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JP5366617B2 - Moisture removal apparatus and moisture removal method - Google Patents
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JP5366617B2 - Moisture removal apparatus and moisture removal method - Google Patents

Moisture removal apparatus and moisture removal method Download PDF

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JP5366617B2
JP5366617B2 JP2009092092A JP2009092092A JP5366617B2 JP 5366617 B2 JP5366617 B2 JP 5366617B2 JP 2009092092 A JP2009092092 A JP 2009092092A JP 2009092092 A JP2009092092 A JP 2009092092A JP 5366617 B2 JP5366617 B2 JP 5366617B2
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moisture
flow path
tank
temperature fluid
low
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JP2010243061A (en
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昇 坂本
清志 勝
信二 村田
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Mitsubishi Electric Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a device and a method for effectively removing moisture from coolant containing the moisture. <P>SOLUTION: An antifreeze liquid circulating device 7 is operated to cool antifreeze liquid housed in the device 7 to around -10&deg;C, for example. The antifreeze liquid is circulated between a tank 6 and the antifreeze liquid circulating device 7 through a conduit 8 and a conduit 10. After temperature of the antifreeze liquid in the tank 6 is stabilized to desired low temperature, a processed medium flows out from a conduit 4 to outside C via a conduit 1 and a coiling conduit part 3. When the processed medium passes through the coiling conduit part 3, moisture contained in the medium is effectively exposed, freezed, and separated on an inner wall surface of the coiling conduit part 3. In this way, the processed medium from which the moisture is removed flows out from the conduit 4 to the outside C and retrieved by a medium recovery device (not shown in the figure), for example. <P>COPYRIGHT: (C)2011,JPO&amp;INPIT

Description

本発明は、水分除去装置および水分除去方法に関し、特に水分を含む冷媒から水分を除去するのに好適な水分除去装置および水分除去方法に関するものである。   The present invention relates to a moisture removing apparatus and a moisture removing method, and more particularly to a moisture removing apparatus and a moisture removing method suitable for removing moisture from a refrigerant containing moisture.

故障や使用済みなどの理由から、冷蔵庫、ショーケース、空気調和機などの冷凍空調機器が具備する冷媒回路から冷凍機油を回収する際に、回収した冷凍機油にはクロロフルオロカ−ボンなどのフルオロカ−ボン類からなる冷媒が溶存しており、それを放置すると当該冷媒が大気中に蒸散して環境に悪影響を及ぼす問題がある。また、それら冷媒類は焼却処理される際に、加熱分解して塩酸およびフッ酸などの有害物の生成を伴うので、これら生成物を無害化するなどの複雑な処理を必須とするなどの課題があった。   When recovering refrigerating machine oil from the refrigerant circuit provided in refrigerating and air-conditioning equipment such as refrigerators, showcases, air conditioners, etc. for reasons such as failure or use, the recovered refrigerating machine oil contains fluorocarbons such as chlorofluorocarbons. -The refrigerant | coolant which consists of Bonn has melt | dissolved, and when it is left, the said refrigerant | coolant will evaporate in air | atmosphere and there exists a problem which has a bad influence on an environment. In addition, when these refrigerants are incinerated, they are decomposed by heating and generate harmful substances such as hydrochloric acid and hydrofluoric acid, so that complicated processing such as detoxification of these products is essential. was there.

この為、回収冷凍機油からフロンを主体とした冷媒を除去する方法が提案されており、例えば回収冷凍機油を加温によって冷媒を蒸発・分離する方法が下記の特許文献1に提案されている。また、超音波による加振によって上層部分と下層部分とを混合し、冷媒の含有濃度の低下を抑制することによって蒸発速度の低下を防止する方法が下記の特許文献2に提案されている。さらに、真空中で冷凍機油の水分を沸騰させて油と水分および冷媒を分離し回収する方法が下記の特許文献3に提案されている。また回収した冷媒には多くの場合、水分が含まれているので当該水分の除去方法として、密閉容器中で冷媒をペルチェ効果を利用して氷点以下に冷却された放熱板に接触させながら、徐々に冷媒中の水分を凍結させて除去する方法が下記の特許文献4に提案されている。また、水分保持部材中に冷媒を通過させることにより冷媒中の水分を除去する方法が下記の特許文献5に提案されている。   For this reason, a method for removing the refrigerant mainly composed of Freon from the recovered refrigeration oil has been proposed. For example, a method for evaporating and separating the refrigerant by heating the recovered refrigeration oil is proposed in Patent Document 1 below. Further, Patent Document 2 below proposes a method of preventing a decrease in evaporation rate by mixing an upper layer portion and a lower layer portion by excitation with ultrasonic waves and suppressing a decrease in the concentration of refrigerant. Further, a method for separating and recovering oil, moisture and refrigerant by boiling the moisture of the refrigerating machine oil in a vacuum is proposed in Patent Document 3 below. In many cases, the recovered refrigerant contains water. As a method of removing the water, the refrigerant is gradually brought into contact with a heat sink cooled to below the freezing point using the Peltier effect in a sealed container. A method for freezing and removing moisture in the refrigerant is proposed in Patent Document 4 below. Further, Patent Document 5 below proposes a method of removing moisture in the refrigerant by allowing the refrigerant to pass through the moisture holding member.

