JP2000292033A - Purging unit for refrigerator - Google Patents
Purging unit for refrigeratorInfo
- Publication number
- JP2000292033A JP2000292033A JP11094905A JP9490599A JP2000292033A JP 2000292033 A JP2000292033 A JP 2000292033A JP 11094905 A JP11094905 A JP 11094905A JP 9490599 A JP9490599 A JP 9490599A JP 2000292033 A JP2000292033 A JP 2000292033A
- Authority
- JP
- Japan
- Prior art keywords
- condenser
- gas
- purge
- refrigerant
- refrigerator
- 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
Links
- 238000010926 purge Methods 0.000 title claims abstract description 108
- 239000003507 refrigerant Substances 0.000 claims abstract description 93
- 239000007788 liquid Substances 0.000 claims abstract description 14
- 238000001816 cooling Methods 0.000 claims abstract description 12
- 238000004781 supercooling Methods 0.000 claims abstract 2
- 238000011084 recovery Methods 0.000 claims description 16
- 238000001179 sorption measurement Methods 0.000 claims description 15
- 238000007599 discharging Methods 0.000 claims description 10
- 238000000605 extraction Methods 0.000 claims description 3
- 238000010586 diagram Methods 0.000 description 6
- 230000007423 decrease Effects 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 238000009833 condensation Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 3
- 230000001172 regenerating effect Effects 0.000 description 2
- 238000000638 solvent extraction Methods 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 239000003990 capacitor Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B43/00—Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat
- F25B43/04—Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat for withdrawing non-condensible gases
- F25B43/046—Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat for withdrawing non-condensible gases for sorption type systems
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Power Engineering (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Sorption Type Refrigeration Machines (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、冷凍機内に漏れ込
む空気等の不凝縮ガスを抽気して機外に排出し、冷媒を
回収する冷凍機の抽気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 bleed air recovery apparatus for recovering refrigerant by extracting non-condensable gas such as air leaking into a refrigerator and discharging the same outside the refrigerator.
【0002】[0002]
【従来の技術】図1は従来のこの種の抽気回収装置を有
する冷凍機の概略構成を示す図である。図示するよう
に、抽気回収装置は、パージコンデンサ1、パージポン
プ6、差圧スイッチ4、電磁弁5等を具備する。パージ
コンデンサ1はコンデンサ室1aとフロート弁室1bの
上下2室に分かれており、コンデンサ室1aはコンデン
サとして作用し、冷凍機のコンデンサ11と連絡配管7
及びオリフィス9によって連通している。2. Description of the Related Art FIG. 1 is a diagram showing a schematic configuration of a conventional refrigerator having this type of bleed gas recovery device. As shown in the drawing, the bleed air recovery device includes a purge condenser 1, a purge pump 6, a differential pressure switch 4, a solenoid valve 5, and the like. The purge condenser 1 is divided into two upper and lower chambers, a condenser chamber 1a and a float valve chamber 1b. The condenser chamber 1a functions as a condenser, and is connected to the condenser 11 of the refrigerator and the communication pipe 7.
And an orifice 9.
【0003】パージコンデンサ1のコンデンサ室1aに
は、冷却コイル2が配置されており、該冷却コイル2に
は冷凍機のクーラ12内の冷媒液で過冷却されたコンデ
ンサ11の液冷媒が冷媒ポンプ13により冷媒フィルタ
ー14を通して流れ、常にパージコンデンサ1内を冷却
している。このためパージコンデンサ1内の圧力はコン
デンサ11の圧力よりも低く、その差圧によってコンデ
ンサ11内のガスは連絡配管7及びオリフィス9を通っ
てパージコンデンサ1内に流入する。そこで冷媒ガスは
冷却液化し、冷媒液は下のフロート弁室1bに流れる。
該フロート弁室1bに一定量以上の冷媒が溜るとフロー
ト弁3が開いて冷媒はクーラ12に戻る。このとき不凝
縮ガスはそのままパージコンデンサ1内に残るため、次
第に蓄積されパージコンデンサ1内の圧力が上昇する。In the condenser chamber 1a of the purge condenser 1, a cooling coil 2 is disposed. In the cooling coil 2, a liquid refrigerant of the condenser 11, which is supercooled by a refrigerant liquid in a cooler 12 of the refrigerator, is supplied with a refrigerant pump. 13 flows through the refrigerant filter 14 and always cools the inside of the purge condenser 1. Therefore, the pressure in the purge condenser 1 is lower than the pressure in the condenser 11, and the gas in the condenser 11 flows into the purge condenser 1 through the communication pipe 7 and the orifice 9 due to the pressure difference. There, the refrigerant gas is cooled and liquefied, and the refrigerant liquid flows to the lower float valve chamber 1b.
When a certain amount or more of the refrigerant accumulates in the float valve chamber 1b, the float valve 3 opens and the refrigerant returns to the cooler 12. At this time, since the non-condensable gas remains in the purge condenser 1 as it is, it is gradually accumulated and the pressure in the purge condenser 1 increases.
