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JPS6261856B2 - - Google Patents
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JPS6261856B2 - - Google Patents

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Publication number
JPS6261856B2
JPS6261856B2 JP20596081A JP20596081A JPS6261856B2 JP S6261856 B2 JPS6261856 B2 JP S6261856B2 JP 20596081 A JP20596081 A JP 20596081A JP 20596081 A JP20596081 A JP 20596081A JP S6261856 B2 JPS6261856 B2 JP S6261856B2
Authority
JP
Japan
Prior art keywords
refrigerant
heat exchanger
evaporator
pipe
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
Application number
JP20596081A
Other languages
Japanese (ja)
Other versions
JPS58106371A (en
Inventor
Yukio Yoshiokaya
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.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric 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 Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP20596081A priority Critical patent/JPS58106371A/en
Publication of JPS58106371A publication Critical patent/JPS58106371A/en
Publication of JPS6261856B2 publication Critical patent/JPS6261856B2/ja
Granted legal-status Critical Current

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  • Devices That Are Associated With Refrigeration Equipment (AREA)
  • Motor Or Generator Cooling System (AREA)

Description

【発明の詳細な説明】 本発明は冷却装置の排気方法の改良に関し、特
に短時間に冷媒回路内の排気を行なうと共に、冷
媒漏洩危険箇所の減少を計つたものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in a method for exhausting a cooling device, and is particularly aimed at evacuating a refrigerant circuit in a short time and reducing the number of locations at risk of refrigerant leakage.

従来此種冷却装置の排気方法は、特公昭45−
40392号公報に記載された如く、冷媒回路内の排
気を行なうのに、圧縮機に設けたサービスパイプ
と乾燥器の入口側に設けたサービス管との間に排
気管を接続しこの排気管を介して排気ポンプにて
行なう方法や、圧縮機のサービスパイプに排気ポ
ンプを接続し、冷媒回路中に窒素ガスを封入し空
気と置換した後排気する方法等があるが、前者で
は溶接箇所が多く、使用中に溶接劣化などにより
冷媒漏洩可能箇所が増え保守点検などの作業増加
と構造の複雑化を伴ない好ましくなく、後者では
排気作業が煩雑であつた。しかも両者共キヤピラ
リーチユーブを経て排気するため、このキヤピラ
リーチユーブが抵抗となり排気ポンプによる排気
が長時間となると共に、加工金属粉などの塵埃等
もキヤピラリーチユーブに詰りやすかつた。
Conventionally, the exhaust method for this type of cooling device was
As described in Publication No. 40392, in order to exhaust the inside of the refrigerant circuit, an exhaust pipe is connected between the service pipe installed on the compressor and the service pipe installed on the inlet side of the dryer. There are two methods: one is to connect an exhaust pump to the service pipe of the compressor, fill nitrogen gas in the refrigerant circuit, replace it with air, and then exhaust the air. During use, the number of locations where refrigerant can leak increases due to welding deterioration, etc., which increases maintenance and inspection work and complicates the structure, which is undesirable, and in the latter case, exhaust work is complicated. Moreover, since both of them are exhausted through a capillary reach tube, this capillary reach tube acts as a resistance, making it take a long time to exhaust the air by the exhaust pump, and the capillary reach tube is easily clogged with dust such as processed metal powder.

本発明は係る点に鑑みて成されたもので、冷媒
回路に高温冷媒を蒸発器に直接流通する側路管を
設け、この側路管の流通を制御する電磁弁を、圧
縮機運転用の電源スイツチより前段に結線し、冷
媒回路の排気運転時前記電磁弁を付勢開枚すると
共に、圧縮機のサービスパイプより排気ポンプに
て排気する排気方法があり、係る方法によつて毛
細管が抵抗となることは少なく、且つ配管も簡素
化されると共に、特別の付加構成は殆んどなく構
造も簡単となり安価であるなどの作用効果を奏す
るものであり、特に本実施例の如く複数種の冷媒
ガスを使用するものに於ては一層効果的である。
The present invention has been made in view of the above-mentioned points, and is provided with a side pipe in the refrigerant circuit that directly flows high-temperature refrigerant to the evaporator, and a solenoid valve for controlling the flow of the side pipe for controlling the flow of the compressor. There is an exhaust method in which the solenoid valve is energized to open when the refrigerant circuit is exhausted, and an exhaust pump is used to exhaust the air from the service pipe of the compressor.This method reduces the capillary resistance. In addition, the piping is simplified, and there are few special additional configurations, the structure is simple, and the cost is low. It is even more effective when using refrigerant gas.