ところで、特許文献4のペルチェ効果を利用した方法では、水分の凍結除去の能率が悪いので、そのために同文献の段落番号0030に記載されているように凍結除去に数日放置する長時間を要する大きな問題がある。   By the way, in the method using the Peltier effect of Patent Document 4, the efficiency of water freezing and removal is poor, and as a result, as described in paragraph No. 0030 of the same document, it takes a long time to leave for several days. There is a big problem.

特開2007−24337号公報JP 2007-24337 A 特開2000−130894号公報JP 2000-130894 A 特開2005−201562号公報JP 2005-201562 A 特許第3554428号公報Japanese Patent No. 3555428 特開平6−201231号公報JP-A-6-201231

ところで、上記のようにして採集された冷媒は、フロン回収装置などを用いて液相化後所定のボンベに収納される。しかし、回収冷凍機油から分離された冷媒中には多くの水分が含まれており、従来の方法では上記したように効率よく水分を除去できずに、そのまま回収すると、フロン回収装置内の圧縮機が絶縁不良を起すなどの問題があった。また従来の方法では、真空状態を保持にするため真空ポンプや冷媒の大気放出を防ぐため密閉容器が必要であった。本発明は、上記のような課題を解決するためになされたもので、冷媒中に含まれる水分を効果的に除去する方法を提供するものである。   By the way, the refrigerant collected as described above is stored in a predetermined cylinder after liquefaction using a Freon recovery device or the like. However, the refrigerant separated from the recovered refrigeration machine oil contains a lot of water, and the conventional method cannot efficiently remove the water as described above. However, there were problems such as causing poor insulation. Moreover, in the conventional method, in order to maintain a vacuum state, a vacuum pump or a sealed container is required to prevent the refrigerant from being released into the atmosphere. The present invention has been made to solve the above problems, and provides a method for effectively removing moisture contained in a refrigerant.

本発明に係る水分除去装置は、良伝熱性金属製であって水分を含む冷媒を流す流路装置、上記流路装置を収容する流路収容槽、上記冷媒は凍結しないが上記水分は上記流路装置の内壁上に氷結する温度に冷却するための低温流体を上記流路収容槽に供給する低温流体供給装置、上記流路収容槽内の低温流体を一時的に収容するバッファタンク、上記低温流体を上記流路収容槽から上記バッファタンクへ、あるいはその逆方向に移送する双方向移送装置、および上記流路装置を加熱して上記内壁上の氷結物を溶融する加熱装置を備えたものである。
本発明に係る水分除去方法は、良伝熱性金属製であって水分を含む冷媒を流す流路装置、上記流路装置を収容する流路収容槽、上記冷媒は凍結しないが上記水分は上記流路装置の内壁上に氷結する温度に冷却するための低温流体を上記流路収容槽に供給する低温流体供給装置、および上記流路装置を加熱して上記内壁上の氷結物を溶融する加熱装置を備えた水分除去装置を用い、水分を含む被処理冷媒を上記流路装置に流す第一工程、上記流路装置を上記冷媒は凍結しないが上記水分は氷結する温度に冷却する第二工程、および上記加熱装置により上記流路装置を加熱して上記氷結物を解凍する第三工程、上記第二工程の後、流路収容槽内の低温流体の略全量を一時的に収容するバッファタンクに移送する第四工程、上記第四工程の後、流路収容槽内に少なくとも20℃の温風または熱風を導入して上記流路装置を加熱して上記氷結物を解凍する第五工程を含むものである。
The moisture removing device according to the present invention is a channel device that is made of a highly heat conductive metal and flows a refrigerant containing moisture, a channel housing tank that houses the channel device, and the refrigerant is not frozen but the moisture is not flowed. A low-temperature fluid supply device for supplying a low-temperature fluid for cooling to a temperature that freezes on the inner wall of the passage device to the flow path storage tank, a buffer tank for temporarily storing the low-temperature fluid in the flow path storage tank, and the low temperature A bi-directional transfer device for transferring fluid from the flow path storage tank to the buffer tank or in the opposite direction; and a heating device for heating the flow path device to melt the frozen matter on the inner wall. is there.
The water removal method according to the present invention includes a flow path device that is made of a highly heat-conductive metal and that flows a refrigerant containing water, a flow path storage tank that houses the flow path device, and the refrigerant does not freeze, but the water flows through the flow path. A low-temperature fluid supply device that supplies a low-temperature fluid for cooling to a temperature that freezes on the inner wall of the passage device to the flow passage storage tank, and a heating device that heats the flow passage device and melts the frozen matter on the inner wall A first step of flowing a refrigerant to be treated to flow into the flow path device, a second step of cooling the flow path device to a temperature at which the refrigerant does not freeze but the water is frozen. And after the third step of thawing the frozen product by heating the flow path device by the heating device and the second step, a buffer tank temporarily storing substantially the entire amount of the low-temperature fluid in the flow path storage tank 4th process to transfer, flow path after the above 4th process By introducing hot air or hot air of at least 20 ° C. in Description tank by heating the flow path unit it is intended to include fifth thawing the frost.

