JP2004190894A - Refrigerant filling method of refrigeration cycle and refrigerant filling device - Google Patents

Refrigerant filling method of refrigeration cycle and refrigerant filling device Download PDF

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Publication number
JP2004190894A
JP2004190894A JP2002356831A JP2002356831A JP2004190894A JP 2004190894 A JP2004190894 A JP 2004190894A JP 2002356831 A JP2002356831 A JP 2002356831A JP 2002356831 A JP2002356831 A JP 2002356831A JP 2004190894 A JP2004190894 A JP 2004190894A
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refrigerant
refrigeration cycle
volume
charging
variable volume
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Japanese (ja)
Inventor
Toshio Hirata
敏夫 平田
Tomokazu Yamanaka
智一 山中
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Denso Corp
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Denso Corp
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Priority to JP2002356831A priority Critical patent/JP2004190894A/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B60VEHICLES IN GENERAL
    • B60HARRANGEMENTS OF HEATING, COOLING, VENTILATING OR OTHER AIR-TREATING DEVICES SPECIALLY ADAPTED FOR PASSENGER OR GOODS SPACES OF VEHICLES
    • B60H1/00Heating, cooling or ventilating devices
    • B60H1/00507Details, e.g. mounting arrangements, desaeration devices
    • B60H1/00585Means for monitoring, testing or servicing the air-conditioning
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B45/00Arrangements for charging or discharging refrigerant
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2309/00Gas cycle refrigeration machines
    • F25B2309/06Compression machines, plants or systems characterised by the refrigerant being carbon dioxide
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2345/00Details for charging or discharging refrigerants; Service stations therefor
    • F25B2345/001Charging refrigerant to a cycle
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B9/00Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
    • F25B9/002Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant
    • F25B9/008Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant the refrigerant being carbon dioxide

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a refrigerant filling method and a refrigerant filling device capable of additionally filling the refrigerant at an appropriate amount without discharging the refrigerant. <P>SOLUTION: The device is provided with a refrigerant storage container 6 storing the refrigerant, a supply path K supplying the refrigerant from the refrigerant storage container 6 to a refrigeration cycle R, and a volume variable part 5 provided by branching from the middle of the supply path K. When the outside air temperature Ta is lower than the critical temperature Tc of the refrigerant, the refrigerant in the volume variable part 5 is sucked into the refrigeration cycle R after the refrigerant is additionally filled to the refrigerant pressure Pn1 at the time when the refrigerant is filled to the appropriate amount by adding the volume V0 in the volume variable part 5 to the refrigeration cycle R. The refrigerant can be additionally filled at the appropriate amount without discharging the refrigerant. <P>COPYRIGHT: (C)2004,JPO&NCIPI

