である。図において、1は被回収機器(図
示せず)との接続用の機器接続弁である機器接続用操作
弁、2は機器接続用操作弁1を介して被回収機器に接続
され、フロンガスを圧縮する圧縮機、3は圧縮機2に接
続され、フロンガス中の油分を分離除去するための油分
離器、4は油分離器3に接続され、圧縮されたフロンガ
スを冷却し液化する凝縮器、5は凝縮器4にメンテナン
ス用操作弁6を介して接続され、液化されたフロンから
不純物を取り除くストレーナであり、メンテナンス用操
作弁6は、ストレーナ交換時にガス回路を閉鎖するため
のものである。7は圧縮機2,油分離器3,凝縮器4及
びストレーナ5等を有する液化精製手段である。
2. Description of the Related Art FIG. 3 is a block diagram showing an example of a conventional CFC gas recovery apparatus. In the figure, reference numeral 1 is a device connection operating valve that is a device connection valve for connecting to a recovery target device (not shown), and 2 is connected to the recovery target device via a device connection operating valve 1 and compresses CFC gas. A compressor 3 for connecting to the compressor 2, an oil separator for separating and removing the oil component in the freon gas, 4 for connecting to the oil separator 3, a condenser for cooling and liquefying the compressed freon gas, 5 Is a strainer connected to the condenser 4 via a maintenance operation valve 6 to remove impurities from the liquefied CFC. The maintenance operation valve 6 is for closing the gas circuit when the strainer is replaced. Reference numeral 7 is a liquefaction refining means having a compressor 2, an oil separator 3, a condenser 4, a strainer 5, and the like.

【0003】8は容器接続弁である容器接続用操作弁9
を介してストレーナ5に接続され、回収したフロンを収
容する回収容器、10は機器接続用操作弁1と容器接続
用操作弁9との間に液化精製手段7と並列に接続されて
いる充填用電磁弁、11は回収容器8内のフロンの重量
を測定するための計量装置、12は液化精製手段7,充
填用電磁弁10及び計量装置11に接続されている制御
装置である。
Reference numeral 8 denotes a container connecting operation valve 9 which is a container connecting valve.
A collection container 10 connected to the strainer 5 via the stor- er for storing the recovered CFCs, and a collecting container 10 connected in parallel with the liquefaction purification means 7 between the device-connecting operation valve 1 and the container-connecting operation valve 9. An electromagnetic valve, 11 is a measuring device for measuring the weight of CFCs in the recovery container 8, and 12 is a control device connected to the liquefaction refining means 7, the filling electromagnetic valve 10 and the measuring device 11.

【0004】また、制御装置12は、装置の運転モード
を回収と充填とで切り替える運転モード切替部12a
と、回収モードのときに各機器を制御する回収モード制
御部12bと、回収モード制御部12bからの信号を各
機器に出力する回収モード出力部12cと、充填モード
のときに充填用電磁弁10に信号を出力する充填モード
出力部12dとを有している。
Further, the control device 12 has an operation mode switching section 12a for switching the operation mode of the device between recovery and filling.
A recovery mode control unit 12b for controlling each device in the recovery mode, a recovery mode output unit 12c for outputting a signal from the recovery mode control unit 12b to each device, and a filling solenoid valve 10 in the filling mode. And a filling mode output section 12d for outputting a signal to the.

【0005】次に、動作について説明する。まず、運転
モード切替部12aにより回収モードを選択した場合、
充填用電磁弁10は閉状態にされており、各操作弁1,
6,9が開状態に操作される。液化精製手段7の各機器
は、回収モード制御部12bにより制御されて運転され
る。機器接続用操作弁1から取り込まれたフロンガス
は、液化精製手段7により圧縮、凝縮、精製されて、回
収容器8に回収される。このとき、回収容器8内のフロ
ンの重量が計量装置により測定されており、回収容器8
への充填が不可となった時点で、それが回収モード制御
部12bにより検出され、装置全体の運転が停止され
る。これにより、回収容器8への過充填が防止されてい
る。
Next, the operation will be described. First, when the recovery mode is selected by the operation mode switching unit 12a,
The filling solenoid valve 10 is in the closed state, and each operation valve 1,
6 and 9 are operated in the open state. Each device of the liquefaction refining means 7 is controlled and operated by the recovery mode controller 12b. The chlorofluorocarbon taken in from the device connecting operation valve 1 is compressed, condensed and purified by the liquefaction refining means 7, and is recovered in the recovery container 8. At this time, the weight of CFCs in the collection container 8 is measured by the weighing device,
When it becomes impossible to fill the container, it is detected by the recovery mode control unit 12b, and the operation of the entire device is stopped. As a result, overfilling of the collection container 8 is prevented.