【0004】パージコンデンサ1内の圧力が上昇し、コ
ンデンサ11内の圧力との差圧が所定の値まで低下する
と、差圧スイッチ4の出力により、制御部10は電磁弁
5を開くと同時にパージポンプ6を起動し、パージコン
デンサ1内の不凝縮ガスを大気中に排出する。パージコ
ンデンサ1内の不凝縮ガスが排出され、該パージコンデ
ンサ1内の圧力が下がり、コンデンサ11内の圧力との
差圧が上昇すると差圧スイッチ4の出力により、制御部
10は電磁弁5を閉じ、パージポンプ6を停止して、不
凝縮ガスの排出は終了する。When the pressure in the purge condenser 1 rises and the pressure difference from the pressure in the condenser 11 falls to a predetermined value, the output of the differential pressure switch 4 causes the control unit 10 to open the solenoid valve 5 and to purge simultaneously. The pump 6 is started to discharge the non-condensable gas in the purge condenser 1 to the atmosphere. When the non-condensable gas in the purge condenser 1 is discharged, the pressure in the purge condenser 1 decreases, and the differential pressure from the pressure in the condenser 11 increases, the output of the differential pressure switch 4 causes the control unit 10 to operate the solenoid valve 5. Closed, the purge pump 6 is stopped, and the discharge of the non-condensable gas ends.
【0005】[0005]
【発明が解決しようとする課題】しかしながら、上記構
成の抽気回収装置においては、パージポンプ6の運転中
も冷凍機のコンデンサ11から冷媒ガスを含む不凝縮ガ
スがパージコンデンサ1内に流入するため、不凝縮ガス
と共に冷媒ガスが大気中に放出されるという問題があっ
た。また、パージコンデンサ1内の圧力とコンデンサ1
1内の圧力との差圧が所定の値まで低下することで、パ
ージコンデンサ1内の不凝縮ガスを排出するため、パー
ジコンデンサ1内の不凝縮ガスの濃度が十分高くならな
いうちに不凝縮ガスの排出が行なわれ、不凝縮ガスの排
出頻度が多くなり、パージポンプ6や電磁弁5の作動頻
度が多くなるという問題もあった。また、不凝縮ガスの
排出に伴って該不凝縮ガス中に含まれる微量な冷媒ガス
も大気中に排出されるという問題もあった。However, in the bleed gas recovery apparatus having the above-mentioned structure, the non-condensable gas containing the refrigerant gas flows into the purge condenser 1 from the condenser 11 of the refrigerator even while the purge pump 6 is operating. There is a problem that the refrigerant gas is released into the atmosphere together with the non-condensable gas. Also, the pressure in the purge condenser 1 and the condenser 1
When the pressure difference between the pressure in the purge condenser 1 and the pressure in the purge condenser 1 decreases to a predetermined value, the non-condensable gas in the purge condenser 1 is discharged. Is discharged, the frequency of discharging the non-condensable gas increases, and the operation frequency of the purge pump 6 and the solenoid valve 5 also increases. Further, there is also a problem that a small amount of refrigerant gas contained in the non-condensable gas is discharged to the atmosphere as the non-condensable gas is discharged.
【0006】本発明は上述の点に鑑みてなされたもの
で、上記問題点を除去し、不凝縮ガスの排出に伴って冷
媒ガスの排出が殆どなく、不凝縮ガス排出頻度が少なく
て済み、且つ不凝縮ガスの排出と同伴して排出される微
量の冷媒ガスも吸着回収できる冷凍機の抽気回収装置を
提供することを目的とする。SUMMARY OF THE INVENTION The present invention has been made in view of the above points, and eliminates the above-mentioned problems. Accordingly, there is almost no discharge of refrigerant gas with discharge of non-condensable gas, and the frequency of discharge of non-condensable gas can be reduced. It is another object of the present invention to provide a bleed gas recovery device for a refrigerator capable of adsorbing and recovering a small amount of refrigerant gas discharged together with discharge of non-condensable gas.
【0007】[0007]
【課題を解決するための手段】上記課題を解決するため
請求項1に記載の発明は、冷凍機のコンデンサに連絡配
管を介してパージコンデンサを接続し、該コンデンサの
内圧と該パージコンデンサの内圧との差圧により該コン
デンサから冷媒ガスを含む不凝縮ガスを該パージコンデ
ンサ内に導入すると共に、該パージコンデンサ内に配置
された冷却コイルに冷凍機のコンデンサ又はエコノマイ
ザの液冷媒を過冷却して導き、該パージコンデンサ内を
冷却して該冷媒ガスを凝縮して冷媒液として回収し、該
パージコンデンサ内の不凝縮ガスを機外に排出するよう
に構成した冷凍機の抽気回収装置において、連絡配管に
開閉弁を設け、パージコンデンサ内の不凝縮ガスを機外
に排出する時、該開閉弁を閉じて、コンデンサから冷媒
ガスを含む不凝縮ガスの該パージコンデンサ内への流入
を遮断することを特徴とする。According to a first aspect of the present invention, a purge condenser is connected to a condenser of a refrigerator through a communication pipe, and an internal pressure of the condenser and an internal pressure of the purge condenser are solved. A non-condensable gas containing a refrigerant gas is introduced from the condenser into the purge condenser by a pressure difference between the condenser condenser and the cooling coil disposed in the purge condenser to supercool the condenser of the refrigerator or the liquid refrigerant of the economizer. In the bleed gas recovery device of the refrigerator, the cooling device is configured to cool the inside of the purge condenser, condense the refrigerant gas and recover it as a refrigerant liquid, and discharge the non-condensable gas in the purge condenser to the outside of the device. When an on-off valve is provided in the piping and the non-condensable gas in the purge condenser is discharged out of the machine, the on-off valve is closed and non-condensation containing refrigerant gas from the condenser is performed. Characterized by interrupting the flow of the scan of the purge within the capacitor.