以下本発明方法に於ける実施例を図について説
明する。
Embodiments of the method of the present invention will be described below with reference to the drawings.

1は理科学実験用等任意の用途に供する冷却装
置本体で、外装体2内に設置した冷却槽3等の被
冷却体を具備し且つこの冷却槽3を冷却するため
の冷媒サイクル4を具備している。この冷媒サイ
クル4は冷媒圧縮機5、凝縮器6、第1気液分離
器7、第1熱交換器8、第2気液分離器9、第2
熱交換器10、過冷却器11、キヤピラリーチユ
ーブ12、及び蒸発器13等を順次接続して構成
し、且つ蒸発温度の異る複数種類(例えば冷媒R
−21とR−13BとR−14など)の冷媒を混合封入
している。前記第1気液分離器7は中空筒状の外
筒側部に、前記凝縮器6よりの冷媒管14を貫通
して臨ませ、上部に連通して第1熱交換器8へ至
る冷媒管15を連結し、下部にドライヤー16等
を介してキヤピラリーチユーブ17に連通する導
管18を連通連結している。前記第2気液分離器
9は側部に、前記第1熱交換器8に一端を連結し
た吐出管19の他端を貫通して臨ませ、且つ上部
に連通して第2熱交換器10へ至る冷媒管20を
連結し、下部にドライヤ21等を介してキヤピラ
リーチユーブ22に連通する導管23を連通連結
している。前記第2熱交換器10よりの吐出管2
4は過冷却器11に連通連結している。前記蒸発
器13より冷媒圧縮機5に至る吸込管25は、途
中に連通して形成した前記熱交換器10,8部分
にて蛇行状に屈曲したり交熱フインを設けるなど
によつてこれら熱交換器10,8と夫々連通熱交
換関係に配設し、且つ第1熱交換器8より蒸発器
13側位置適所に前記キヤピラリーチユーブ17
を、第2熱交換器10より蒸発器13側位置適所
に前記キヤピラリーチユーブ22を、夫々連通連
結している。
Reference numeral 1 denotes a cooling device body used for any purpose such as science and science experiments, and is equipped with objects to be cooled such as a cooling tank 3 installed in an exterior body 2, and a refrigerant cycle 4 for cooling this cooling tank 3. are doing. This refrigerant cycle 4 includes a refrigerant compressor 5, a condenser 6, a first gas-liquid separator 7, a first heat exchanger 8, a second gas-liquid separator 9, a second
It is configured by sequentially connecting a heat exchanger 10, a subcooler 11, a capillary reach tube 12, an evaporator 13, etc., and it is configured by connecting a heat exchanger 10, a supercooler 11, a capillary reach tube 12, an evaporator 13, etc.
-21, R-13B, R-14, etc.) are mixed and sealed. The first gas-liquid separator 7 has a refrigerant pipe 14 from the condenser 6 passed through the side of the hollow cylindrical outer cylinder, and is connected to the upper part of the refrigerant pipe leading to the first heat exchanger 8. 15 are connected to each other, and a conduit 18 communicating with a capillary reach tube 17 via a dryer 16 or the like is connected to the lower part thereof. The second gas-liquid separator 9 has its side facing through the other end of a discharge pipe 19 whose one end is connected to the first heat exchanger 8, and communicates with the upper part thereof to the second heat exchanger 10. A refrigerant pipe 20 is connected to the refrigerant pipe 20, and a conduit 23 communicating with a capillary reach tube 22 is connected to the lower part via a dryer 21 and the like. Discharge pipe 2 from the second heat exchanger 10
4 is connected to the supercooler 11. The suction pipe 25 leading from the evaporator 13 to the refrigerant compressor 5 is bent in a meandering manner at the heat exchanger 10, 8 portion formed in communication with the evaporator 13, or is provided with heat exchanger fins to absorb the heat. The capillary reach tube 17 is disposed in a communicating heat exchange relationship with the exchangers 10 and 8, respectively, and is located at an appropriate position on the side of the evaporator 13 from the first heat exchanger 8.
and the capillary reach tube 22 are connected to each other at appropriate positions closer to the evaporator 13 than the second heat exchanger 10.