Description

【0001】
【発明の属する技術分野】
本発明は、圧縮機、凝縮器、減圧装置および蒸発器を環状に接続した冷凍サイクルに冷媒を追加充填する場合の冷媒充填方法および冷媒充填装置に関するものであり、特に、臨界温度の低いCO等の冷媒の冷媒充填方法および冷媒充填装置に関する。
【0002】
【従来の技術】
従来、臨界温度の高いフロン冷媒等では、冷媒の気液状態をレシーバのサイトグラスから確認しながら適正量の追加充填ができる。これに対し、臨界温度の低いCO冷媒等では冷媒がガスの単相状態となるため、目視で確認しながら適正量を追加充填するということができない。そのため、CO冷媒等を用いた冷凍サイクルにおいて冷媒を追加充填する場合、実際には一旦冷凍サイクル内の冷媒を全て放出してから、重量を計測しながら正規の充填量だけ冷媒を充填し直している。
【0003】
【発明が解決しようとする課題】
しかしながら、上記した冷凍サイクル内の冷媒を全て放出してから充填し直す上では次のような問題点がある。
・ 冷媒放出時、コンプレッサオイルも同時に放出されるため、充填し直した後にコンプレッサオイルの不足によりコンプレッサの潤滑不良を引き起こす可能性がある。
・ 放出したコンプレッサオイルが霧状となって人体に吸入され、気管支系の障害等で悪影響を及ぼす可能性がある。
・ 正規の充填量を計測するためには、ボンベ等の冷媒容器ごと重量計測できる上、充填した量を検出できるだけの精度を持った量りが必要となる。
【0004】
本発明は、上記従来の問題点に鑑みて成されたものであり、その目的は、冷媒を放出することなく適正量に追加充填することのできる冷媒充填方法および冷媒充填装置を提供することにある。
【0005】
【課題を解決するための手段】
上記目的を達成するために、請求項1ないし請求項5に記載の技術的手段を採用する。すなわち、請求項1に記載の発明では、冷媒の圧縮機(10)、凝縮器(11)、減圧装置(12)、および蒸発器(13)を順に冷媒配管(14)で環状に接続した冷凍サイクル(R)と、冷媒を貯蔵している冷媒貯蔵手段(6)と、冷媒貯蔵手段(6)から冷凍サイクル(R)へ冷媒を供給する供給路(K)と、供給路(K)の途中から分岐して設けられた容積可変部(5)とを設け、冷凍サイクル(R)に冷媒を追加充填する際の冷媒充填方法であり、
外気温度(Ta)が冷媒の臨界温度(Tc)よりも低い場合、冷凍サイクル(R)に容積可変部(5)の容積(V0)を加えて冷媒を適正量充填した時の冷媒圧力(Pn0)まで追加充填した後、容積可変部(5)の冷媒を冷凍サイクル(R)内に吸引させることを特徴とする。
【0006】
また、請求項2に記載の発明では、冷媒の圧縮機(10)、凝縮器(11)、減圧装置(12)、および蒸発器(13)を順に冷媒配管(14)で環状に接続した冷凍サイクル(R)に冷媒を追加充填する際の冷媒充填方法および冷媒充填装置あり、冷媒を貯蔵している冷媒貯蔵手段(6)と、冷媒貯蔵手段(6)から冷凍サイクル(R)へ冷媒を供給する供給路(K)と、供給路(K)の途中から分岐して設けられた容積可変部(5)とを備え、
外気温度(Ta)が冷媒の臨界温度(Tc)よりも低い場合、冷凍サイクル(R)に容積可変部(5)の容積(V0)を加えて冷媒を適正量充填した時の冷媒圧力(Pn0)まで追加充填した後、容積可変部(5)の冷媒を冷凍サイクル(R)内に吸引させることを特徴とする。
【0007】
これらにより、冷媒を放出することなく適正量に追加充填する(補充だけですませる)ことができる。また、冷媒を放出しなくなることより、コンプレッサオイルを放出してコンプレッサの潤滑不良を引き起こしたり、人体に悪影響を及ぼしたりする可能性がなくなるうえ、従来作業と比べて作業安全が確保でき、作業時間も短縮できる。また、従来と同様の圧力計だけで適正な充填量を量ることができる。
【0008】
請求項3に記載の発明では、容積可変部(5)の容積(V0)は、外気温度(Ta)が冷媒の臨界温度(Tc)よりも低くても容積可変部(5)内の容積(V0)を加えることにより冷凍サイクル(R)内の冷媒がガスの単相状態になる容積(V0)としたことを特徴とする。これにより、冷媒充填作業を行なう時の環境温度(外気温度)が様々であっても、冷媒をガスの単相状態にそろえて冷媒充填作業を行なうことができる。
【0009】
請求項4に記載の発明では、容積可変部(5)をフリーピストン(5a)で構成したことを特徴とする。これにより、冷凍サイクル(R)内の残圧で容易に冷凍サイクル(R)の容積を増やすことができるうえ、冷凍サイクル(R)側で吸引することにより容易に増やした容積をゼロにすることができる。
【0010】
請求項5に記載の発明では、冷媒はフロンガスよりも臨界温度(Tc)の低い冷媒であることを特徴とする。これは、本発明が従来一般的なフロンガスよりも臨界温度(Tc)が低くガスの単相状態になり易いCO等の冷媒を追加充填する際の冷媒充填方法および冷媒充填装置に好適なことによる。尚、上記各手段の括弧内の符号は、後述する実施形態に記載の具体的手段との対応関係を示す一例である。
【0011】
【発明の実施の形態】
以下、本発明の実施形態を、図面に基づき説明する。図1の(a)は、本発明の一実施形態における冷媒充填装置100の構成を示す模式図、(b)は、冷媒を二相から単相にする時の容積可変部5の説明図、(c)は、冷媒吸引時の容積可変部5の説明図である。また、図2は、冷凍サイクルRの概略の構成を示す模式図である。
【0012】
本実施形態は、CO冷媒を用いた車両用空調装置の冷凍サイクルRに冷媒を追加充填する際の冷媒充填装置の構成および冷媒充填方法について説明する。まず、図2に示すように、車両の冷凍サイクルRは、冷媒のコンプレッサ(圧縮機)10、コンデンサ(凝縮器)11、膨張弁(減圧装置)12、エバポレータ(蒸発器)13およびアキュムレータ15を順次冷媒配管14により接続して構成され、冷媒として臨界温度の低いCOを使用している。
【0013】
コンプレッサ10は、共に図示しない車両走行用エンジンもしくは内蔵する電動モータによって駆動され、アキュムレータ15より吸引した冷媒を一般的使用条件において臨界圧力以上まで圧縮して吐出する。コンデンサ11は、コンプレッサ10より吐出された高圧のガス冷媒と送風機11aによって送風される外部空気(以下、外気)とを熱交換するもので、冷媒が流れる冷媒通路と、外気が流れる空気通路とを有し、冷媒の流れ方向と空気の流れ方向とが直交するように構成されている。
【0014】
しかし、コンデンサ11に流入するCO冷媒は、コンプレッサ10で臨界圧力以上に加圧されているので、コンデンサ11で放熱しても凝縮することはない。膨張弁12は、コンデンサ11から流出する冷媒を弁開度に応じて減圧する減圧装置であり、制御装置(図示せず)によって弁開度が電気的に制御される。
【0015】
エバポレータ13は、膨張弁12で減圧された冷媒を送風機13aによって送風される外気もしくは車室内空気との熱交換によって蒸発させる。アキユムレータ15は、エバポレータ13で蒸発した冷媒を気液分離して液冷媒を貯留し、気相冷媒のみコンプレッサ10に吸引させ、サイクル中の余剰冷媒を蓄えておくものである。
【0016】
次に、本発明の要部である冷媒充填装置100の構成および冷媒充填方法について説明する。冷媒充填装置100は、冷媒を貯蔵しているCOボンベ(冷媒貯蔵手段)6を内蔵もしくは接続できるようになっており、そのCOボンベ6と、そこから冷凍サイクルRへ冷媒を供給する供給路Kとからなっている。供給路Kには冷媒の供給を断続させるためのバルブ1が設けられている。