【0008】上記のように、パージコンデンサ内の不凝
縮ガスを機外に排出する時、開閉弁を閉じて、コンデン
サから冷媒ガスを含む不凝縮ガスの該パージコンデンサ
内への流入を遮断するので、不凝縮ガスを機外に排出す
る時にコンデンサからの冷媒ガスが排出されることがな
い。As described above, when discharging the non-condensable gas in the purge condenser to the outside of the apparatus, the on-off valve is closed to shut off the flow of the non-condensable gas containing the refrigerant gas from the condenser into the purge condenser. In addition, the refrigerant gas is not discharged from the condenser when the non-condensable gas is discharged outside the apparatus.
【0009】また、請求項2に記載の発明は、請求項1
に記載の冷凍機の抽気回収装置において、開閉弁を閉じ
てコンデンサから冷媒ガスを含む不凝縮ガスの該パージ
コンデンサ内への流入を遮断すると共に、該パージコン
デンサ内の冷媒ガス濃度が最小限になるまで凝縮させ、
その後に該開閉弁を開いてコンデンサから冷媒ガスを含
む不凝縮ガスを該パージコンデンサ内に流入させ、該動
作を複数回繰返し、該パージコンデンサ内の不凝縮ガス
濃度を高め、該不凝縮ガスを機外に排出させるように構
成したことを特徴とする。The invention described in claim 2 is the first invention.
In the bleed gas extraction device of the refrigerator described in the above, while closing the on-off valve to block the inflow of non-condensable gas containing refrigerant gas from the condenser into the purge condenser, the refrigerant gas concentration in the purge condenser is minimized. Condense until
Thereafter, the on-off valve is opened to allow the non-condensable gas including the refrigerant gas to flow into the purge condenser from the condenser, and the operation is repeated a plurality of times to increase the concentration of the non-condensable gas in the purge condenser, and It is characterized by being configured to be discharged outside the machine.
【0010】上記のように開閉弁を閉じてパージコンデ
ンサ内の冷媒ガス濃度が最小限になるまで凝縮させる動
作を複数回繰返し、該パージコンデンサ内の不凝縮ガス
濃度を高めてから機外に排出させるように構成すること
により、不凝縮ガスの排出頻度が少なくて済み、不凝縮
ガス排出手段を構成する機器の長寿命化等を図ることが
できる。As described above, the operation of closing the on-off valve and condensing the refrigerant gas in the purge condenser until the concentration of the refrigerant gas is minimized is repeated a plurality of times to increase the concentration of non-condensable gas in the purge condenser and then discharge the gas to the outside of the apparatus. With such a configuration, the frequency of discharging the non-condensable gas can be reduced, and the life of the device constituting the non-condensable gas discharging means can be extended.
【0011】また、請求項3に記載の発明は、請求項1
又は2に記載の冷凍機の抽気回収装置において、機外に
排出させる不凝縮ガスを冷媒吸着フィルターを通して大
気に排出することを特徴とする。[0011] The invention according to claim 3 is based on claim 1.
Alternatively, in the bleed gas extraction device according to 2, the non-condensable gas discharged outside the device is discharged to the atmosphere through a refrigerant adsorption filter.
【0012】上記のように、機外に排出させる不凝縮ガ
スを冷媒吸着フィルターを通して大気に排出するので、
不凝縮ガスに含まれる微量の冷媒ガスは冷媒吸着フィル
ターに吸着されるから、大気中には冷媒ガスは排出され
ないし、該冷媒吸着フィルターを再生処理することによ
り吸着された冷媒は回収され、吸着フィルターは再利用
できる。As described above, the non-condensable gas discharged outside the apparatus is discharged to the atmosphere through the refrigerant adsorption filter.
Since a small amount of refrigerant gas contained in the non-condensable gas is adsorbed by the refrigerant adsorption filter, the refrigerant gas is not discharged into the atmosphere, and the refrigerant adsorbed by regenerating the refrigerant adsorption filter is recovered and adsorbed. Filters can be reused.
【0013】[0013]
【発明の実施の形態】以下、本発明の実施の形態例を図
面に基づいて説明する。図2は本発明に係る抽気回収装
置を有する冷凍機の概略構成を示す図である。本抽気回
収装置は、パージコンデンサ1、パージポンプ6、差圧
スイッチ4、電磁弁5等を具備し、パージコンデンサ1
はコンデンサ室1aとフロート弁室1bとに分かれて、
コンデンサ室1aはコンデンサとして作用し、冷凍機の
コンデンサ11と連絡配管7及びオリフィス9によって
連通し、コンデンサ室1aに配置された冷却コイル2に
は冷凍機のクーラ12内の冷媒液で過冷却されたコンデ
ンサ11の液冷媒が冷媒ポンプ13により冷媒フィルタ
ー14を通して流れ、常にパージコンデンサ1内を冷却
している等は図1の従来例と同一である。Embodiments of the present invention will be described below with reference to the drawings. FIG. 2 is a diagram showing a schematic configuration of a refrigerator having the bleed air recovery device according to the present invention. The bleed gas recovery device includes a purge condenser 1, a purge pump 6, a differential pressure switch 4, a solenoid valve 5, and the like.