前記凝縮器6の出口と蒸発器13の入口間と
を、電磁弁26にて流通制御される側路管27に
て連通せしめ、前記電磁弁26を付勢開放するこ
とにより、冷媒圧縮機5よりの加圧高温冷媒を、
凝縮器6を経た後、蒸発器13へ直接供給し、こ
の蒸発器13を加熱して前記本体1の冷却槽3に
付着した霜氷を加熱溶融する。前記冷媒圧縮機5
は密閉容器内に開口し、冷却装置1完成後に圧潰
するなどにより閉塞するサービスパイプ28を設
けている。
The outlet of the condenser 6 and the inlet of the evaporator 13 are communicated through a bypass pipe 27 whose flow is controlled by a solenoid valve 26, and the refrigerant compressor 5 is opened by energizing and opening the solenoid valve 26. More pressurized high temperature refrigerant,
After passing through the condenser 6, it is directly supplied to the evaporator 13, and the evaporator 13 is heated to heat and melt the frost and ice attached to the cooling tank 3 of the main body 1. The refrigerant compressor 5
A service pipe 28 is provided which opens into the airtight container and is closed by crushing or the like after the cooling device 1 is completed.

そして係る冷媒サイクル4の動作は、冷媒圧縮
機5にて圧縮された複数種(実施例では3種類)
の混合冷媒が、凝縮器6にて放熱され蒸発温度の
高い冷媒が液化し、未だガス状の他の冷媒と共に
冷媒管14より第1気液分離器7内へ流入する。
第1気液分離器7内へ噴出した気液混合冷媒は、
気液を分離されて、凝縮器6にて液化されなかつ
た蒸発温度の低いガス状冷媒(実施例ではR−
13BとR−14の二種類の混合ガス冷媒)が冷媒管
15を介して第1熱交換器8へ流通する。一方御
1気液分離器7内底部に滴下した液状冷媒は、導
管18よりドライヤ16を通つて除湿され、キヤ
ピラリーチユーブ17にて減圧されて第1熱交換
器8と交熱関係の吸込管25にて蒸発気化し第1
熱交換器8を冷却する。これによつて第1気液分
離器7を通過し第1熱交換器8に流入した混合冷
媒ガスのうち蒸発温度の高い冷媒ガスが凝縮液化
する。そして第1熱交換器8より、気液混合冷媒
が第2気液分離器9に流入し、第1気液分離器7
と同様この第2気液分離器9にて蒸発温度の低い
ガス状冷媒(例えばR−14)と第1熱交換器8に
て液化した液状冷媒(例えばR−13B)とに分離
し、ガス状冷媒は第2熱交換器10へ、液状冷媒
は導管23よりドライヤ21を経て除湿されキヤ
ピラリーチユーブ22にて減圧されて第2熱交換
器10と交熱関係の吸込管25にて蒸発気化し第
2熱交換器10を冷却する。この時凝縮器6にて
液化する冷媒より第1熱交換器8で液化する冷媒
が蒸発温度が低いため、第2熱交換器10に第2
気液分離器9より分離されて供給されるガス状冷
媒は第2熱交換器10にて第1熱交換器8よりも
低温度に冷却されて凝縮液化され吐出管24より
過冷却器11に流通し、この過冷却器11の中空
筒体を貫通した蒸発器13より冷媒圧縮機5へ帰
還する吸込管25を流通する低温度(例えば−20
℃〜−80℃前後)の帰還冷媒にて過冷却される。
この過冷却器11の中空筒体内に第2熱交換器1
0を経て流入した、蒸発温度の最も低い冷媒(実
施例では冷媒R−14)は、第2熱交換器10で冷
却液化しきれないでガス状冷媒を含んだ気液混合
冷媒であるが、ガス状冷媒は中空筒体内上部に浮
遊滞溜し、液状冷媒が中空筒体内に露出している
吸込管25の交熱部にて過冷却され、吐出口より
冷媒管29及びキヤピラリーチユーブ12を介し
て蒸発器13へ供給される。一方中空筒体内上部
に浮遊しているガス状冷媒は、蒸発器13より流
出した直後の低温冷媒を流通する吸込管25の交
熱部に接触しているため、冷却されて交熱部外表
面等に凝縮結露し、上下方向に延びた交熱部等を
伝つて流下し、或いは直接滴下して、中空筒体内
底部に溜つた液状冷媒に合流して吐出口より流出
する。この過冷却器11を経てキヤピラリーチユ
ーブ12に至る最も蒸発温度が低い冷媒にて、蒸
発器13を蒸発冷却し、この蒸発器13を冷却槽
3外周に捲回装着したり、冷却槽3内に投入した
りして利用する。実験のものでは前記3種類の冷
媒R−21、R−13B、R−14を使用して冷却槽3
を−80℃〜−90℃の冷却温度が得られた。
The operation of the refrigerant cycle 4 includes a plurality of types (three types in the embodiment) of the refrigerant compressed by the refrigerant compressor 5.
The mixed refrigerant radiates heat in the condenser 6, and the refrigerant having a high evaporation temperature liquefies, and flows into the first gas-liquid separator 7 through the refrigerant pipe 14 together with other refrigerants that are still gaseous.
The gas-liquid mixed refrigerant spouted into the first gas-liquid separator 7,
Gaseous refrigerant with a low evaporation temperature (R-
Two types of mixed gas refrigerants (13B and R-14) flow through the refrigerant pipe 15 to the first heat exchanger 8. On the other hand, the liquid refrigerant dripped into the inner bottom of the control first gas-liquid separator 7 is dehumidified through the conduit 18 and the dryer 16, and is depressurized in the capillary reach tube 17 and connected to the first heat exchanger 8 through a suction pipe connected to heat exchange. At 25, the first