【0017】
また、供給路Kの途中から分岐して容積可変部5が設けられている。この容積可変部5は、圧力タンクとなっており、内部には容積を可変するためのフリーピストン5aが内蔵されている((b)参照)。フリーピストン5aは、Oリング5bでシールを保ちながら両側の圧力差によって自由に内部を摺動する構造となっている。
【0018】
容積可変部5の一方には冷凍サイクルRとの連通を断続させるためのバルブ2が設けられている。また、容積可変部5の他方には内部の気体を外部へ逃がす時に開閉するバルブ3と、COボンベ6との連通を断続させるためのバルブ4とが設けられている。100aは冷凍サイクルR側と接続するためのジョイント部である。
【0019】
冷凍サイクルR側の接続部は、エバポレータ13とアキュムレータ15との間の冷媒配管14に低圧側サービスバルブ14aが配設されている(図2参照)。ちなみに14bは高圧側サービスバルブである。そして、ゲージマニホールド7で冷凍サイクルRと冷媒充填装置100とを接続する(図1参照)。尚、ゲージマニホールド7は冷凍サイクルの作動圧点検および真空引きや冷媒充填時に使用される器具である。
【0020】
具体的に、低圧チャージングホース7aを低圧側サービスバルブ14aに、高圧チャージングホース7bを高圧側サービスバルブ14bに、そしてセンターチャージングホース7cを冷媒充填装置100のジョイント100aに接続する。ちなみにこの時、ゲージマニホールド7の低圧バルブ7d・高圧バルブ7eおよび冷媒充填装置100のバルブ1〜4は全て閉じた状態とし、冷媒充填時にゲージマニホールド7の低圧バルブ7dを開いて冷凍サイクルRと冷媒充填装置100とを連通させる。
【0021】
次に、COボンベ6から冷凍サイクルR内にCO冷媒を追加充填させる手順について図3のフローチャートを用いて説明する。図3は本発明の冷媒充填装置100における冷媒追加充填時の作動を示すフローチャートである。まず、冷媒充填作業を行なう前の必要データとして、正規の冷媒充填量Gnと、冷凍サイクルRの内容積Vinを調べ、これらから下記の数式1で正規の冷媒充填量Gnが充填された時の冷媒密度γgを出しておく。
【0022】
【数式1】
γg=Gn/Vin
次に、ステップS1で冷媒充填作業を行なう時の環境温度として、外気温度Taを読み込む。そして、ステップS2でその外気温度Taが冷媒の臨界温度Tcよりも高いか否かの判定を行なう。この判定で外気温度Taが臨界温度Tcより高くYESの場合はステップS3に進みバルブ1を開いて冷媒を供給する。外気温度Taが冷媒の臨界温度Tcよりも高いということは、冷凍サイクルR内の冷媒はガスの単相状態のため、適正冷媒量充填時の冷媒圧力Pnが下記の数式2より導き出される。
【0023】
【数式2】
Pn=Pn(γg、Ta)
そして、ステップS4でゲージマニホールド7のゲージで検出される冷凍サイクルの圧力PがPnに到達しておらず判定結果がNOの場合は、ステップS5で冷媒の追加充填を行ない、ステップS4で冷凍サイクルの圧力PがPnに到達して判定結果がYESになったらステップS6に進みバルブ1を閉じて冷媒の追加充填を終了する。
【0024】
次に、ステップS2の判定で外気温度Taが臨界温度Tcより低くNOの場合はステップS7に進みバルブ2・3を開く。外気温度Taが冷媒の臨界温度Tcよりも低いということは、冷凍サイクルR内の冷媒は気液二相状態のため、上記の手段で適正量は求められない。
【0025】
そのため、バルブ2・3を開いて容積可変部5に冷凍サイクルR内の残圧を加えてフリーピストン5aを移動させ、冷凍サイクルR内容積Vinに容積可変部5の容積V0を加えて大きくし、冷凍サイクルR内の冷媒をガスの単相状態にする。ちなみに、容積可変部5の内部は図1(b)の状態となる。
【0026】
この容積を大きくした状態で正規の冷媒充填量Gnが充填された時の冷媒密度γg0を下記の数式3より導き出す。また、ガスの単相状態のため、適正冷媒量充填時の冷媒圧力Pn0を下記の数式4で計算する。
【0027】
【数式3】
γg0=Gn/(Vin+V0)
【0028】
【数式4】
Pn0=Pn0(γg0、Ta)
そして、ステップS8で逃がしバルブ3を閉じると共に、バルブ1を開いて冷媒を供給する。ステップS9でゲージマニホールド7のゲージで検出される冷凍サイクルの圧力PがPn0に到達しておらず判定結果がNOの場合は、ステップS10で冷媒の追加充填を行ない、ステップS9で冷凍サイクルの圧力PがPn0に到達して判定結果がYESになったらステップS11に進む。
【0029】
ステップS11では、バルブ1を閉じて冷媒の供給を停止すると共に、バルブ4を開いてCOボンベ6の圧力をフリーピストン5aがバルブ2側へ移動するように加える。次に、ステップS12でコンプレッサ10を駆動させ、容積可変部5内の冷媒を冷凍サイクルR内に吸引させる。ちなみにこの時、容積可変部5の内部は図1(c)の状態となる。そして冷媒を吸引した後ステップS13でバルブ2・4を閉じて冷媒の追加充填を終了する。
【0030】
次に、本実施形態での特徴を説明する。まず、冷媒を貯蔵しているCOボンベ等の冷媒貯蔵手段6と、その冷媒貯蔵手段6から冷凍サイクルRへ冷媒を供給する供給路Kと、その供給路Kの途中から分岐して設けられた容積可変部5とを設け、外気温度Taが冷媒の臨界温度Tcよりも低い場合、冷凍サイクルRに容積可変部5の容積V0を加えて冷媒を適正量充填した時の冷媒圧力Pn0まで追加充填した後、容積可変部5の冷媒を冷凍サイクルR内に吸引させている。
【0031】
これにより、冷媒を放出することなく適正量に追加充填する(補充だけですませる)ことができる。また、冷媒を放出しなくなることより、コンプレッサオイルを放出してコンプレッサの潤滑不良を引き起こしたり、人体に悪影響を及ぼしたりする可能性がなくなるうえ、従来作業と比べて作業安全が確保でき、作業時間も短縮できる。また、従来と同様の圧力計だけで適正な充填量を量ることができる。
【0032】
また、容積可変部5の容積V0は、外気温度Taが冷媒の臨界温度Tcよりも低くても容積可変部5内の容積V0を加えることにより冷凍サイクルR内の冷媒がガスの単相状態になる容積V0としている。これにより、冷媒充填作業を行なう時の環境温度(外気温度)が様々であっても、冷媒をガスの単相状態にそろえて冷媒充填作業を行なうことができる。
【0033】
また、容積可変部5をフリーピストン5aで構成している。これにより、冷凍サイクルR内の残圧で容易に冷凍サイクルRの容積を増やすことができるうえ、冷凍サイクルR側で吸引することにより容易に増やした容積をゼロにすることができる。
【0034】
また、冷媒はフロンガスよりも臨界温度Tcの低い例えばCO等の冷媒である。これは、本発明が従来一般的なフロンガスよりも臨界温度Tcが低くガスの単相状態になり易いCO等の冷媒を追加充填する際の冷媒充填方法および冷媒充填装置に好適なことによる。
【0035】
(その他の実施形態)
上述の実施形態では、車両用空調装置に対する冷媒の追加充填に本発明の冷媒充填方法および冷媒充填装置を適用しているが、本発明はこれに限定されるものではなく、定置式の空調装置や給湯装置等冷媒を用いる冷凍サイクル全般の冷媒の追加充填に適用しても良い。また、冷媒もCOに限らず、臨界温度の低いものであればエチレン・エタン・酸化窒素等の冷媒に適用しても良い。