【0006】一方、運転モード切替部12aにより充填
モードを選択した場合、操作弁6は閉状態に、操作弁
1,9は開状態にそれぞれ操作され、また充填用電磁弁
10は充填モード出力部12dからの信号により開状態
にされる。このような状態で、回収容器8内から充填用
電磁弁10及び操作弁1を介して被回収機器、即ち被充
填機器内にフロンガスが充填される。
On the other hand, when the filling mode is selected by the operation mode switching section 12a, the operation valve 6 is operated in the closed state, the operation valves 1 and 9 are operated in the open state, and the filling solenoid valve 10 is operated in the filling mode output section. It is opened by the signal from 12d. In such a state, CFC gas is filled from the inside of the collection container 8 through the filling electromagnetic valve 10 and the operation valve 1 into the collection target device, that is, the filling target device.

【0007】[0007]

【発明が解決しようとする課題】上記のように構成され
た従来のフロンガス回収装置においては、充填モードで
被回収機器にフロンガスを充填する際、その充填量を作
業者が調整せざるを得ないため、各被回収機器毎に決ま
っている充填量に対して、過充填や充填不足が発生する
という問題点があった。また、回収モードの終了後に、
液化精製手段7を構成する各機器や配管内に回収フロン
ガスが残留するが、この残留フロンガスは未精製である
ため、被回収機器へ再充填することもできず、大気放出
されてしまうという問題点もあった。
In the conventional CFC gas recovery apparatus configured as described above, when the CFC gas is charged into the recovery target device in the charging mode, the operator has to adjust the charging amount. Therefore, there is a problem that overfilling or underfilling occurs with respect to the filling amount determined for each device to be recovered. Also, after the end of the collection mode,
Although the recovered CFC gas remains in each of the devices and pipes that make up the liquefaction refining means 7, the residual CFC gas is unrefined and cannot be refilled into the recovered device, and is released into the atmosphere. There was also.

【0008】この発明は、上記のような問題点を解決す
ることを課題としてなされたものであり、未精製の残留
フロンガスの大気放出を防止することができるフロンガ
ス回収装置を得ることを目的とする。
[0008] The present invention has been made as a problem of solving the above problems, and an object thereof is to obtain a Freon gas recovery apparatus capable of preventing the atmospheric discharge of residual Freon crude .

【0009】[0009]

【課題を解決するための手段】この発明に係るフロンガ
ス回収装置は、機器接続弁を介して被回収機器に接続さ
れ、フロンガスを液化精製する液化精製手段と、この液
化精製手段に容器接続弁を介して接続されている回収容
器と、機器接続弁及び容器接続弁の間に液化精製手段と
並列に接続されている充填用電磁弁と、液化精製手段に
設けられ、液化精製手段内の未精製の残留フロンガスを
液化精製手段内に閉じ込めるための一対の逆流防止用電
磁弁と、これら一対の逆流防止用電磁弁及び充填用電磁
弁に接続され、被回収機器へのフロンガス充填時に一対
の逆流防止用電磁弁を閉じるための信号を出力する制御
装置とを備えたものである。また、回収容器の重量を測
定する計量装置をさらに備え、制御装置は、計量装置及
び充填用電磁弁に接続され、被回収機器へのフロンガス
充填時に、計量装置による計量値の充填開始時からの減
少量を、被回収機器に応じて入力された設定値と比較
し、減少量が設定値を超える前に充填用電磁弁を閉じる
ための信号を出力する。
A CFC gas recovery apparatus according to the present invention is connected to a recovery target device through a device connection valve, and a liquefaction purification unit for liquefying and refining CFC gas, and a container connection valve for this liquefaction purification unit. A recovery container connected through the device, a solenoid valve for filling connected between the equipment connection valve and the container connection valve in parallel with the liquefaction purification means, and the liquefaction purification means provided in the liquefaction purification means A pair of backflow prevention solenoid valves for confining the residual CFC gas in the liquefaction refining means, and a pair of backflow prevention solenoid valves and a charging solenoid valve connected to prevent a pair of backflows when the collected equipment is filled with CFC gas. And a control device for outputting a signal for closing the solenoid valve for use. Also, weigh the collection container.
The measuring device is further equipped with
Connected to the solenoid valve for filling and CFC gas to the recovery target equipment.
At the time of filling, the value measured by the weighing device is reduced from the beginning of filling.
Compare a small amount with the set value input according to the device to be collected
Close the solenoid valve for filling before the decrease exceeds the set value.
To output the signal.