Cool the heat exchanger 8. As a result, the refrigerant gas having a high evaporation temperature among the mixed refrigerant gases that have passed through the first gas-liquid separator 7 and flowed into the first heat exchanger 8 is condensed and liquefied. Then, the gas-liquid mixed refrigerant flows from the first heat exchanger 8 into the second gas-liquid separator 9, and the gas-liquid mixture refrigerant flows into the first gas-liquid separator 7.
Similarly, the second gas-liquid separator 9 separates the gaseous refrigerant with a low evaporation temperature (e.g. R-14) and the liquid refrigerant liquefied in the first heat exchanger 8 (e.g. R-13B), and the gas The liquid refrigerant is sent to the second heat exchanger 10, and the liquid refrigerant is dehumidified through the conduit 23 through the dryer 21, depressurized in the capillary reach tube 22, and evaporated in the suction pipe 25 connected to the second heat exchanger 10. to cool down the second heat exchanger 10. At this time, since the refrigerant that liquefies in the first heat exchanger 8 has a lower evaporation temperature than the refrigerant that liquefies in the condenser 6, the second heat exchanger 10
The gaseous refrigerant separated and supplied from the gas-liquid separator 9 is cooled to a lower temperature than the first heat exchanger 8 in the second heat exchanger 10, condensed and liquefied, and sent to the supercooler 11 through the discharge pipe 24. The low temperature (for example -20
It is supercooled with the return refrigerant at a temperature of around -80℃.
A second heat exchanger 1 is installed inside the hollow cylinder of this supercooler 11.
The refrigerant with the lowest evaporation temperature (refrigerant R-14 in the example), which has flown in through the second heat exchanger 10, is a gas-liquid mixed refrigerant that contains gaseous refrigerant and cannot be completely liquefied by cooling in the second heat exchanger 10. The gaseous refrigerant floats and accumulates in the upper part of the hollow cylinder, and the liquid refrigerant is supercooled in the heat exchanger part of the suction pipe 25 exposed inside the hollow cylinder, and then flows through the refrigerant pipe 29 and capillary reach tube 12 from the discharge port. It is supplied to the evaporator 13 via the evaporator 13. On the other hand, since the gaseous refrigerant floating in the upper part of the hollow cylinder is in contact with the heat exchanger part of the suction pipe 25 through which the low-temperature refrigerant flows immediately after flowing out from the evaporator 13, it is cooled and the outer surface of the heat exchanger part is cooled. The refrigerant condenses, flows down along the vertically extending heat exchanger, or drops directly, joins the liquid refrigerant accumulated at the bottom of the hollow cylinder, and flows out from the discharge port. The evaporator 13 is evaporatively cooled using the refrigerant with the lowest evaporation temperature that passes through the supercooler 11 and reaches the capillary reach tube 12. Use it by putting it in. In the experiment, the three types of refrigerants R-21, R-13B, and R-14 were used in the cooling tank 3.
A cooling temperature of -80℃ to -90℃ was obtained.