【図面の簡単な説明】
【図1】(a)は、本発明の一実施形態における冷媒充填装置の構成を示す模式図、(b)は、冷媒を二相から単相にする時の容積可変部の説明図、(c)は、冷媒吸引時の容積可変部の説明図である。
【図2】冷凍サイクルの概略の構成を示す模式図である。
【図3】本発明の冷媒充填装置における冷媒追加充填時の作動を示すフローチャートである。
【符号の説明】
5 容積可変部
5a フリーピストン
6 COボンベ(冷媒貯蔵手段)
10 コンプレッサ(圧縮機)
11 コンデンサ(凝縮器)
12 膨張弁(減圧装置)
13 エバポレータ(蒸発器)
14 冷媒配管
K 供給路
Pn0 冷媒圧力
R 冷凍サイクル
Ta 外気温度
Tc 臨界温度
V0 容積可変部内の容積
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention includes a compressor, a condenser, a decompressor and an evaporator relates refrigerant charging method and refrigerant charging apparatus for adding fill the refrigerant in the refrigerating cycle annularly connecting, in particular, low critical temperature CO 2 And a refrigerant charging method.
[0002]
[Prior art]
Conventionally, for a Freon refrigerant or the like having a high critical temperature, an appropriate amount of additional charge can be performed while checking the gas-liquid state of the refrigerant from the sight glass of the receiver. On the other hand, in the case of a CO 2 refrigerant or the like having a low critical temperature, the refrigerant is in a single-phase gas state, so that it is not possible to additionally charge an appropriate amount while visually checking the refrigerant. Therefore, when the refrigerant is additionally charged in a refrigeration cycle using a CO 2 refrigerant or the like, the refrigerant in the refrigeration cycle is actually discharged once, and then the refrigerant is refilled by a regular amount while measuring the weight. ing.
[0003]
[Problems to be solved by the invention]
However, there are the following problems in discharging and refilling the refrigerant in the refrigeration cycle.
-When the refrigerant is discharged, the compressor oil is also discharged at the same time, so there is a possibility that insufficient lubrication of the compressor due to lack of compressor oil after refilling.
・ The released compressor oil may be in the form of a mist and inhaled by the human body.
-In order to measure the regular filling amount, it is necessary to measure the weight of each refrigerant container such as a cylinder, and to weigh with sufficient accuracy to detect the filled amount.
[0004]
The present invention has been made in view of the above-described conventional problems, and an object of the present invention is to provide a refrigerant charging method and a refrigerant charging device capable of additionally charging an appropriate amount without discharging the refrigerant. is there.
[0005]
[Means for Solving the Problems]
In order to achieve the above object, the technical means described in claims 1 to 5 is adopted. That is, according to the first aspect of the present invention, a refrigeration system in which a refrigerant compressor (10), a condenser (11), a pressure reducing device (12), and an evaporator (13) are sequentially connected in a ring by a refrigerant pipe (14). A cycle (R), a refrigerant storage means (6) storing the refrigerant, a supply path (K) for supplying the refrigerant from the refrigerant storage means (6) to the refrigeration cycle (R), and a supply path (K). A variable volume section (5) branching from the middle, and a refrigerant charging method for additionally charging the refrigerant to the refrigeration cycle (R).