Is divided into a condenser chamber 1a and a float valve chamber 1b,
The condenser chamber 1a functions as a condenser, communicates with the condenser 11 of the refrigerator by the communication pipe 7 and the orifice 9, and the cooling coil 2 disposed in the condenser chamber 1a is supercooled by the refrigerant liquid in the cooler 12 of the refrigerator. The liquid refrigerant in the condenser 11 flows through the refrigerant filter 14 by the refrigerant pump 13 and always cools the inside of the purge condenser 1, which is the same as the conventional example of FIG.
【0014】本発明が図1の従来例と相違する点は、パ
ージコンデンサ1と冷凍機のコンデンサ11を接続する
連絡配管7に電磁弁8を設けた点、パージポンプ6によ
り排出されるパージコンデンサ1からの不凝縮ガスが冷
媒吸着フィルター15を通って大気中に排出されるよう
になっている点、パージポンプ6及び電磁弁5の外に電
磁弁8の動作も制御部10の制御で行なっている点であ
る。The present invention is different from the conventional example shown in FIG. 1 in that a solenoid valve 8 is provided in a communication pipe 7 connecting a purge condenser 1 and a condenser 11 of a refrigerator, and a purge condenser discharged by a purge pump 6. In addition to the purge pump 6 and the solenoid valve 5, the operation of the solenoid valve 8 is also controlled by the control unit 10 in that the non-condensable gas from 1 is discharged to the atmosphere through the refrigerant adsorption filter 15. That is the point.
【0015】上記構成の抽気回収装置において、パージ
コンデンサ1における冷媒の冷却は上述のように、従来
例と同じく冷凍機のクーラ12で過冷却した冷凍機の凝
縮冷媒(液冷媒)を使用している。エコノマイザサイク
ルの冷凍機の場合は、エコノマイザの液冷媒を使用する
と、より低温の冷却冷媒を供給できるため、パージコン
デンサ1の圧力が低くなり、パージコンデンサ1の冷媒
ガス濃度を低減できる。In the bleed gas recovery apparatus having the above-described structure, the cooling of the refrigerant in the purge condenser 1 is performed by using the condensed refrigerant (liquid refrigerant) of the refrigerator supercooled by the cooler 12 of the refrigerator as in the conventional example, as described above. I have. In the case of the refrigerator of the economizer cycle, when the liquid refrigerant of the economizer is used, a lower-temperature cooling refrigerant can be supplied, so that the pressure of the purge condenser 1 decreases, and the refrigerant gas concentration of the purge condenser 1 can be reduced.
【0016】パージコンデンサ1への不凝縮ガスの集積
は従来と同様、冷凍機のコンデンサ11内の圧力とパー
ジコンデンサ1内の圧力差による。即ち、この差圧によ
ってコンデンサ11内のガスを連絡配管7及びオリフィ
ス9を通ってパージコンデンサ1内に流入させることで
行なっている。そこで冷媒ガスは冷却液化し、該冷媒液
は下のフロート弁室1bに流れ込む。該フロート弁室1
bに一定量以上の冷媒が溜るとフロート弁3が開いて冷
媒はクーラ12に戻る。このとき不凝縮ガスはそのまま
パージコンデンサ1内に残る。The accumulation of the non-condensable gas in the purge condenser 1 depends on the difference between the pressure in the condenser 11 of the refrigerator and the pressure in the purge condenser 1 as in the prior art. That is, the gas in the condenser 11 is caused to flow into the purge condenser 1 through the communication pipe 7 and the orifice 9 by this differential pressure. There, the refrigerant gas is cooled and liquefied, and the refrigerant liquid flows into the lower float valve chamber 1b. The float valve chamber 1
When a certain amount or more of the refrigerant accumulates in b, the float valve 3 opens and the refrigerant returns to the cooler 12. At this time, the non-condensable gas remains in the purge condenser 1 as it is.
【0017】パージコンデンサ1内に不凝縮ガスが蓄積
され、パージコンデンサ1内の圧力が上昇し、コンデン
サ11内の圧力との差圧が所定の値まで低下すると、差
圧スイッチ4が作動し、制御部10は電磁弁5を開くと
同時にパージポンプ6を始動し、パージコンデンサ1内
の不凝縮ガスを大気中に排出する。この不凝縮ガスの排
出時に制御部10は電磁弁8を閉じ、コンデンサ11か
らパージコンデンサ1への冷媒ガスを含む不凝縮ガスの
流入を遮断する。これにより従来のように、不凝縮ガス
の排出時にコンデンサ11からパージコンデンサ1を通
って冷媒ガスが機外に排出されることはなくなる。When non-condensable gas is accumulated in the purge condenser 1 and the pressure in the purge condenser 1 rises and the pressure difference from the pressure in the condenser 11 decreases to a predetermined value, the differential pressure switch 4 is activated, The control unit 10 starts the purge pump 6 at the same time as opening the electromagnetic valve 5, and discharges the non-condensable gas in the purge condenser 1 to the atmosphere. When discharging the non-condensable gas, the control unit 10 closes the solenoid valve 8 and shuts off the flow of the non-condensable gas including the refrigerant gas from the condenser 11 to the purge condenser 1. As a result, the refrigerant gas is not discharged from the condenser 11 to the outside through the purge condenser 1 when the non-condensable gas is discharged, unlike the related art.