尚、前記実施例では3種類の冷媒を利用したも
のについて記述したが、2種類であつても、4種
類以上であつても差しつかえない。この時には冷
媒の種類に応じて気液分離器及び熱交換器の数量
が増減する。又、側路管27は凝縮器6の後段で
はなく、冷媒圧縮機5の後段で凝縮器6の前段に
て蒸発器13に高温冷媒を供給する如く配管して
も良い。
In the above embodiments, three types of refrigerants were used, but two or four or more types may be used. At this time, the number of gas-liquid separators and heat exchangers increases or decreases depending on the type of refrigerant. Further, the bypass pipe 27 may be arranged not after the condenser 6 but after the refrigerant compressor 5 and before the condenser 6 to supply high-temperature refrigerant to the evaporator 13.

前記本体1の冷却槽3は、生物学物質A等を収
納する収納容器30に一端を連通した、管体にて
形成した中空路31の他端を臨ませると共に、真
空ポンプ32の吸込管33を臨ませており、前記
収納容器30内の空気を、この冷却槽3内を介し
て真空ポンプ32にて吸引し、収納容器30内を
真空状態にして予備凍結された生物学物質A等を
所謂凍結乾燥する。この時冷却槽3内を通過する
収納容器30よりの空気中に含まれた湿気は、−
80℃〜−90℃等極低温に冷却された冷却槽3内周
壁に凍結し、殆んど除湿された空気が真空ポンプ
32へ引かれ、排気筒34より大気中へ排出され
る。
The cooling tank 3 of the main body 1 faces the other end of a hollow passage 31 formed of a tubular body, one end of which communicates with a storage container 30 for storing biological substances A, etc., and a suction pipe 33 of a vacuum pump 32. The air inside the storage container 30 is sucked through the cooling tank 3 by the vacuum pump 32, and the inside of the storage container 30 is evacuated to remove the pre-frozen biological substances A, etc. So-called freeze-drying. At this time, the moisture contained in the air from the storage container 30 passing through the cooling tank 3 is -
Air that is frozen on the inner peripheral wall of the cooling tank 3 cooled to an extremely low temperature such as 80° C. to -90° C. and is almost dehumidified is drawn to the vacuum pump 32 and discharged into the atmosphere from the exhaust pipe 34.

次に前述の如き構成における制御を行う、第3
図に示した電気回路について説明する。
Next, the third
The electric circuit shown in the figure will be explained.

真空ポンプ32は電源端子35に、電源スイツ
チ36を介して、凝縮器6を強制通風する送風機
37、電磁弁26及び冷媒圧縮機5等と共に接続
している。前記電磁弁26は直列に手動或いはタ
イマなど自動的に開閉するホツトガススイツチ3
8を介して前記電源スイツチ36より前段にて電
源端子35に接続すると共に、リレーコイル39
を並列に接続している。40は切替開閉器41制
御用のリレーコイルで、前記冷却槽3の温度等を
感知して開閉する温度開閉器42を介して電源端
子35に接続されている。前記冷媒圧縮機5は第
1接点a、第2接点b及び切替片cよりなる前記
切替開閉器41の切替片cに接続し、リレーコイ
ル40の付勢時には切替片cを介して第1接点a
に、消勢時には切替片cを介して第2接点bに接
続される。43は前記リレーコイル39にて開閉
制御される常閉スイツチで、一端を前記電源スイ
ツチ36と温度開閉器42間に接続し、他端を切
替開閉器41の第2接点bに接続している。44
は冷媒圧縮機5の過負荷開閉器である。
The vacuum pump 32 is connected to a power terminal 35 via a power switch 36 along with a blower 37 for forcing air through the condenser 6, a solenoid valve 26, a refrigerant compressor 5, and the like. The solenoid valve 26 is connected in series to a hot gas switch 3 that opens and closes manually or automatically, such as with a timer.
8 to the power terminal 35 at a stage earlier than the power switch 36, and the relay coil 39
are connected in parallel. Reference numeral 40 denotes a relay coil for controlling the switching switch 41, which is connected to the power supply terminal 35 via a temperature switch 42 that opens and closes by sensing the temperature of the cooling tank 3 and the like. The refrigerant compressor 5 is connected to the switching piece c of the switching switch 41, which is composed of a first contact a, a second contact b, and a switching piece c, and when the relay coil 40 is energized, the first contact is connected to the switching piece c through the switching piece c. a
When the power is de-energized, it is connected to the second contact b via the switching piece c. 43 is a normally closed switch whose opening and closing are controlled by the relay coil 39, one end of which is connected between the power switch 36 and the temperature switch 42, and the other end of which is connected to the second contact b of the switching switch 41. . 44
is an overload switch for the refrigerant compressor 5.