【0010】[0010]

【0011】[0011]

【作用】この発明においては、被回収機器へのフロンガ
スの充填時に、一対の逆流防止用電磁弁を自動的に閉
じ、液化精製手段内の残留フロンガスが被回収機器に逆
流するのを防止する。
According to the present invention, the pair of backflow preventing solenoid valves are automatically closed when the recovery target equipment is filled with the Freon gas to prevent the residual Freon gas in the liquefaction refining means from flowing back to the recovery target equipment.

【0012】[0012]

【0013】[0013]

【実施例】以下、この発明の実施例を図について説明す
る。図1はこの発明の一実施例によるフロンガス回収装
置を示す構成図であり、図3と同一又は相当部分には同
一符号を付し、その説明を省略する。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a configuration diagram showing a CFC gas recovery apparatus according to an embodiment of the present invention. The same or corresponding portions as those in FIG. 3 are designated by the same reference numerals and the description thereof will be omitted.

【0014】図において、21は機器接続用操作弁1と
圧縮機2との間に設けられている第1の逆流防止用電磁
弁、22は凝縮器4とストレーナ5との間に設けられて
いる第2の逆流防止用電磁弁であり、この逆流防止用電
磁弁22は、ストレーナ5のメンテナンス用の弁を兼ね
ている。また、8a,8bはそれぞれ回収容器8に付属
する液相用バルブ及び気相用バルブである。
In the figure, 21 is a first backflow preventing solenoid valve provided between the device connecting operation valve 1 and the compressor 2, and 22 is provided between the condenser 4 and the strainer 5. This is a second backflow preventing solenoid valve, and this backflow preventing solenoid valve 22 also serves as a valve for maintenance of the strainer 5. Further, 8a and 8b are a liquid phase valve and a gas phase valve which are attached to the recovery container 8, respectively.

【0015】23は液化精製手段7,計量装置11及び
充填用電磁弁10等に接続されている制御装置であり、
この制御装置23は、装置の運転モードを回収と充填と
で切り替えたり充填時の設定値を入力するための運転モ
ード設定・切替部23aと、回収モードのときに各機器
を制御する回収モード制御部23bと、充填モードのと
きに各機器を制御する充填モード制御部23cと、計量
装置11による計量値を表示する計量値表示部23d
と、各モードにおいて各機器に制御信号を出力する制御
出力部23eとを有している。
A control device 23 is connected to the liquefaction refining means 7, the measuring device 11, the filling solenoid valve 10 and the like,
The control device 23 includes an operation mode setting / switching unit 23a for switching the operation mode of the device between recovery and filling and inputting a set value at the time of filling, and a recovery mode control for controlling each device in the recovery mode. 23b, a filling mode control unit 23c that controls each device in the filling mode, and a weighing value display unit 23d that displays a weighing value by the weighing device 11.
And a control output unit 23e that outputs a control signal to each device in each mode.

【0016】次に、動作について説明する。図2は図1
の装置の動作を説明するためのフローチャートである。
まず、運転モード設定・切替部23aにより回収モード
を選択(ステップS1)した場合、各操作弁1,9が開
状態に操作されるなど、運転が可能となる条件が整えら
れる。このようにして運転可能条件が満たされると(ス
テップS2)、充填用電磁弁10は閉状態のままで、各
逆流防止用電磁弁21,22が開状態にされる(ステッ
プS3)。以下は、従来例と同様にしてフロンガスの回
収運転が行われ(ステップS4)、回収モード制御部2
3bにより回収終了条件が満たされたことが確認される
と(ステップS5)、各電磁弁10,21,22が閉状
態にされて回収運転が終了する(ステップS6)。
Next, the operation will be described. 2 is shown in FIG.
3 is a flowchart for explaining the operation of the apparatus of FIG.
First, when the recovery mode is selected by the operation mode setting / switching unit 23a (step S1), the conditions for enabling the operation are prepared such that the operation valves 1 and 9 are operated in the open state. When the operable condition is satisfied in this way (step S2), the solenoid valves 10 for filling are kept closed and the solenoid valves 21, 22 for backflow prevention are opened (step S3). Thereafter, the CFC recovery operation is performed in the same manner as in the conventional example (step S4), and the recovery mode control unit 2
When it is confirmed by 3b that the recovery end condition is satisfied (step S5), the solenoid valves 10, 21, 22 are closed and the recovery operation ends (step S6).