【0018】パージコンデンサ1内の冷媒ガス濃度を小
さくするため、制御部10は次のような制御を行なう。
差圧スイッチ4が作動した時、電磁弁8を閉じ、パージ
コンデンサ1内に取り込まれた冷媒ガスを更に凝縮させ
る。この凝縮プロセスによりパージコンデンサ1内の冷
媒ガスが充分に凝縮すると、パージコンデンサ1内の圧
力が下がり、差圧スイッチ4が切れる。差圧スイッチ4
が切れると再び電磁弁8を開き、更にコンデンサ11か
ら冷媒ガスを含む不凝縮ガスをパージコンデンサ1内に
導入し、冷媒ガスを凝縮し、不凝縮ガスを蓄積する。The controller 10 performs the following control to reduce the refrigerant gas concentration in the purge condenser 1.
When the differential pressure switch 4 is operated, the solenoid valve 8 is closed, and the refrigerant gas taken into the purge condenser 1 is further condensed. When the refrigerant gas in the purge condenser 1 is sufficiently condensed by the condensation process, the pressure in the purge condenser 1 decreases, and the differential pressure switch 4 is turned off. Differential pressure switch 4
When the power is cut off, the solenoid valve 8 is opened again, and an uncondensable gas containing a refrigerant gas is introduced from the condenser 11 into the purge condenser 1 to condense the refrigerant gas and accumulate the non-condensable gas.
【0019】図3は制御部10における不凝縮ガスのパ
ージ動作フローを示す図である。冷凍機の始動完了後5
分経過したら、先ずパージ用の差圧スイッチ4がONか
否かを判断し(ステップST1)、差圧スイッチ4がO
Nであったら、仕切用の電磁弁8を閉じる(ステップS
T2)。次に差圧スイッチ4の動作カウントが所定値
(図では「5」)になったか否かを判断し(ステップS
T3)、動作カウントが所定値でなかった場合、差圧ス
イッチ4がONした後所定時間(図では「30秒」)経
過したら(ステップST4)、仕切用の電磁弁8を開い
て(ステップST5)、前記ステップST1に戻る。FIG. 3 is a diagram showing a flow of the non-condensable gas purging operation in the control unit 10. After the start of the refrigerator 5
After a lapse of one minute, first, it is determined whether or not the purge differential pressure switch 4 is ON (step ST1).
If the answer is N, the partitioning solenoid valve 8 is closed (step S).
T2). Next, it is determined whether or not the operation count of the differential pressure switch 4 has reached a predetermined value ("5" in the figure) (Step S).
T3) When the operation count is not the predetermined value, when a predetermined time ("30 seconds" in the figure) has elapsed after the differential pressure switch 4 was turned on (step ST4), the partitioning solenoid valve 8 is opened (step ST5). ), And return to step ST1.
【0020】前記ステップST3において、差圧スイッ
チ4の動作カウントが所定値になり、次に差圧スイッチ
4がONした後所定時間(図では「30秒」)経過した
ら(ステップST6)、パージ排出用の電磁弁5を開く
と共に、パージポンプ6を運転する(ステップST
7)。続いてパージポンプ6の運転が所定時間(図では
「10秒」)経過したら(ステップST8)、パージ排
出用の電磁弁5を閉じると共に、パージポンプ6を停止
し(ステップST9)、前記ステップST1に戻る。In step ST3, the operation count of the differential pressure switch 4 reaches a predetermined value, and when a predetermined time ("30 seconds" in the figure) elapses after the differential pressure switch 4 is turned on (step ST6), the purge discharge is performed. The solenoid valve 5 is opened and the purge pump 6 is operated (step ST
7). Subsequently, when the operation of the purge pump 6 has elapsed for a predetermined time ("10 seconds" in the figure) (step ST8), the purge discharge solenoid valve 5 is closed, and the purge pump 6 is stopped (step ST9). Return to
【0021】なお、図2に示す例ではパージポンプ6を
設けているが、このパージポンプ6は必ずしも必要なも
のではない。但し、パージポンプ6を設けない場合は、
パージコンデンサ1内の圧力が大気圧以上であるか否か
を判断するスイッチを設け、該スイッチが大気圧以上と
判断したら、パージ排出用の電磁弁5を開くようにす
る。Although the purge pump 6 is provided in the example shown in FIG. 2, the purge pump 6 is not always required. However, when the purge pump 6 is not provided,
A switch for determining whether or not the pressure in the purge condenser 1 is higher than the atmospheric pressure is provided. When the switch determines that the pressure is higher than the atmospheric pressure, the purge discharge solenoid valve 5 is opened.