本発明に係る水分除去装置および水分除去方法によれば、冷媒中の水分を短時間でしかも効率的に除去することができ、冷媒を回収するための装置の故障問題が実際上生じないという効果を有する。また本発明の水分除去装置は、密閉容器や水分保持部材、例えばシリカゲルやモリキュラーシーブなどの消耗品を用いないために使用中の劣化もなく、また真空ポンプなども用いない為、簡単な構成で確実に冷媒中の水分を効果的に除去できる。   According to the moisture removing device and the moisture removing method of the present invention, it is possible to efficiently remove moisture in the refrigerant in a short time, and the effect that the failure problem of the device for collecting the refrigerant does not actually occur. Have In addition, the moisture removing device of the present invention has a simple structure because it does not use a sealed container or a moisture retaining member, for example, silica gel or molecular sieve, so that there is no deterioration during use and no vacuum pump is used. Thus, moisture in the refrigerant can be effectively removed with certainty.

実施の形態1を示す図で冷媒中の水分除去装置の構成図である。FIG. 2 is a diagram illustrating the first embodiment and is a configuration diagram of a moisture removing device in refrigerant. 実施の形態2を示す図で冷媒中の水分除去装置の構成図である。It is a figure which shows Embodiment 2, and is a block diagram of the moisture removal apparatus in a refrigerant | coolant.

以下において、互いに同一部分は同一符号を付して、説明を省略することがある。   In the following, the same parts are denoted by the same reference numerals, and the description thereof may be omitted.

実施の形態1.
図1は、本発明の実施の形態1における水分除去装置の構成を示す図である。図1において、当該水分除去装置は、管路1、管路1に設けられた三方弁2、コイル巻き状管路部3、管路4、管路4に設けられた三方弁5、タンク6、不凍液循環装置7、管路8、管路8に設けられた三方弁9、管路10、管路10に設けられた三方弁11、管路12、加温部13、および温度センサ14、から構成されている。これらのうち、コイル巻き状管路部3が本発明における流路装置の一例であり、タンク6〜温度センサ14が本発明における冷却・加熱装置の一例であって、これらのうち、コイル巻き状管路部3は、銅、アルミニウム、あるいはその他の良伝熱性金属にて形成されている。
Embodiment 1 FIG.
FIG. 1 is a diagram showing a configuration of a moisture removing apparatus according to Embodiment 1 of the present invention. In FIG. 1, the moisture removing apparatus includes a pipe 1, a three-way valve 2 provided in the pipe 1, a coiled pipe part 3, a pipe 4, a three-way valve 5 provided in the pipe 4, and a tank 6. , Antifreeze circulating device 7, pipe 8, three-way valve 9 provided in pipe 8, pipe 10, three-way valve 11 provided in pipe 10, pipe 12, heating unit 13, and temperature sensor 14, It is composed of Of these, the coil-wound pipe section 3 is an example of the flow path device in the present invention, and the tank 6 to the temperature sensor 14 are examples of the cooling / heating device in the present invention. The pipe line part 3 is made of copper, aluminum, or other good heat conductive metal.