前述の如く構成によつて、冷媒サイクル4中の
排気を行うのは、冷媒圧縮機5のサービスパイプ
28に排気ポンプ45を連結し、且つ本体1の電
源端子35を電源に接続すると共に、ホツトガス
スイツチ38を強制閉路する。これによつて電磁
弁26が開放し側路管27を連通するので、排気
ポンプ45を作動すれば、キヤピラリーチユーブ
12を経ずに側路管27等大きな管径の管体を介
して冷媒圧縮機5に冷媒サイクル4中の空気が吸
引され、サービスパイプ28を介して排気ポンプ
45にて排気される。キヤピラリーチユーブ12
や17,22中及びその近傍の空気も、蒸発器1
3や凝縮器6より冷媒圧縮機5に至る大きな管径
の管体を流通する吸気中に吸引合流されて排気ポ
ンプ45により排気され、その量は冷媒サイクル
4中の空気全体に対しては少量であり、排気時間
の延長には殆んど関係しない。排気完了後冷媒ガ
スを封入し、サービスパイプ28を圧潰などによ
り閉塞すれば完成する。
With the above-mentioned configuration, the refrigerant cycle 4 is exhausted by connecting the exhaust pump 45 to the service pipe 28 of the refrigerant compressor 5, connecting the power terminal 35 of the main body 1 to the power source, and connecting the hot The gas switch 38 is forcibly closed. This opens the solenoid valve 26 and communicates with the side pipe 27, so when the exhaust pump 45 is operated, the refrigerant flows through a pipe body with a large diameter such as the side pipe 27 without passing through the capillary reach tube 12. Air in the refrigerant cycle 4 is sucked into the compressor 5 and exhausted by the exhaust pump 45 via the service pipe 28. Capillary reach tube 12
The air in and near the evaporator 1 and 17 and 22 is also
3 and the condenser 6 to the refrigerant compressor 5, and are sucked into the intake air flowing through the pipe body with a large diameter, and are exhausted by the exhaust pump 45, and the amount thereof is small compared to the total air in the refrigerant cycle 4. , and has little to do with evacuation time extension. After the exhaust is completed, refrigerant gas is filled in and the service pipe 28 is closed by crushing or the like to complete the process.

その後の冷却装置1の運転は、冷却槽3を蒸発
器13によつて冷却する場合、電源スイツチ36
を投入すると、35−36−43−b−c−5−
44−35の閉回路が形成され冷媒圧縮機5が運
転されて蒸発器13による冷却が開始され、所定
温度以下(例えば2℃程度)になると温度開閉器
42が閉路し、リレーコイル40を付勢して切替
片cを第2接点bより第1接点aに切替えて冷媒
圧縮機5の運転を継続し、冷却槽3を−80℃〜−
90℃等の極低温迄冷却する。その後収納容器30
よりの中空路31を冷却槽3内に臨ませると、運
転中の真空ポンプ32により、収納容器30内の
空気が冷却槽3を介して吸引排気され、収納容器
30内の凍結した生物学物質A等を昇華乾燥す
る。
The subsequent operation of the cooling device 1 is performed by switching the power switch 36 when the cooling tank 3 is cooled by the evaporator 13.
When inputting, 35-36-43-b-c-5-
A closed circuit 44-35 is formed, the refrigerant compressor 5 is operated, and cooling by the evaporator 13 is started. When the temperature falls below a predetermined temperature (for example, about 2°C), the temperature switch 42 closes and the relay coil 40 is attached. The switching piece c is switched from the second contact b to the first contact a to continue operating the refrigerant compressor 5, and the cooling tank 3 is heated from -80°C to -
Cool to an extremely low temperature such as 90℃. Then storage container 30
When the hollow passage 31 faces the inside of the cooling tank 3, the air inside the storage container 30 is sucked and exhausted through the cooling tank 3 by the vacuum pump 32 in operation, and the frozen biological substances inside the storage container 30 are removed. Dry A etc. by sublimation.