【0022】上記プロセスを複数回繰り返し、パージコ
ンデンサ1内の不凝縮ガスの濃度が充分高くなったら電
磁弁5を開き、パージポンプ6を起動し、パージコンデ
ンサ1内の不凝縮ガスを機外に放出する。The above process is repeated a plurality of times. When the concentration of the non-condensable gas in the purge condenser 1 becomes sufficiently high, the solenoid valve 5 is opened, the purge pump 6 is started, and the non-condensable gas in the purge condenser 1 is discharged outside the machine. discharge.
【0023】パージコンデンサ1内の不凝縮ガスの濃度
は差圧スイッチ4の動作回数(冷凍機の使用状況によっ
て任意に設定可能とする)により判断する。不凝縮ガス
の濃度の別の判定方法としては、上記電磁弁の開閉及び
パージコンデンサ1内の凝縮プロセスにおけるパージコ
ンデンサ1内の圧力を検知すれば定量的に不凝縮ガスの
蓄積量を判断できる。The concentration of the non-condensable gas in the purge condenser 1 is determined by the number of operations of the differential pressure switch 4 (which can be arbitrarily set depending on the use condition of the refrigerator). As another method of determining the concentration of the non-condensable gas, the amount of the non-condensable gas can be quantitatively determined by detecting the opening and closing of the electromagnetic valve and the pressure in the purge condenser 1 in the condensation process in the purge condenser 1.
【0024】上記のようにして機外に排出される不凝縮
ガスの中には微量の冷媒ガスが含まれ、該不凝縮ガスを
そのまま大気中に放出すると、微量ながら冷媒ガスも大
気中に放出されることになる。そこで、上記不凝縮ガス
の排出部に冷媒吸着フィルター15を設け、排出される
不凝縮ガスを該冷媒吸着フィルター15を通して大気中
に放出する。これにより不凝縮ガスに含まれる微量な冷
媒ガスは冷媒吸着フィルター15に吸着され、冷媒ガス
を含まない不凝縮ガスのみが大気中に放出されることに
なる。この冷媒吸着フィルター15は定期的に交換し、
吸着された冷媒を回収して再生処理した後再利用する。A small amount of refrigerant gas is contained in the non-condensable gas discharged to the outside as described above, and when the non-condensable gas is discharged to the atmosphere as it is, a small amount of the refrigerant gas is also discharged to the air. Will be done. Therefore, a refrigerant adsorption filter 15 is provided at the discharge section of the non-condensable gas, and the discharged non-condensable gas is discharged into the atmosphere through the refrigerant adsorption filter 15. As a result, a small amount of refrigerant gas contained in the non-condensable gas is adsorbed by the refrigerant adsorption filter 15, and only the non-condensable gas containing no refrigerant gas is released to the atmosphere. This refrigerant adsorption filter 15 is replaced regularly,
The adsorbed refrigerant is recovered, regenerated, and reused.
【0025】上記のようにすることにより冷媒の大気中
への放出がなく、冷媒としてフロン系の冷媒を用いる場
合は、環境保全の点から特に有効である。In the case where the refrigerant is not released into the atmosphere by using the above-mentioned method, and a CFC-based refrigerant is used as the refrigerant, it is particularly effective in terms of environmental conservation.
【0026】[0026]
【発明の効果】以上説明したように、各請求項に記載の
発明によれば、下記のような優れた効果が得られる。As described above, according to the invention described in each claim, the following excellent effects can be obtained.
【0027】請求項1に記載の発明によれば、パージコ
ンデンサ内の不凝縮ガスを機外に排出する時、開閉弁を
閉じて、コンデンサから冷媒ガスを含む不凝縮ガスの該
パージコンデンサ内への流入を遮断するので、不凝縮ガ
スを機外に排出する時にコンデンサからの冷媒ガスが排
出されることがない。According to the first aspect of the present invention, when discharging the non-condensable gas in the purge condenser out of the apparatus, the on-off valve is closed and the non-condensable gas containing the refrigerant gas is discharged from the condenser into the purge condenser. , The refrigerant gas is not discharged from the condenser when the non-condensable gas is discharged outside the machine.
【0028】請求項2に記載の発明によれば、開閉弁を
閉じて該パージコンデンサ内の冷媒ガス濃度が最小限に
なるまで凝縮させる動作を複数回繰返し、該パージコン
デンサ内の不凝縮ガス濃度を高めて機外に排出させるよ
うに構成することにより、不凝縮ガスの排出頻度が少な
くて済み、不凝縮ガス排出手段を構成する機器の長寿命
化等を図ることができる。According to the second aspect of the present invention, the operation of closing the on-off valve and condensing the refrigerant gas concentration in the purge condenser until the concentration becomes minimum is repeated a plurality of times, and the non-condensable gas concentration in the purge condenser is repeated. In this case, the frequency of discharging the non-condensable gas can be reduced, and the life of the device constituting the non-condensable gas discharging means can be extended.