不凍液循環装置7は、少なくとも−20℃〜100℃程度の温度範囲で低粘度の液状を呈する不凍液、例えば、エチレングリコール水溶液、プロピレングリコール水溶液などが収容されており、且つ当該不凍液を上記の温度範囲内の所望の温度に保持する冷却・加熱装置および当該不凍液を管路8および管路10を通じてタンク6と不凍液循環装置7との間で循環させるポンプ(いずれも図示せず)を備えている。コイル巻き状管路部3以外の各部は、必要があれば上記の良伝熱性金属にて形成されてもよいが、多くの場合、従来の水分除去装置と同様の材料、例えば、鉄系材料、アルミニウム合金、樹脂材料などで形成されてもよい。   The antifreeze circulating device 7 contains an antifreeze that exhibits a low-viscosity liquid in a temperature range of at least about −20 ° C. to 100 ° C., for example, an ethylene glycol aqueous solution, a propylene glycol aqueous solution, and the like. A cooling / heating device that maintains the desired temperature in the inside and a pump that circulates the antifreeze liquid between the tank 6 and the antifreeze liquid circulation device 7 through the pipe line 8 and the pipe line 10 (both not shown). Each part other than the coil-wound pipe line part 3 may be formed of the above-described highly heat-conductive metal if necessary, but in many cases, the same material as that of the conventional moisture removing device, for example, an iron-based material , An aluminum alloy, a resin material, or the like.

次に、実施の形態1の動作に就き説明する。先ず、不凍液循環装置7を稼動させて同装置7に内蔵する不凍液を例えば−10℃程度に冷却し、三方弁9および三方弁11を操作し、且つ上記内蔵ポンプを操作して、当該不凍液を管路8と管路10とを通じてタンク6と不凍液循環装置7との間で循環させる。タンク6内の不凍液の温度が所望の低温に安定した後、三方弁2および三方弁5を操作して被処理媒体が管路1およびコイル巻き状管路部3を経て管路4から外部Cに流出させる。上記被処理媒体がコイル巻き状管路部3を通過する際にそれに含まれている水分は、コイル巻き状管路部3の内壁面上で効果的に露出氷結し分離され、かくして水分除去された被処理媒体は、管路4から外部Cに流出され、例えば媒体回収装置(図示せず)に回収される。その際、管路4の端部は当該媒体回収装置の入り口と接続しておくとよい。   Next, the operation of the first embodiment will be described. First, the antifreeze circulating device 7 is operated to cool the antifreeze contained in the device 7 to about −10 ° C., for example, the three-way valve 9 and the three-way valve 11 are operated, and the built-in pump is operated to remove the antifreeze liquid. It is circulated between the tank 6 and the antifreeze circulating device 7 through the pipe line 8 and the pipe line 10. After the temperature of the antifreeze liquid in the tank 6 is stabilized at a desired low temperature, the three-way valve 2 and the three-way valve 5 are operated so that the medium to be treated passes through the pipe line 1 and the coiled pipe line part 3 from the pipe line 4 to the outside C. Spill into. When the medium to be treated passes through the coiled duct portion 3, the moisture contained therein is effectively exposed to freezing and separated on the inner wall surface of the coiled duct portion 3 and thus the moisture is removed. The treated medium flows out from the pipe line 4 to the outside C and is collected by, for example, a medium collecting device (not shown). At that time, the end of the conduit 4 is preferably connected to the entrance of the medium recovery device.

コイル巻き状管路部3の内壁面での氷結量が過大となると、当該管路内を閉塞する問題があるので、適当な時点で三方弁2および三方弁5を外部、例えば大気に開放するように図示するA、Bの方向に切り替えて上記被処理媒体のコイル巻き状管路部3内への供給を停止し、且つ三方弁9および三方弁11を操作して不凍液循環装置7内の不凍液が、不凍液循環装置7から出て管路8、三方弁9、管路12、三方弁11、管路10を経て不凍液循環装置7に還流する、あるいはそれと逆方向に還流する循環運転に切り替える。   If the amount of icing on the inner wall surface of the coiled pipe line section 3 becomes excessive, there is a problem of blocking the inside of the pipe line. Therefore, the three-way valve 2 and the three-way valve 5 are opened to the outside, for example, the atmosphere at an appropriate time. In this way, the direction of A and B shown in the figure is switched to stop the supply of the medium to be processed into the coil-wound pipe section 3, and the three-way valve 9 and the three-way valve 11 are operated to operate the antifreeze liquid circulation device 7. The operation is switched to the circulation operation in which the antifreeze liquid exits from the antifreeze liquid circulation device 7 and returns to the antifreeze liquid circulation device 7 through the pipe 8, the three-way valve 9, the pipe 12, the three-way valve 11, and the pipe 10 or in the opposite direction. .