When the outside air temperature (Ta) is lower than the critical temperature (Tc) of the refrigerant, the refrigerant pressure (Pn0) when the appropriate amount of refrigerant is charged by adding the volume (V0) of the variable volume section (5) to the refrigeration cycle (R). ), The refrigerant in the variable volume section (5) is sucked into the refrigeration cycle (R).
[0006]
According to the second aspect of the present invention, a refrigeration system in which a refrigerant compressor (10), a condenser (11), a pressure reducing device (12), and an evaporator (13) are connected in order in a refrigerant pipe (14). A refrigerant charging method and a refrigerant charging device for additionally charging a refrigerant to the cycle (R) include a refrigerant storage means (6) storing the refrigerant, and a refrigerant from the refrigerant storage means (6) to the refrigeration cycle (R). A supply path (K) for supply, and a variable volume section (5) branched from the middle of the supply path (K),
When the outside air temperature (Ta) is lower than the critical temperature (Tc) of the refrigerant, the refrigerant pressure (Pn0) when the appropriate amount of refrigerant is charged by adding the volume (V0) of the variable volume section (5) to the refrigeration cycle (R). ), The refrigerant in the variable volume section (5) is sucked into the refrigeration cycle (R).
[0007]
By these means, it is possible to additionally charge the refrigerant to an appropriate amount without discharging the refrigerant (only replenishment is required). In addition, since no refrigerant is released, there is no possibility that the compressor oil will be released to cause poor lubrication of the compressor or adversely affect the human body. Can also be shortened. In addition, an appropriate filling amount can be measured only by using a conventional pressure gauge.
[0008]
According to the third aspect of the present invention, the volume (V0) of the variable-volume section (5) can be set such that the volume (V0) of the variable-volume section (5) can be reduced even if the outside air temperature (Ta) is lower than the critical temperature (Tc) of the refrigerant. V0) is added to the volume (V0) at which the refrigerant in the refrigeration cycle (R) becomes a single-phase gas state. Thereby, even if the ambient temperature (outside air temperature) at the time of performing the refrigerant charging operation is various, the refrigerant charging operation can be performed by aligning the refrigerant with the single-phase state of the gas.
[0009]
The invention according to claim 4 is characterized in that the variable volume section (5) is constituted by a free piston (5a). Thus, the volume of the refrigeration cycle (R) can be easily increased by the residual pressure in the refrigeration cycle (R), and the volume easily increased by suctioning on the refrigeration cycle (R) side can be made zero. Can be.
[0010]
The invention according to claim 5 is characterized in that the refrigerant is a refrigerant having a lower critical temperature (Tc) than Freon gas. This means that the present invention is suitable for a refrigerant charging method and a refrigerant charging apparatus when additionally charging a refrigerant such as CO 2 which has a lower critical temperature (Tc) than a conventional general fluorocarbon gas and tends to be in a single-phase gas state. by. In addition, the code | symbol in the parenthesis of each said means is an example which shows the correspondence with the concrete means described in embodiment mentioned later.
[0011]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings. FIG. 1A is a schematic diagram illustrating a configuration of a refrigerant charging device 100 according to an embodiment of the present invention, and FIG. 1B is an explanatory diagram of a volume variable unit 5 when the refrigerant is changed from two phases to a single phase. (C) is an explanatory view of the volume variable section 5 during refrigerant suction. FIG. 2 is a schematic diagram showing a schematic configuration of the refrigeration cycle R.
[0012]
In the present embodiment, a configuration and a refrigerant charging method of a refrigerant charging device when a refrigerant is additionally charged into a refrigeration cycle R of a vehicle air conditioner using a CO 2 refrigerant will be described. First, as shown in FIG. 2, a refrigeration cycle R of a vehicle includes a refrigerant compressor (compressor) 10, a condenser (condenser) 11, an expansion valve (decompression device) 12, an evaporator (evaporator) 13, and an accumulator 15. CO 2 having a low critical temperature is used as a refrigerant.
[0013]
The compressor 10 is driven by a vehicle driving engine (not shown) or a built-in electric motor, and compresses and discharges the refrigerant sucked from the accumulator 15 to a critical pressure or higher under general use conditions. The condenser 11 exchanges heat between the high-pressure gas refrigerant discharged from the compressor 10 and external air (hereinafter, “outside air”) blown by the blower 11a, and includes a refrigerant passage through which the refrigerant flows and an air passage through which the outside air flows. It is configured so that the flow direction of the refrigerant and the flow direction of the air are orthogonal.
[0014]
However, since the CO 2 refrigerant flowing into the condenser 11 is pressurized to a critical pressure or higher by the compressor 10, the CO 2 refrigerant does not condense even if heat is radiated by the condenser 11. The expansion valve 12 is a pressure reducing device that reduces the pressure of the refrigerant flowing out of the condenser 11 in accordance with the valve opening. The valve opening is electrically controlled by a control device (not shown).
[0015]
The evaporator 13 evaporates the refrigerant decompressed by the expansion valve 12 by heat exchange with the outside air or the vehicle interior air blown by the blower 13a. The accumulator 15 separates the refrigerant evaporated by the evaporator 13 into gas and liquid, stores the liquid refrigerant, causes only the gas-phase refrigerant to be sucked into the compressor 10, and stores the surplus refrigerant during the cycle.