【0029】請求項3に記載の発明によれば、機外に排
出させる不凝縮ガスを冷媒吸着フィルターを通して大気
中に排出するので、不凝縮ガスに含まれる微量の冷媒ガ
スは冷媒吸着フィルターに吸着され、大気中には冷媒ガ
スは排出されないし、該冷媒吸着フィルターを再生処理
することにより、吸着された冷媒は回収され、吸着フィ
ルターは再利用できる。According to the third aspect of the present invention, since the non-condensable gas discharged outside the machine is discharged into the atmosphere through the refrigerant adsorption filter, a small amount of refrigerant gas contained in the non-condensable gas is adsorbed by the refrigerant adsorption filter. The refrigerant gas is not discharged into the atmosphere, and the adsorbed refrigerant is recovered by regenerating the refrigerant adsorption filter, so that the adsorption filter can be reused.
【図1】従来のこの種の抽気回収装置を有する冷凍機の
概略構成を示す図である。FIG. 1 is a diagram showing a schematic configuration of a conventional refrigerator having this type of bleed air recovery device.
【図2】本発明に係る抽気回収装置を有する冷凍機の概
略構成を示す図である。FIG. 2 is a diagram showing a schematic configuration of a refrigerator having a bleed air recovery device according to the present invention.
【図3】本発明に係る抽気回収装置の不凝縮ガスのパー
ジ動作フローを示す図である。FIG. 3 is a diagram showing a flow of a non-condensable gas purging operation of the bleed gas recovery device according to the present invention.
1 パージコンデンサ 2 冷却コイル 3 フロート弁 4 差圧スイッチ 5 電磁弁 6 パージポンプ 7 連絡配管 8 電磁弁 9 オリフィス 10 制御部 11 コンデンサ 12 クーラ 13 冷媒ポンプ 14 冷媒フィルター 15 冷媒吸着フィルター DESCRIPTION OF SYMBOLS 1 Purge condenser 2 Cooling coil 3 Float valve 4 Differential pressure switch 5 Solenoid valve 6 Purge pump 7 Communication pipe 8 Solenoid valve 9 Orifice 10 Control part 11 Condenser 12 Cooler 13 Refrigerant pump 14 Refrigerant filter 15 Refrigerant adsorption filter
Claims (3)
パージコンデンサを接続し、該コンデンサの内圧と該パ
ージコンデンサの内圧との差圧により該コンデンサから
冷媒ガスを含む不凝縮ガスを該パージコンデンサ内に導
入すると共に、該パージコンデンサ内に配置された冷却
コイルに前記冷凍機のコンデンサ又はエコノマイザの液
冷媒を過冷却して導き、該パージコンデンサ内を冷却し
て該冷媒ガスを凝縮して冷媒液として回収し、該パージ
コンデンサ内の不凝縮ガスを機外に排出するように構成
した冷凍機の抽気回収装置において、 前記連絡配管に開閉弁を設け、前記パージコンデンサ内
の不凝縮ガスを機外に排出する時、該開閉弁を閉じて、
前記コンデンサから冷媒ガスを含む不凝縮ガスの該パー
ジコンデンサ内への流入を遮断することを特徴とする冷
凍機の抽気回収装置。A purge condenser is connected to a condenser of a refrigerator through a communication pipe, and a non-condensable gas containing a refrigerant gas is removed from the condenser by the pressure difference between the internal pressure of the condenser and the internal pressure of the purge condenser. While supercooling and guiding the liquid refrigerant of the condenser or economizer of the refrigerator to the cooling coil disposed in the purge condenser, and cooling the inside of the purge condenser to condense the refrigerant gas to thereby cool the refrigerant. A bleed gas recovery device for a refrigerator configured to recover as a liquid and discharge the non-condensable gas in the purge condenser to the outside of the machine. When discharging outside, close the on-off valve,
A bleed air recovery device for a refrigerator, wherein an inflow of non-condensable gas including a refrigerant gas from the condenser into the purge condenser is blocked.
において、 前記開閉弁を閉じて前記コンデンサから冷媒ガスを含む
不凝縮ガスの該パージコンデンサ内への流入を遮断する
と共に、該パージコンデンサ内の冷媒ガス濃度が最小限
になるまで凝縮させ、その後に該開閉弁を開いて前記コ
ンデンサから冷媒ガスを含む不凝縮ガスを該パージコン
デンサ内に流入させ、該動作を複数回繰返し、該パージ
コンデンサ内の不凝縮ガス濃度を高め、該不凝縮ガスを
機外に排出させるように構成したことを特徴とする冷凍
機の抽気回収装置。2. The bleed air recovery device for a refrigerator according to claim 1, wherein the on-off valve is closed to block inflow of non-condensable gas containing refrigerant gas from the condenser into the purge condenser, and to purge the gas. The condenser gas is condensed until the concentration of the refrigerant gas in the condenser becomes minimum, and then the on-off valve is opened to allow the non-condensable gas containing the refrigerant gas to flow from the condenser into the purge condenser, and the operation is repeated a plurality of times. A bleed gas recovery device for a refrigerator, wherein the concentration of non-condensable gas in a purge condenser is increased and the non-condensable gas is discharged outside the device.