その後、タンク6内の不凍液を加温部13により水の解凍し得る温度、例えば5〜20℃程度に高めると共に三方弁2をA方向に、三方弁5をB方向にそれぞれ開口するようにして大気をコイル巻き状管路部3内に導入し、導入した大気がコイル巻き状管路部3を通過して三方弁5から外部に抜ける様にする。かくすると、コイル巻き状管路部3の内壁上の氷結物は融解して三方弁5から水蒸気やドレーンとして外部に放出される。コイル巻き状管路部3の内壁上の氷結物が充分除去された後、三方弁2および三方弁5を切り替えて再びコイル巻き状管路部3を冷却し被処理媒体を導入する上記の氷結操作と氷結物の融解による除去操作を繰り返す。   Thereafter, the antifreezing liquid in the tank 6 is increased to a temperature at which the water can be thawed by the heating unit 13, for example, about 5 to 20 ° C., and the three-way valve 2 is opened in the A direction and the three-way valve 5 is opened in the B direction. Atmosphere is introduced into the coiled conduit 3 so that the introduced atmosphere passes through the coiled conduit 3 and exits from the three-way valve 5 to the outside. As a result, the icing matter on the inner wall of the coiled duct section 3 is melted and discharged from the three-way valve 5 to the outside as water vapor or drain. After the icing matter on the inner wall of the coiled conduit 3 is sufficiently removed, the three-way valve 2 and the three-way valve 5 are switched to cool the coiled conduit 3 again and introduce the medium to be treated. Repeat the operation and the removal operation by thawing the frozen matter.

本発明において、上記媒体としては従来から当該技術分野で採用されているものであって良く、例えば凝固点が−1℃以下、好ましくは−10℃以下で、室温で気体状の各種のフルオロカ−ボン類である。それらを例示すると、トリフルオロメタン、テトラフルオロメタン、トリフルオロエタン、ペンタフルオロエタン、ヘキサフルオロエタン、ペンタフルオロプロパン、ヘキサフルオロプロパン、等のフルオロカーボン類、モノクロロ−モノフルオロ−メタン、モノクロロ−トリフルオロ−メタン、ジクロロ−ジフルオロ−メタン、トリクロロ−モノフルオロ−メタン、モノクロロ−モノフルオロ−エタン、ジクロロ−トリフルオロ−エタン、モノクロロ−テトラフルオロ−エタン、ジクロロ−ペンタフルオロ−プロパン、などのクロロフルオロカーボン類などである。   In the present invention, the medium may be a medium conventionally used in the technical field. For example, various fluorocarbons having a freezing point of −1 ° C. or lower, preferably −10 ° C. or lower and gaseous at room temperature. It is kind. Examples thereof include trifluoromethane, tetrafluoromethane, trifluoroethane, pentafluoroethane, hexafluoroethane, pentafluoropropane, hexafluoropropane, etc., fluorocarbons, monochloro-monofluoro-methane, monochloro-trifluoro-methane Chlorofluorocarbons such as dichloro-difluoro-methane, trichloro-monofluoro-methane, monochloro-monofluoro-ethane, dichloro-trifluoro-ethane, monochloro-tetrafluoro-ethane, dichloro-pentafluoro-propane, etc. .

被処理媒体の例として、冷媒R12(ジクロロジフルオロメタン)が溶存した冷凍機油(合成油:一般的な飽和水分量は、50〜100ppmである。)20リットルから回収して得た冷媒R12を被検体ガスを使用した。この被検体ガスに混入する水分を除去するために、実施の形態1と同条件で氷結とを解凍とを行ったところ、検出された水の質量は1.47gであった。上記冷凍機油の飽和水分量を100ppmとした場合の検出水分量の一致度は82%であって、工業的には良好に一致していることを確認した。   As an example of the medium to be treated, refrigerant R12 obtained by recovering from 20 liters of refrigeration oil (synthetic oil: general saturated water content is 50 to 100 ppm) in which refrigerant R12 (dichlorodifluoromethane) is dissolved is covered. Specimen gas was used. In order to remove the moisture mixed in the analyte gas, freezing and thawing were performed under the same conditions as in the first embodiment. As a result, the detected water mass was 1.47 g. When the saturated water content of the refrigerating machine oil was set to 100 ppm, the degree of coincidence of the detected water amount was 82%, and it was confirmed that the coincidence was good industrially.