[0016]
Next, a configuration and a refrigerant charging method of the refrigerant charging device 100 which is a main part of the present invention will be described. The refrigerant charging device 100 is provided with a built-in or connectable CO 2 cylinder (refrigerant storage means) 6 that stores the refrigerant, and supplies the CO 2 cylinder 6 and the refrigerant supplied to the refrigeration cycle R from the CO 2 cylinder 6. Road K. The supply path K is provided with a valve 1 for interrupting the supply of the refrigerant.
[0017]
Further, a variable volume section 5 is provided which branches off in the middle of the supply path K. The volume variable section 5 is a pressure tank, and has a built-in free piston 5a for varying the volume (see (b)). The free piston 5a has a structure in which the free piston 5a slides freely by the pressure difference between both sides while maintaining the seal with the O-ring 5b.
[0018]
A valve 2 for interrupting communication with the refrigeration cycle R is provided on one of the variable volume units 5. The other of the variable volume section 5 is provided with a valve 3 that opens and closes when the internal gas is released to the outside, and a valve 4 for interrupting communication with the CO 2 cylinder 6. 100a is a joint for connecting to the refrigeration cycle R side.
[0019]
In the connection portion on the refrigeration cycle R side, a low-pressure side service valve 14a is disposed in a refrigerant pipe 14 between the evaporator 13 and the accumulator 15 (see FIG. 2). Incidentally, 14b is a high-pressure side service valve. Then, the refrigeration cycle R and the refrigerant charging device 100 are connected by the gauge manifold 7 (see FIG. 1). The gauge manifold 7 is an instrument used for checking the operation pressure of the refrigeration cycle, evacuation and charging the refrigerant.
[0020]
Specifically, the low pressure charging hose 7a is connected to the low pressure side service valve 14a, the high pressure charging hose 7b is connected to the high pressure side service valve 14b, and the center charging hose 7c is connected to the joint 100a of the refrigerant charging device 100. By the way, at this time, the low pressure valve 7d and the high pressure valve 7e of the gauge manifold 7 and the valves 1 to 4 of the refrigerant charging device 100 are all closed, and when the refrigerant is charged, the low pressure valve 7d of the gauge manifold 7 is opened to open the refrigeration cycle R and the refrigerant. The communication with the filling device 100 is performed.
[0021]
Next, a procedure for additionally charging the refrigeration cycle R with the CO 2 refrigerant from the CO 2 cylinder 6 will be described with reference to the flowchart of FIG. FIG. 3 is a flowchart showing the operation of the refrigerant charging apparatus 100 according to the present invention when additional refrigerant is charged. First, as necessary data before performing the refrigerant charging operation, the normal refrigerant charging amount Gn and the internal volume Vin of the refrigeration cycle R are examined. The refrigerant density γg is calculated.
[0022]
[Formula 1]
γg = Gn / Vin
Next, the outside air temperature Ta is read as the ambient temperature when the refrigerant charging operation is performed in step S1. Then, in step S2, it is determined whether or not the outside air temperature Ta is higher than the critical temperature Tc of the refrigerant. If the determination is YES that the outside air temperature Ta is higher than the critical temperature Tc, the process proceeds to step S3 to open the valve 1 and supply the refrigerant. The fact that the outside air temperature Ta is higher than the critical temperature Tc of the refrigerant means that the refrigerant in the refrigeration cycle R is in a single-phase gas state, and thus the refrigerant pressure Pn at the time of charging the appropriate refrigerant amount is derived from the following equation (2).
[0023]
[Formula 2]
Pn = Pn (γg, Ta)
If the pressure P of the refrigeration cycle detected by the gauge of the gauge manifold 7 has not reached Pn in step S4 and the determination result is NO, the refrigerant is additionally charged in step S5, and the refrigeration cycle is determined in step S4. When the pressure P reaches Pn and the determination result is YES, the process proceeds to step S6, the valve 1 is closed, and the additional charging of the refrigerant is completed.
[0024]
Next, if the outside air temperature Ta is lower than the critical temperature Tc and the determination in step S2 is NO, the process proceeds to step S7, and the valves 2.3 are opened. The fact that the outside air temperature Ta is lower than the critical temperature Tc of the refrigerant means that the refrigerant in the refrigeration cycle R is in a gas-liquid two-phase state, so that an appropriate amount cannot be obtained by the above means.
[0025]
Therefore, the valves 2 and 3 are opened to apply the residual pressure in the refrigeration cycle R to the variable volume section 5 to move the free piston 5a, and to increase the volume V0 of the variable volume section 5 to the internal volume Vin of the refrigeration cycle R to increase the volume. Then, the refrigerant in the refrigeration cycle R is brought into a single-phase gas state. Incidentally, the inside of the variable volume section 5 is in the state of FIG.
[0026]
The refrigerant density γg0 when the regular refrigerant filling amount Gn is charged in a state where the volume is increased is derived from the following equation (3). In addition, since the gas is in a single-phase state, the refrigerant pressure Pn0 at the time of filling the appropriate refrigerant amount is calculated by the following Expression 4.
[0027]
(Equation 3)
γg0 = Gn / (Vin + V0)
[0028]
(Equation 4)
Pn0 = Pn0 (γg0, Ta)
Then, in step S8, the escape valve 3 is closed and the valve 1 is opened to supply the refrigerant. If the pressure P of the refrigeration cycle detected by the gauge of the gauge manifold 7 has not reached Pn0 in step S9 and the determination result is NO, the refrigerant is additionally charged in step S10, and the pressure of the refrigeration cycle is determined in step S9. When P reaches Pn0 and the determination result is YES, the process proceeds to step S11.