【0017】一方、運転モード設定・切替部23aによ
り充填モードを選択(ステップS1)した場合、被回収
機器、即ち被充填機器に応じた必要充填量を運転モード
設定・切替部23aに設定値(M1)として入力する
(ステップS7)。次に、充填モード制御部23cによ
り、充填開始時における計量装置11の計量値が初期計
量値(M2)として記憶される。このようにして、M
1,M2がメモリに記憶された後、各逆流防止用電磁弁
21,22は閉状態のままで、充填用電磁弁10が開状
態にされる(ステップS8)。このような状態で、回収
容器8内から充填用電磁弁10及び操作弁1を介して被
回収機器内にフロンガスを充填する。
On the other hand, when the filling mode is selected by the operation mode setting / switching unit 23a (step S1), the required filling amount according to the recovered equipment, that is, the filling equipment is set in the operation mode setting / switching unit 23a. It is input as M1) (step S7). Next, the filling mode control unit 23c stores the weighing value of the weighing device 11 at the start of filling as the initial weighing value (M2). In this way, M
After 1 and M2 are stored in the memory, the backflow preventing solenoid valves 21 and 22 are kept closed and the filling solenoid valve 10 is opened (step S8). In such a state, CFC gas is filled from the inside of the collection container 8 through the filling electromagnetic valve 10 and the operation valve 1 into the collection target device.

【0018】このとき、充填モード制御部23cでは、
計量装置11による計量値(M3)を一定時間毎に検出
し、初期計量値(M2)からの減少量(M2−M3)を
求め、M2−M3≧M1の条件を満たしているかどうか
を判定する(ステップS9)。上記の条件が満たされ
る、即ち回収容器8内のフロンガスの減少量が必要充填
量以上となると、即座に充填用電磁弁10が閉じられ、
充填運転が終了する(ステップS10)。
At this time, in the filling mode control section 23c,
The weighing value (M3) by the weighing device 11 is detected at regular time intervals, the amount of decrease (M2-M3) from the initial weighing value (M2) is obtained, and it is determined whether or not the condition of M2-M3 ≧ M1 is satisfied. (Step S9). When the above condition is satisfied, that is, when the amount of reduced CFC gas in the recovery container 8 becomes equal to or more than the required filling amount, the filling solenoid valve 10 is immediately closed,
The filling operation ends (step S10).

【0019】上記のようなフロンガス回収装置では、被
回収機器へのフロンガスの必要充填量を設定値として制
御装置23に入力しておき、回収容器8内のフロンガス
の減少量を設定値と比較しながら充填を行い、過充填さ
れる前に充填用電磁弁10を自動的に閉じるようにした
ので、過充填及び充填不足をより確実かつ容易に防止す
ることができる。
In the CFC gas recovery apparatus as described above, the required amount of CFC gas to be recovered is input to the control unit 23 as a set value, and the decrease amount of CFC gas in the recovery container 8 is compared with the set value. However, since the filling is performed and the filling solenoid valve 10 is automatically closed before overfilling, overfilling and underfilling can be prevented more reliably and easily.

【0020】また、液化精製手段7に一対の逆流防止用
電磁弁21,22を設け、これらの電磁弁21,22を
充填時に閉じるようにしたので、被回収機器へのフロン
ガスの充填時に、液化精製手段7内の未精製の残留フロ
ンガスが被回収機器に逆流するのが防止され、従って残
留フロンガスの大気放出も防止される。
Further, since a pair of backflow preventing solenoid valves 21 and 22 are provided in the liquefaction refining means 7 and these solenoid valves 21 and 22 are closed at the time of filling, the liquefaction is made at the time of filling the apparatus to be recovered with CFC gas. It is possible to prevent the unrefined residual CFC gas in the refining means 7 from flowing back to the recovery target device, and thus prevent the residual CFC gas from being released into the atmosphere.