被処理媒体の例として、冷媒R134a(1,1,1,2−テトラフルオロエタン)が溶存した冷凍機油(エステル油:一般的な飽和水分量は、500ppm程度である。)20リットルから回収して得た冷媒R134aを使用した。カールフィッシャ法で測定した当該冷凍機油の含有水分量が170ppmであるものを採用した以外は、実施例1と同条件で氷結と解凍とを行ったところ、検出された水の質量は2.20gであって、検出水分量の一致度は72%であった。   As an example of the medium to be treated, the refrigerant R134a (1,1,1,2-tetrafluoroethane) is dissolved from 20 liters of refrigerating machine oil (ester oil: a general saturated water content is about 500 ppm). The refrigerant R134a obtained above was used. When freezing and thawing were performed under the same conditions as in Example 1 except that the water content of the refrigerator oil measured by the Karl Fischer method was 170 ppm, the mass of detected water was 2.20 g. And the coincidence degree of the detected water content was 72%.

実施の形態2.
図2は、本発明の実施の形態2における水分除去装置の構成を示す図である。図2において、当該水分除去装置は、符号1〜14の各部は前記実施の形態1のそれらと同じものであって同じ機能をなす。但し、実施の形態1における加温部13は設けられておらず、バッファタンク15、管路16、管路17、管路18、管路18に設けられたポンプ19、および管路16に設けられた2個の二方弁20、21、管路17に設けに設けられた2個の二方弁22、23、を有することにおいて前記実施の形態1の装置と異なる。
Embodiment 2. FIG.
FIG. 2 is a diagram showing the configuration of the moisture removing apparatus according to Embodiment 2 of the present invention. In FIG. 2, in the moisture removing apparatus, each part of reference numerals 1 to 14 is the same as those in the first embodiment and has the same function. However, the heating unit 13 in the first embodiment is not provided, and is provided in the buffer tank 15, the pipeline 16, the pipeline 17, the pipeline 18, the pump 19 provided in the pipeline 18, and the pipeline 16. The two two-way valves 20 and 21 and the two two-way valves 22 and 23 provided in the pipe 17 are different from the apparatus of the first embodiment.

実施の形態2では、冷媒中の水分を氷結して除去する過程は実施の形態1と同じである。コイル巻き状管路部3の内壁上に氷結された水分を除去するため、三方弁5で冷媒ガスの導入を遮断し、且つ三方弁9と三方弁11とでタンク6と不凍液循環装置7とを遮断し、管路8、管路12、管路11、および不凍液循環装置7の閉回路内での循環運転に切り替える。その後、4個の二方弁20〜23を切り替え、ポンプ19を稼動させて、タンク6内の冷水をバッファタンク15内に移送してタンク6内の冷水を抜く。次いで、三方弁2のAから熱風を導入し、それをタンク6内に供給してタンク6内を加熱し、三方弁5のBから外部へ排出する。上記の加熱と排気により、コイル巻き状管路部3内の氷結物を解凍し、それを水蒸気あるいはドレーンとして大気中に放出する。その後、二方弁20〜23を切り替え、ポンプ19を作動してバッファタンク15内の冷水をタンク6に戻す。次いで、三方弁9、三方弁11を切替えてタンク6と不凍液循環装置7とを連通させ、再びタンク6内での冷水循環に切り替える。従って、実施の形態2では冷水を加温しないために加温に必要なエネルギーの節約、タンク6内での冷却再開までの時間が短縮されるなどの利点がある。   In the second embodiment, the process of freezing and removing moisture in the refrigerant is the same as in the first embodiment. In order to remove the water frozen on the inner wall of the coiled duct 3, the introduction of the refrigerant gas is blocked by the three-way valve 5, and the tank 6 and the antifreeze liquid circulation device 7 are formed by the three-way valve 9 and the three-way valve 11. Is switched to the circulation operation in the closed circuit of the pipeline 8, the pipeline 12, the pipeline 11, and the antifreeze liquid circulation device 7. Thereafter, the four two-way valves 20 to 23 are switched, the pump 19 is operated, the cold water in the tank 6 is transferred into the buffer tank 15, and the cold water in the tank 6 is drained. Next, hot air is introduced from A of the three-way valve 2, supplied to the tank 6 to heat the tank 6, and discharged from B of the three-way valve 5 to the outside. By the above heating and exhaust, the frozen matter in the coiled duct 3 is thawed and released into the atmosphere as water vapor or drain. Thereafter, the two-way valves 20 to 23 are switched, the pump 19 is operated, and the cold water in the buffer tank 15 is returned to the tank 6. Next, the three-way valve 9 and the three-way valve 11 are switched to allow the tank 6 and the antifreeze circulating device 7 to communicate with each other, and switching to the cold water circulation in the tank 6 is performed again. Therefore, in the second embodiment, since cold water is not heated, there are advantages such as saving energy required for heating and shortening the time until the cooling in the tank 6 is resumed.