[0029]
In step S11, the valve 1 is closed to stop the supply of the refrigerant, and the valve 4 is opened to apply the pressure of the CO 2 cylinder 6 so that the free piston 5a moves to the valve 2 side. Next, in step S12, the compressor 10 is driven to suck the refrigerant in the variable volume section 5 into the refrigeration cycle R. Incidentally, at this time, the inside of the variable volume unit 5 is in the state shown in FIG. After the refrigerant is sucked, the valves 2 and 4 are closed in step S13, and the additional charging of the refrigerant is completed.
[0030]
Next, features of the present embodiment will be described. First, a refrigerant storage means 6 such as a CO 2 cylinder storing a refrigerant, a supply path K for supplying the refrigerant from the refrigerant storage means 6 to the refrigeration cycle R, and a branch provided from the middle of the supply path K are provided. When the outside air temperature Ta is lower than the critical temperature Tc of the refrigerant, the volume V0 of the variable volume section 5 is added to the refrigeration cycle R, and the refrigerant pressure Pn0 when the refrigerant is filled with an appropriate amount is added. After filling, the refrigerant in the variable volume section 5 is sucked into the refrigeration cycle R.
[0031]
As a result, the refrigerant can be additionally charged to an appropriate amount without discharging the refrigerant (only replenishment is required). In addition, since no refrigerant is released, there is no possibility that the compressor oil will be released to cause poor lubrication of the compressor or adversely affect the human body. Can also be shortened. In addition, an appropriate filling amount can be measured only by using a conventional pressure gauge.
[0032]
In addition, even if the outside air temperature Ta is lower than the critical temperature Tc of the refrigerant, the volume V0 of the variable volume unit 5 is changed to the single phase state of the gas in the refrigeration cycle R by adding the volume V0 of the variable volume unit 5. Volume V0. Thereby, even if the ambient temperature (outside air temperature) at the time of performing the refrigerant charging operation is various, the refrigerant charging operation can be performed by aligning the refrigerant with the single-phase state of the gas.
[0033]
Further, the volume variable section 5 is constituted by a free piston 5a. Accordingly, the volume of the refrigeration cycle R can be easily increased by the residual pressure in the refrigeration cycle R, and the increased volume can be easily reduced to zero by suction on the refrigeration cycle R side.
[0034]
The refrigerant is a refrigerant having a lower critical temperature Tc than Freon gas, such as CO 2 . This is because the present invention is suitable for a refrigerant charging method and a refrigerant charging apparatus when additionally charging a refrigerant such as CO 2, which has a lower critical temperature Tc than a conventional general fluorocarbon gas and tends to be in a single-phase state of the gas.
[0035]
(Other embodiments)
In the above-described embodiment, the refrigerant charging method and the refrigerant charging device of the present invention are applied to the additional charging of the refrigerant to the vehicle air conditioner. However, the present invention is not limited to this. The present invention may be applied to additional charging of a refrigerant in the entire refrigeration cycle using a refrigerant such as a water heater or a water heater. Further, the refrigerant is not limited to CO 2 , and may be applied to refrigerants such as ethylene, ethane, and nitrogen oxide as long as they have a low critical temperature.
[Brief description of the drawings]
FIG. 1A is a schematic diagram showing a configuration of a refrigerant charging device according to an embodiment of the present invention, FIG. 1B is an explanatory diagram of a volume variable portion when a refrigerant is changed from two phases to a single phase, (c) is an explanatory diagram of the volume variable section during refrigerant suction.
FIG. 2 is a schematic diagram showing a schematic configuration of a refrigeration cycle.
FIG. 3 is a flowchart showing an operation at the time of additional refrigerant charging in the refrigerant charging apparatus of the present invention.
[Explanation of symbols]
5 Variable volume section 5a Free piston 6 CO 2 cylinder (refrigerant storage means)
10 Compressor
11 Condenser (condenser)
12 Expansion valve (pressure reducing device)
13. Evaporator (evaporator)
14 Refrigerant pipe K Supply path Pn0 Refrigerant pressure R Refrigeration cycle Ta Outside air temperature Tc Critical temperature V0 Volume in variable volume section

Claims (5)

冷媒の圧縮機(10)、凝縮器(11)、減圧装置(12)、および蒸発器(13)を順に冷媒配管(14)で環状に接続した冷凍サイクル(R)と、
冷媒を貯蔵している冷媒貯蔵手段(6)と、
前記冷媒貯蔵手段(6)から前記冷凍サイクル(R)へ冷媒を供給する供給路(K)と、
前記供給路(K)の途中から分岐して設けられた容積可変部(5)とを設け、前記冷凍サイクル(R)に冷媒を追加充填する際の冷媒充填方法であり、
外気温度(Ta)が冷媒の臨界温度(Tc)よりも低い場合、前記冷凍サイクル(R)に前記容積可変部(5)の容積(V0)を加えて冷媒を適正量充填した時の冷媒圧力(Pn0)まで追加充填した後、前記容積可変部(5)の冷媒を前記冷凍サイクル(R)内に吸引させることを特徴とする冷凍サイクルの冷媒充填方法。
A refrigeration cycle (R) in which a refrigerant compressor (10), a condenser (11), a pressure reducing device (12), and an evaporator (13) are sequentially connected in an annular manner by a refrigerant pipe (14);
Refrigerant storage means (6) storing refrigerant;
A supply path (K) for supplying a refrigerant from the refrigerant storage means (6) to the refrigeration cycle (R);
A method for charging a refrigerant when a refrigerant is additionally charged into the refrigeration cycle (R) by providing a volume variable portion (5) branched from the middle of the supply path (K).