【0021】なお、上記実施例では第2の逆流防止用電
磁弁22がストレーナ5のメンテナンス用の弁を兼ねる
ものを示したが、別の弁としてもよい。
In the above embodiment, the second backflow preventing solenoid valve 22 also serves as a valve for maintenance of the strainer 5, but another valve may be used.

【0022】[0022]

【0023】[0023]

【発明の効果】この発明のフロンガス回収装置は、液化
精製手段に一対の逆流防止用電磁弁を設け、被回収機器
へのフロンガスの充填時に、一対の逆流防止用電磁弁を
自動的に閉じ、液化精製手段内の残留フロンガスを閉じ
込めるようにしたので、未精製の残留フロンガスが被回
収機器に逆流するのを防止することができ、残留フロン
ガスの大気放出を防止することができるという効果を奏
する。また、被回収機器へのフロンガス充填時に、計量
装置による測定値の充填開始時からの減少量を、被回収
機器に応じて入力された設定値と比較し、減少量が設定
値を超える前に充填用電磁弁を閉じるようにしたので、
過充填及び充填不足をより確実かつ容易に防止すること
ができるという効果を奏する。
EFFECT OF THE INVENTION The CFC gas recovery apparatus of the present invention is provided with a pair of backflow preventing solenoid valves in the liquefaction refining means, and automatically closes the pair of backflow preventing solenoid valves when the collected equipment is filled with CFC gas. Since the residual CFC gas in the liquefaction refining means is confined, it is possible to prevent the unrefined residual CFC gas from flowing back to the recovery target device, and it is possible to prevent the residual CFC gas from being released into the atmosphere. In addition, when the collected equipment is filled with CFC gas,
The amount of decrease measured by the device from the start of filling is recovered.
Compared with the set value input according to the device, the reduction amount is set
Since the solenoid valve for filling is closed before exceeding the value,
Prevent overfilling and underfilling more reliably and easily
There is an effect that can be.

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

【図1】 この発明の一実施例によるフロンガス回収装
置を示す構成図である。
FIG. 1 is a configuration diagram showing a fluorocarbon recovery device according to an embodiment of the present invention.

【図2】 図1の装置の動作を説明するためのフローチ
ャートである。
2 is a flow chart for explaining the operation of the apparatus of FIG.

【図3】 従来のフロンガス回収装置の一例を示す構成
図である。
FIG. 3 is a configuration diagram showing an example of a conventional CFC gas recovery apparatus.

【符号の説明】[Explanation of symbols]

1 機器接続用操作弁(機器接続弁)、7 液化精製手
段、8 回収容器、9容器接続用操作弁(容器接続
弁)、10 充填用電磁弁、11 計量装置、21,2
2 逆流防止用電磁弁、23 制御装置。
1 device connecting operation valve (device connecting valve), 7 liquefaction refining means, 8 recovery container, 9 container connecting operating valve (container connecting valve), 10 filling solenoid valve, 11 metering device, 21, 2
2 Solenoid valve for backflow prevention, 23 Control device.

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) F17C 5/00 - 5/06 F25B 45/00 ─────────────────────────────────────────────────── ─── Continuation of the front page (58) Fields surveyed (Int.Cl. 7 , DB name) F17C 5/00-5/06 F25B 45/00