以上、本発明を実施の形態1、2で詳細に説明したが、本発明はそれらの実施の形態に制限されるものではなく、本発明の解決課題や解決手段の精神に沿った種々の実施の形態を包含する。なお、実施の形態で説明したコイル巻き状管路部3の冷媒の冷却に実質的に寄与する管長は、導入される冷媒ガスの温度、流量、コイル巻き状管路部3の冷却管断面積、冷水温度、比熱、熱伝導率、プラントル数などの要素で決定されるため、冷却管内部に突起などを設けて断面積を大きくすることで短くすることができる。また、実施の形態1、2で使用された二方弁や三方弁を電磁弁などとすることにより全ての動作を自動化することができることは勿論である。   The present invention has been described in detail in the first and second embodiments. However, the present invention is not limited to these embodiments, and various implementations in accordance with the problem to be solved and the spirit of the solution means of the present invention. Of the form. The tube length that substantially contributes to the cooling of the refrigerant in the coiled winding line portion 3 described in the embodiment is the temperature and flow rate of the introduced refrigerant gas, and the cross-sectional area of the cooling pipe in the coiled winding line portion 3. Since it is determined by factors such as the cold water temperature, specific heat, thermal conductivity, and Prandtl number, it can be shortened by providing a protrusion in the cooling pipe to increase the cross-sectional area. Of course, all the operations can be automated by using the two-way valve or the three-way valve used in the first and second embodiments as a solenoid valve.

本発明は、冷蔵庫、ショーケース、空気調和機などの冷凍空調機器が具備する冷媒回路で使用された冷凍機油から冷媒を回収する上で利用される可能性が高い。   The present invention is highly likely to be used for recovering refrigerant from refrigerating machine oil used in a refrigerant circuit provided in a refrigerating and air-conditioning apparatus such as a refrigerator, a showcase, and an air conditioner.

1 管路、2 三方弁、3 コイル巻き状管路部、4 管路、5 三方弁、6 タンク、7 不凍液循環装置、8 管路、9 三方弁、10 管路、11 三方弁、12 管路、13 加温部、14 温度センサ、15 バッファタンク、16 管路、17 管路、
18 管路、19 管ポンプ、20 二方弁、21 二方弁、22 二方弁、
23 二方弁
1 pipe, 2 three-way valve, 3 coil winding pipe, 4 pipe, 5 three-way valve, 6 tank, 7 antifreeze circulating device, 8 pipe, 9 three-way valve, 10 pipe, 11 three-way valve, 12 pipe Path, 13 heating section, 14 temperature sensor, 15 buffer tank, 16 pipe line, 17 pipe line,
18 pipes, 19 pipe pumps, 20 two-way valves, 21 two-way valves, 22 two-way valves,
23 Two-way valve

Claims (7)