所定時間運転後冷却槽3内周壁に多量の湿気が
付着凍結するため、自動的に或いは目視などによ
り確認して手動にてホツトガススイツチ38を閉
路すると、電磁弁26が開路して冷媒圧縮機5よ
りの冷媒が、凝縮器6を経た後直接蒸発器13に
流通し、加熱して冷却槽3周壁に付着した霜氷を
溶融する。霜氷の溶融が進み、冷却槽3内が所定
温度例えば約10℃迄上昇すると温度開閉器42が
開路し、リレーコイル40が消勢され切替開閉器
41の切替片cを第1接点aより第2接点bに切
替復帰する。これと同時に電磁弁26と並列のリ
レーコイル39がホツトガススイツチ38の閉路
により付勢されたまゝであり、常閉スイツチ43
が開路を継続しており、冷媒圧縮機5は停止し、
冷媒サイクル4の冷媒流通を停止する。従つて冷
却槽3内周壁の残溜霜氷は、室温にて徐々に溶融
される。冷却槽3内周壁の霜氷が完全に溶融除去
されると、目視により或いは自動的にホツトガス
スイツチ38を開路し、電磁弁26を閉路すると
共にリレーコイル39を消勢すると、常閉スイツ
チ43が閉路し、再び冷媒圧縮機5を運転して冷
却槽3の冷却を再開する。
After a predetermined period of operation, a large amount of moisture adheres to the inner peripheral wall of the cooling tank 3 and freezes, so when the hot gas switch 38 is closed automatically or manually after checking visually, the solenoid valve 26 is opened and the refrigerant compressor is closed. After passing through the condenser 6, the refrigerant from No. 5 flows directly into the evaporator 13, where it is heated and melts the frost and ice attached to the peripheral wall of the cooling tank 3. When the melting of the frost and ice progresses and the temperature inside the cooling tank 3 rises to a predetermined temperature, for example, about 10°C, the temperature switch 42 opens, the relay coil 40 is deenergized, and the switching piece c of the switching switch 41 is switched from the first contact a. Switching back to the second contact b. At the same time, the relay coil 39 in parallel with the solenoid valve 26 remains energized due to the closing of the hot gas switch 38, and the normally closed switch 43 remains energized.
continues to open, the refrigerant compressor 5 stops,
Refrigerant flow in the refrigerant cycle 4 is stopped. Therefore, the residual frost on the inner circumferential wall of the cooling tank 3 is gradually melted at room temperature. When the frost and ice on the inner circumferential wall of the cooling tank 3 are completely melted and removed, the hot gas switch 38 is opened visually or automatically, and the solenoid valve 26 is closed and the relay coil 39 is deenergized. is closed, and the refrigerant compressor 5 is operated again to resume cooling of the cooling tank 3.

この冷媒圧縮機5の停止中に、側路管27を介
して冷媒サイクル4の高低圧調整が出来、再起動
時に冷媒圧縮機5に過負荷が加わりバルブ折損や
モータ焼損などの損傷が回避される。前記真空ポ
ンプ32は、制御スイツチ46を直列接続して任
意に運転制御するのが望ましい。
While the refrigerant compressor 5 is stopped, the high and low pressures of the refrigerant cycle 4 can be adjusted via the side pipe 27, and damage such as valve breakage and motor burnout due to overload on the refrigerant compressor 5 when restarted can be avoided. Ru. Preferably, the vacuum pump 32 is connected in series with a control switch 46 to arbitrarily control its operation.