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 機器接続弁を介して被回収機器に接続さ
れ、フロンガスを液化精製する液化精製手段と、 この液化精製手段に容器接続弁を介して接続されている
回収容器と、 上記機器接続弁及び上記容器接続弁の間に上記液化精製
手段と並列に接続されている充填用電磁弁と、 上記液化精製手段に設けられ、上記液化精製手段内の未
精製の残留フロンガスを上記液化精製手段内に閉じ込め
るための一対の逆流防止用電磁弁と、 これら一対の逆流防止用電磁弁及び上記充填用電磁弁に
接続され、上記被回収機器へのフロンガス充填時に上記
一対の逆流防止用電磁弁を閉じるための信号を出力する
制御装置とを備えていることを特徴とするフロンガス回
収装置。
1. A liquefaction and refining means for liquefying and refining CFC gas, which is connected to an equipment to be recovered via an equipment connection valve, a recovery container connected to the liquefaction and refining means via a container connection valve, and the equipment connection. A solenoid valve for filling, which is connected in parallel with the liquefaction and purification means between the valve and the container connection valve, and an unpurified residual CFC gas in the liquefaction and purification means, which is provided in the liquefaction and purification means, is liquefied and purified by the liquefaction and purification means. A pair of backflow preventing solenoid valves to be confined inside, and a pair of the backflow preventing solenoid valves and the filling solenoid valve, which are connected to the pair of backflow preventing solenoid valves at the time of filling the collected device with CFC gas. A Freon gas recovery device, comprising: a control device that outputs a signal for closing.
【請求項2】 上記回収容器の重量を測定する計量装置
をさらに備え、 上記制御装置は、上記 計量装置及び上記充填用電磁弁に
接続され、上記被回収機器へのフロンガス充填時に、上
記計量装置による計量値の充填開始時からの減少量を、
上記被回収機器に応じて入力された設定値と比較し、上
記減少量が上記設定値を超える前に上記充填用電磁弁を
閉じるための信号を出力することを特徴とする請求項1
記載のフロンガス回収装置。
2. A weighing device for measuring the weight of the recovery container
Further, the control device is connected to the measuring device and the filling solenoid valve, at the time of filling CFC gas into the recovery target device, the reduction amount from the start of filling the measured value by the measuring device,
It was compared with a set value input in response to the target collection device, according to claim 1 in which said reduction is characterized and Turkey to output a signal for closing the filling solenoid valve before exceeding the set value
CFC gas recovery device described .
JP22692994A 1994-09-21 1994-09-21 Freon gas recovery device Expired - Lifetime JP3530592B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22692994A JP3530592B2 (en) 1994-09-21 1994-09-21 Freon gas recovery device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22692994A JP3530592B2 (en) 1994-09-21 1994-09-21 Freon gas recovery device

Publications (2)

Publication Number Publication Date
JPH0893997A JPH0893997A (en) 1996-04-12
JP3530592B2 true JP3530592B2 (en) 2004-05-24

Family

ID=16852823

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22692994A Expired - Lifetime JP3530592B2 (en) 1994-09-21 1994-09-21 Freon gas recovery device

Country Status (1)

Country Link
JP (1) JP3530592B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020051627A (en) * 2000-12-23 2002-06-29 이구택 Apparatus for preventing backflow of hydrogen gas

Also Published As

Publication number Publication date
JPH0893997A (en) 1996-04-12

Similar Documents

Publication Publication Date Title
US7832222B2 (en) Background tank fill based on refrigerant composition
EP2591929B1 (en) Apparatus and method for identifying and operating air purge in safe mode and having a dip tube
US5095713A (en) Refrigerant handling system and method with multiple refrigerant capability
EP0519859B1 (en) Method and apparatus for recovering refrigerant
JP5821412B2 (en) Refrigerant filling device
US5099653A (en) Apparatus for purification and recovery of refrigrant
JP3530592B2 (en) Freon gas recovery device
US5078756A (en) Apparatus and method for purification and recovery of refrigerant
EP0271429A1 (en) Heat pump charging
WO1998013653A1 (en) Refrigerant recycle and reclaim system
US6530237B2 (en) Refrigeration system pressure control using a gas volume
CA2112204C (en) Purification of refrigerant
WO2003008878A1 (en) Refrigerator
US5243831A (en) Apparatus for purification and recovery of refrigerant
JP2012202606A (en) Refrigerant recovery method
US5400606A (en) Apparatus for recovering refrigerant
JP3375906B2 (en) Control method and device for helium liquefaction device
JPH0611216A (en) Device and method for recovering refrigerant
WO1989012792A1 (en) Method and apparatus for full evacuation of air conditioner or refrigeration system
JPH05322330A (en) Freezer device
JPH05248717A (en) Air conditioner and pump-down operating method
JP2004301420A (en) Method of updating refrigerating equipment
JPH07332811A (en) Refrigerator, method for recovering refrigerant therefrom and method for modifying the same
JP3326998B2 (en) Refrigerant recovery device
JP2008256326A (en) Refrigerant collecting system

Legal Events

Date Code Title Description
TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20040224

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20040301

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090305

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090305

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100305

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110305

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110305

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120305

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120305

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130305

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20140305

Year of fee payment: 10

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

EXPY Cancellation because of completion of term