良伝熱性金属製であって水分を含む冷媒を流す流路装置、上記流路装置を収容する流路収容槽、上記冷媒は凍結しないが上記水分は上記流路装置の内壁上に氷結する温度に冷却するための低温流体を上記流路収容槽に供給する低温流体供給装置、上記流路収容槽内の低温流体を一時的に収容するバッファタンク、上記低温流体を上記流路収容槽から上記バッファタンクへ、あるいはその逆方向に移送する双方向移送装置、および上記流路装置を加熱して上記内壁上の氷結物を溶融する加熱装置を備えたことを特徴とする水分除去装置。 A flow channel device made of a highly heat-conductive metal and flowing a refrigerant containing moisture, a channel housing tank for accommodating the channel device, and a temperature at which the moisture does not freeze but the moisture freezes on the inner wall of the channel device A low-temperature fluid supply device for supplying a low-temperature fluid for cooling to the flow path storage tank, a buffer tank for temporarily storing the low-temperature fluid in the flow path storage tank, and the low-temperature fluid from the flow path storage tank A moisture removing device comprising: a bidirectional transfer device for transferring to a buffer tank or in the opposite direction; and a heating device for heating the flow path device to melt the frozen matter on the inner wall. 上記流路装置は、コイル巻き状管路部を有し、上記低温流体供給装置および上記加熱装置は、上記コイル巻き状管路部を、それぞれ冷却および加熱するものであることを特徴とする請求項1に記載の水分除去装置。   The flow path device has a coiled duct portion, and the low-temperature fluid supply device and the heating device cool and heat the coiled duct portion, respectively. Item 2. A moisture removing apparatus according to Item 1. 上記流路装置内で上記氷結物が溶融して生じた水を上記流路装置の外に排出する気体吹き込み手段を有することを特徴とする請求項1または2に記載の水分除去装置。   The moisture removing device according to claim 1 or 2, further comprising gas blowing means for discharging water generated by melting the frozen matter in the flow channel device to the outside of the flow channel device. 上記流路収容槽と上記低温流体供給装置との間には、上記低温流体供給装置から上記流路収容槽に低温流体を供給する管路、および上記低温流体供給装置から流出した低温流体を上記流路収容槽に供給せずに上記低温流体供給装置に還流させる循環管路とを有することを特徴とする請求項1〜3の何れか項に記載の水分除去装置。 Between the flow path storage tank and the low temperature fluid supply device, a pipe for supplying a low temperature fluid from the low temperature fluid supply apparatus to the flow path storage tank, and the low temperature fluid flowing out from the low temperature fluid supply apparatus moisture removal device according to any one of claims 1-3, characterized in that it comprises a circulation pipe for circulating to the cryogenic fluid supply apparatus without supplying the flow path containing tank. 上記流路装置、上記流路収容槽、および上記加熱装置を含む水分除去装置部分を2対以上有する請求項1〜の何れか項に記載の水分除去装置。 The flow path unit, the flow path containing tank, and moisture removal device according to any one of claim 1 to 4 having water eliminator part two or more pairs including the heating device. 良伝熱性金属製であって水分を含む冷媒を流す流路装置、上記流路装置を収容する流路収容槽、上記冷媒は凍結しないが上記水分は上記流路装置の内壁上に氷結する温度に冷却するための低温流体を上記流路収容槽に供給する低温流体供給装置、および上記流路装置を加熱して上記内壁上の氷結物を溶融する加熱装置を備えた水分除去装置を用い、水分を含む被処理冷媒を上記流路装置に流す第一工程、上記流路装置を上記冷媒は凍結しないが上記水分は氷結する温度に冷却する第二工程、および上記加熱装置により上記流路装置を
加熱して上記氷結物を解凍する第三工程、上記第二工程の後、流路収容槽内の低温流体の略全量を一時的に収容するバッファタンクに移送する第四工程、上記第四工程の後、流路収容槽内に少なくとも20℃の温風または熱風を導入して上記流路装置を加熱して上記氷結物を解凍する第五工程を含むことを特徴とする水分除去方法。
A flow channel device made of a highly heat-conductive metal and flowing a refrigerant containing moisture, a channel housing tank for accommodating the channel device, and a temperature at which the moisture does not freeze but the moisture freezes on the inner wall of the channel device Using a moisture removing device provided with a low-temperature fluid supply device that supplies a low-temperature fluid for cooling to the flow passage housing tank, and a heating device that heats the flow passage device and melts the frozen matter on the inner wall, A first step of flowing a refrigerant to be treated to flow through the flow path device; a second step of cooling the flow path device to a temperature at which the refrigerant does not freeze, but the water freezes; The fourth step of heating the lyophilized product and the second step, the fourth step of transferring substantially the entire amount of the low-temperature fluid in the flow path storage tank to the buffer tank, and the fourth step After the process, at least 20 ° C. in the flow path storage tank Water removal method characterized by introducing the air or hot air by heating the flow path unit includes a fifth step of thawing the frost.
上記流路装置、上記流路収容槽、および上記加熱装置を含む水分除去装置部分を2対以上有する複数の水分除去装置を用い、複数の水分除去装置を交互に運転することを特徴とする請求項に記載の水分除去方法。 A plurality of moisture removing devices having two or more pairs of moisture removing devices including the channel device, the channel housing tank, and the heating device are operated alternately. Item 7. A method for removing moisture according to Item 6 .
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