When the outside air temperature (Ta) is lower than the critical temperature (Tc) of the refrigerant, the refrigerant pressure at the time when the appropriate amount of refrigerant is charged by adding the volume (V0) of the variable volume section (5) to the refrigeration cycle (R). A refrigerant charging method for a refrigeration cycle, characterized in that the refrigerant in the variable volume section (5) is sucked into the refrigeration cycle (R) after additional charging to (Pn0).
冷媒の圧縮機(10)、凝縮器(11)、減圧装置(12)、および蒸発器(13)を順に冷媒配管(14)で環状に接続した冷凍サイクル(R)に冷媒を追加充填する際の冷媒充填装置であり、
冷媒を貯蔵している冷媒貯蔵手段(6)と、
前記冷媒貯蔵手段(6)から前記冷凍サイクル(R)へ冷媒を供給する供給路(K)と、
前記供給路(K)の途中から分岐して設けられた容積可変部(5)とを備え、
外気温度(Ta)が冷媒の臨界温度(Tc)よりも低い場合、前記冷凍サイクル(R)に前記容積可変部(5)の容積(V0)を加えて冷媒を適正量充填した時の冷媒圧力(Pn0)まで追加充填した後、前記容積可変部(5)の冷媒を前記冷凍サイクル(R)内に吸引させることを特徴とする冷凍サイクルの冷媒充填装置。
When the refrigerant is additionally charged into a refrigeration cycle (R) in which a refrigerant compressor (10), a condenser (11), a pressure reducing device (12), and an evaporator (13) are sequentially connected in an annular manner by a refrigerant pipe (14). Refrigerant charging device,
Refrigerant storage means (6) storing refrigerant;
A supply path (K) for supplying a refrigerant from the refrigerant storage means (6) to the refrigeration cycle (R);
A variable volume section (5) provided by branching from the middle of the supply path (K);
When the outside air temperature (Ta) is lower than the critical temperature (Tc) of the refrigerant, the refrigerant pressure at the time when the appropriate amount of refrigerant is charged by adding the volume (V0) of the variable volume section (5) to the refrigeration cycle (R). The refrigerant charging device for a refrigeration cycle, wherein the refrigerant in the variable volume section (5) is sucked into the refrigeration cycle (R) after additional charging to (Pn0).
前記容積可変部(5)の容積(V0)は、外気温度(Ta)が冷媒の臨界温度(Tc)よりも低くても前記容積可変部(5)の容積(V0)を加えることにより前記冷凍サイクル(R)内の冷媒がガスの単相状態になる容積(V0)としたことを特徴とする請求項2に記載の冷凍サイクルの冷媒充填装置。The volume (V0) of the variable volume section (5) is increased by adding the volume (V0) of the variable volume section (5) even when the outside air temperature (Ta) is lower than the critical temperature (Tc) of the refrigerant. The refrigerant charging device for a refrigeration cycle according to claim 2, wherein the refrigerant in the cycle (R) has a volume (V0) at which a gas is in a single-phase state. 前記容積可変部(5)をフリーピストン(5a)で構成したことを特徴とする請求項2または請求項3に記載の冷凍サイクルの冷媒充填装置。The refrigerant charging device for a refrigeration cycle according to claim 2 or 3, wherein the variable volume portion (5) is constituted by a free piston (5a). 前記冷媒はフロンガスよりも前記臨界温度(Tc)の低い冷媒であることを特徴とする請求項2または請求項3に記載の冷凍サイクルの冷媒充填装置。The refrigerant charging device for a refrigeration cycle according to claim 2, wherein the refrigerant is a refrigerant having a lower critical temperature (Tc) than Freon gas. 5.
JP2002356831A 2002-12-09 2002-12-09 Refrigerant filling method of refrigeration cycle and refrigerant filling device Pending JP2004190894A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006113069A1 (en) * 2005-04-19 2006-10-26 Snap-On Incorporated Refrigerant charging device and method using line having a control valve
EP2071257A1 (en) * 2007-12-11 2009-06-17 Linde Aktiengesellschaft Integrated filling and emptying system for air conditioners
JP2009243882A (en) * 2009-07-31 2009-10-22 Daikin Ind Ltd Refrigerant filling method in refrigeration device using carbon dioxide as refrigerant
CN109737532A (en) * 2019-02-18 2019-05-10 哈尔滨雷士丹电气科技有限公司 A kind of high energy saving communication base station Special flexible air-conditioning system

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006113069A1 (en) * 2005-04-19 2006-10-26 Snap-On Incorporated Refrigerant charging device and method using line having a control valve
US7310964B2 (en) 2005-04-19 2007-12-25 Snap-On Incorporated Refrigerant charging using line having a control valve
EP2071257A1 (en) * 2007-12-11 2009-06-17 Linde Aktiengesellschaft Integrated filling and emptying system for air conditioners
JP2009243882A (en) * 2009-07-31 2009-10-22 Daikin Ind Ltd Refrigerant filling method in refrigeration device using carbon dioxide as refrigerant
CN109737532A (en) * 2019-02-18 2019-05-10 哈尔滨雷士丹电气科技有限公司 A kind of high energy saving communication base station Special flexible air-conditioning system

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