本発明は以上の如き方法にて冷媒サイクル中の
排気を行うため、冷媒圧縮機のサービスパイプを
利用して排気出来、構成が簡単且つ冷媒漏洩危険
箇所の増加を伴なうこともない。しかもキヤピラ
リーチユーブを殆んど介さず管径の大なる管体を
介して冷媒サイクル中の殆んどの排気が出来、排
気時間の短縮化が計れ且つキヤピラリーチユーブ
に金属粉などの塵埃等が詰る恐れも著しく減少す
る。又、係る動作も蒸発器のホツトガス加熱用に
設けた側路管の電磁弁を開放することによつて行
なえ、特別の付加構成を殆んど要さず構造の簡略
化が計れ、且つ取扱いも容易となる。しかも冷却
装置完成後には何らの支障もない。
Since the present invention performs exhaust in the refrigerant cycle using the method described above, the service pipe of the refrigerant compressor can be used for exhaust, the structure is simple, and the number of locations at risk of refrigerant leakage does not increase. Moreover, most of the exhaust during the refrigerant cycle can be done through the large-diameter pipe body without using the capillary reach tube, which shortens the exhaust time and prevents dust such as metal powder from entering the capillary reach tube. The risk of clogging is also significantly reduced. In addition, this operation can be performed by opening the solenoid valve of the side pipe provided for heating the hot gas of the evaporator, which simplifies the structure with almost no special additional configuration required, and is easy to handle. It becomes easier. Furthermore, there will be no problems after the cooling system is completed.

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

第1図は本発明方法により完成した冷却装置の
斜視図、第2図は同概略冷媒サイクル図、第3図
は同じく概略電気回路図、第4図は同使用例を示
す一部切欠断面せる概略構成図である。 5……冷媒圧縮機、26……電磁弁、27……
側路管、28……サービスパイプ、45……排気
ポンプ。
Fig. 1 is a perspective view of a cooling device completed by the method of the present invention, Fig. 2 is a schematic diagram of the refrigerant cycle, Fig. 3 is a schematic electrical circuit diagram, and Fig. 4 is a partially cutaway cross-section showing an example of its use. It is a schematic block diagram. 5... Refrigerant compressor, 26... Solenoid valve, 27...
Side pipe, 28...service pipe, 45...exhaust pump.

Claims (1)

【特許請求の範囲】[Claims] 1 冷媒圧縮機、凝縮器、キヤピラリーチユー
ブ、及び蒸発器等よりなる冷媒サイクルに、高温
冷媒を蒸発器に直接供給する電磁弁にて連通制御
される側路管を設け、この電磁弁を前記冷媒圧縮
機用の電源スイツチより前段に結線し、且つ前記
冷媒圧縮機の密閉容器内に連通して設けたサービ
スパイプに排気ポンプを連結すると共に、前記電
磁弁に通電付勢して開放し側路管を連通せしめ、
前記排気ポンプを運転して冷媒サイクル中の空気
の排出を行う冷却装置の排気方法。
1 A refrigerant cycle consisting of a refrigerant compressor, a condenser, a capillary reach tube, an evaporator, etc. is provided with a side pipe whose communication is controlled by a solenoid valve that directly supplies high-temperature refrigerant to the evaporator, and this solenoid valve is connected to the An exhaust pump is connected to a service pipe connected upstream of a power switch for the refrigerant compressor and communicated with the airtight container of the refrigerant compressor, and the electromagnetic valve is energized and opened. Connect the pipes,
A method for exhausting a cooling device, which operates the exhaust pump to exhaust air from a refrigerant cycle.
JP20596081A 1981-12-18 1981-12-18 Method of exhausting cooling device Granted JPS58106371A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20596081A JPS58106371A (en) 1981-12-18 1981-12-18 Method of exhausting cooling device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20596081A JPS58106371A (en) 1981-12-18 1981-12-18 Method of exhausting cooling device

Publications (2)

Publication Number Publication Date
JPS58106371A JPS58106371A (en) 1983-06-24
JPS6261856B2 true JPS6261856B2 (en) 1987-12-23

Family

ID=16515549

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20596081A Granted JPS58106371A (en) 1981-12-18 1981-12-18 Method of exhausting cooling device

Country Status (1)

Country Link
JP (1) JPS58106371A (en)

Also Published As

Publication number Publication date
JPS58106371A (en) 1983-06-24

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