収装置において、 前記機外に排出させる不凝縮ガスを冷媒吸着フィルター
を通して大気に排出することを特徴とする冷凍機の抽気
回収装置。3. The bleed gas extraction device for a refrigerator according to claim 1, wherein the non-condensable gas discharged outside the device is discharged to the atmosphere through a refrigerant adsorption filter. .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11094905A JP2000292033A (en) | 1999-04-01 | 1999-04-01 | Purging unit for refrigerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11094905A JP2000292033A (en) | 1999-04-01 | 1999-04-01 | Purging unit for refrigerator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2000292033A true JP2000292033A (en) | 2000-10-20 |
Family
ID=14123047
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11094905A Pending JP2000292033A (en) | 1999-04-01 | 1999-04-01 | Purging unit for refrigerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2000292033A (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003106711A (en) * | 2001-09-27 | 2003-04-09 | Daikin Ind Ltd | Absorption refrigeration equipment |
| JP2011075208A (en) * | 2009-09-30 | 2011-04-14 | Ebara Refrigeration Equipment & Systems Co Ltd | Bleed air recovery device, method for operating the bleed air recovery device, and turbo refrigerator including the bleed air recovery device |
| JP2011133192A (en) * | 2009-12-25 | 2011-07-07 | Ebara Refrigeration Equipment & Systems Co Ltd | Refrigerant recovering device |
| WO2012069048A3 (en) * | 2010-11-23 | 2012-08-30 | Invensor Gmbh | Vacuum container for removing foreign gases from an adsorption chiller |
| WO2014041083A1 (en) * | 2012-09-12 | 2014-03-20 | Invensor Gmbh | Method for the controlled removal of foreign gases from a sorption device with an inert gas trap |
| WO2016047305A1 (en) * | 2014-09-25 | 2016-03-31 | 三菱重工業株式会社 | Control device and control method for bleed device |
| JP2017180994A (en) * | 2016-03-31 | 2017-10-05 | 三菱重工サーマルシステムズ株式会社 | Extraction device, refrigerator having the same, and control method of the same |
| JP2021509464A (en) * | 2017-12-31 | 2021-03-25 | テクニオン リサーチ アンド ディベロップメント ファンデーション リミテッド | Purge system for closed cycle absorption heat pumps |
-
1999
- 1999-04-01 JP JP11094905A patent/JP2000292033A/en active Pending
Cited By (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003106711A (en) * | 2001-09-27 | 2003-04-09 | Daikin Ind Ltd | Absorption refrigeration equipment |
| JP2011075208A (en) * | 2009-09-30 | 2011-04-14 | Ebara Refrigeration Equipment & Systems Co Ltd | Bleed air recovery device, method for operating the bleed air recovery device, and turbo refrigerator including the bleed air recovery device |
| JP2011133192A (en) * | 2009-12-25 | 2011-07-07 | Ebara Refrigeration Equipment & Systems Co Ltd | Refrigerant recovering device |
| US9631851B2 (en) | 2010-11-23 | 2017-04-25 | Invensor Gmbh | Vacuum container for removing foreign gases from an adsorption refrigeration machine |
| WO2012069048A3 (en) * | 2010-11-23 | 2012-08-30 | Invensor Gmbh | Vacuum container for removing foreign gases from an adsorption chiller |
| JP2014500944A (en) * | 2010-11-23 | 2014-01-16 | インベンソール ゲーエムベーハー | Vacuum container for removing foreign gas from adsorption refrigerator |
| US20130239595A1 (en) * | 2010-11-23 | 2013-09-19 | Invensor Gmbh | Vacuum container for removing foreign gases from an adsorption refrigeration machine |
| WO2014041083A1 (en) * | 2012-09-12 | 2014-03-20 | Invensor Gmbh | Method for the controlled removal of foreign gases from a sorption device with an inert gas trap |
| US10495363B2 (en) | 2014-09-25 | 2019-12-03 | Mitsubishi Heavy Industries Thermal Systems, Ltd. | Control device and control method for bleed device |
| WO2016047305A1 (en) * | 2014-09-25 | 2016-03-31 | 三菱重工業株式会社 | Control device and control method for bleed device |
| JP2017180994A (en) * | 2016-03-31 | 2017-10-05 | 三菱重工サーマルシステムズ株式会社 | Extraction device, refrigerator having the same, and control method of the same |
| WO2017170649A1 (en) * | 2016-03-31 | 2017-10-05 | 三菱重工サーマルシステムズ株式会社 | Purging device, refrigerator equipped with same, and method for controlling purging device |
| CN108700355A (en) * | 2016-03-31 | 2018-10-23 | 三菱重工制冷空调系统株式会社 | Air extractor and have its refrigeration machine and air extractor control method |
| US20190056159A1 (en) * | 2016-03-31 | 2019-02-21 | Mitsubishi Heavy Industries Thermal Systems, Ltd. | Purging device, chiller equipped with same, and method for controlling purging device |
| CN108700355B (en) * | 2016-03-31 | 2020-09-11 | 三菱重工制冷空调系统株式会社 | Air extraction device, refrigerator provided with same, and control method for air extraction device |
| JP2021509464A (en) * | 2017-12-31 | 2021-03-25 | テクニオン リサーチ アンド ディベロップメント ファンデーション リミテッド | Purge system for closed cycle absorption heat pumps |
| JP7313356B2 (en) | 2017-12-31 | 2023-07-24 | テクニオン リサーチ アンド ディベロップメント ファンデーション リミテッド | Motorless Purge System and Method for Removing Non-Condensable Gases from Closed Cycle Absorption Transformer Heat Pump and Closed Cycle Absorption Chiller Systems |
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