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JP3720675B2 - Gas recovery method and gas recovery device - Google Patents
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JP3720675B2 - Gas recovery method and gas recovery device - Google Patents

Gas recovery method and gas recovery device Download PDF

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Publication number
JP3720675B2
JP3720675B2 JP2000130372A JP2000130372A JP3720675B2 JP 3720675 B2 JP3720675 B2 JP 3720675B2 JP 2000130372 A JP2000130372 A JP 2000130372A JP 2000130372 A JP2000130372 A JP 2000130372A JP 3720675 B2 JP3720675 B2 JP 3720675B2
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Prior art keywords
gas
gas recovery
reserve tank
recovered
valve
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JP2001312947A (en
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広幸 中江
修 山本
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Kansai Electric Power Co Inc
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Kansai Electric Power Co Inc
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Description

【0001】
【発明の属する技術分野】
本発明は、例えば、被充填ガスが充填された装置から被回収ガスを吸引して高圧ガスボンベに回収するガス回収方法及びガス回収装置に関する。
【0002】
【従来の技術】
被回収ガスが充填された装置として、例えば、変電設備などの高電圧装置は、内部に絶縁性に優れた6フッ化硫黄ガス(SF6)が高い圧力で封入されており、内部に配設された高電圧機械がショートすることを抑止している。
【0003】
この6フッ化硫黄ガスは、人体に悪影響を及ぼすガスではないが、近年の研究の結果、地球温暖化に影響のあるガスであることがわかった。そこで、地球温暖化を防止する環境対策から6フッ化硫黄ガスを回収してリサイクルすることを試みている。即ち、高電圧装置をメンテナンスする場合は、ガス回収装置によって高電圧装置内の6フッ化硫黄ガスを吸引して高圧ガスボンベに回収し、メンテナンス終了後に高圧ガスボンベから高電圧装置内に再び6フッ化硫黄ガスを充填している。
【0004】
ガス回収装置(A)は、図4に示すように、ガス回収装置本体52、ガス回収装置本体52に高電圧装置51を接続するホース54、及び、ガス回収装置本体52に高圧ガスボンベ53を接続するホース55を備えている。
【0005】
ホース54は、一端をガス回収装置本体52の吸引口56に接続し、他端を高電圧装置51のホース取付口51aに接続する。また、ホース55は、一端をガス回収装置本体52の吐出口57に接続し、他端を高圧ガスボンベ53のホース取付口53aに接続する。
【0006】
ガス回収装置本体52の内部には、吸引口56から吐出口57に至るガス回収通路58が形成されている。
【0007】
ガス回収通路58は、吸引口56側から順に、チェック用真空ポンプ61、吸引用真空ポンプ62、ガス溜り部63、コンプレッサ64、冷却器65及び減圧調整弁66を備えている。
【0008】
チェック用真空ポンプ61は、6フッ化硫黄ガスの回収を始める前に、ガス回収装置(A)の気密性をチェックするための真空ポンプである。
【0009】
吸引用真空ポンプ62は、高電圧装置51からガス回収通路58に6フッ化硫黄ガスを吸引するための真空ポンプである。ガス溜り部63は吸引した6フッ化硫黄ガスを一次的に留めてコンプレッサ64に安定した状態で導入するための部位である。コンプレッサ64は吸引した6フッ化硫黄ガスを圧縮して高圧ガスにしている。冷却器65は6フッ化硫黄ガスを冷却して液化させている。なお、高圧ガスボンベ53とガス回収装置本体52を接続しているホース55は、液化した6フッ化硫黄ガスが流通するので、耐圧性と断熱性を備えた耐圧断熱ホースを採用している。
【0010】
また、減圧調整弁66は、ガス回収通路58の冷却器65により吐出口57側と、吸引用真空ポンプ62より吸引口56側を繋ぐバイパス通路69に設けた弁であって、冷却器65より高圧ガスボンベ53側のガス回収通路58に溜まった高圧ガスを、吸引用真空ポンプ62より吸引口56側のガス回収通路58に導入して、冷却器65より高圧ガスボンベ53側のガス回収通路58を減圧するときに使用し、通常は閉じた状態で使用される。
【0011】
以下、このガス回収装置(A)におけるガスの回収手順を順番に説明する。
【0012】
I.ガス回収装置(A)の気密性が確保されていることを確認する。具体的には、高電圧装置51のホース取付口51aのバルブと、高圧ガスボンベ53のホース取付口53aのバルブを閉じた状態で、ホース54とホース55を、高電圧装置51及び高圧ガスボンベ53に取付け、チェック用真空ポンプ61を作動させてホース54、ガス回収装置本体52内部のガス回収通路58及びホース55を真空にし、ホース54、ガス回収通路58及びホース55に漏れる箇所が無いことを確認する。
【0013】
これは、ガス回収中に6フッ化硫黄ガスが大気中に漏れること、及び、大気がガス回収通路58内に混入することを防ぐためである。また、真空にして装置の気密性を確認するのは、気密性を確認するのと同時に、ガス回収を始める前に、ガス回収通路58内の空気を排出して、6フッ化硫黄ガスを回収するときに高圧ガスボンベ53内に不純物が混じらないようにするためである。
【0014】
II.次に、チェック用真空ポンプ61のホース取付口67のバルブを閉め、高電圧装置51のホース取付口51aと、高圧ガスボンベ53のホース取付口53aのバルブを開けて、高電圧装置51内の6フッ化硫黄ガスをガス回収通路58に導入し、ガス回収通路58のガス溜り部63に溜め、コンプレッサ64で圧縮し、更に、冷却器65で液化させて、ホース55を経て高圧ガスボンベ53に回収する。そして、高電圧装置51内の6フッ化硫黄ガスの気圧が低下すれば、吸引用真空ポンプ62を作動させて、高電圧装置51内が真空になるまで6フッ化硫黄ガスを回収する。
【0015】
III.高電圧装置51が真空になった状態で、高電圧装置51のホース取付口51aのバルブ、高電圧ガスボンベ53のホース取付口53aのバルブを閉めて6フッ化硫黄ガスの回収を終える。高電圧ガスボンベ53内の6フッ化硫黄ガスは、メンテナンス後に再び高電圧装置51内に供給されて再利用される。
【0016】
【発明が解決しようとする課題】
6フッ化硫黄ガスは、全て高圧ガスボンベ53に回収されることが望ましい。しかし、上記の手順によれば、大半の6フッ化硫黄ガスは高圧ガスボンベ53に回収されるが、図4において黒塗りして示すように、ホース55及びガス回収通路58に、高圧ガスボンベ53に回収しきれない6フッ化硫黄ガスが残留しており、この残留ガスは回収作業が終了した後に大気中に放出されている。
【0017】
特に、ガス回収通路58の冷却器65からホース55に残留した6フッ化硫黄ガスは液化しているので、常温で大気圧に気化した状態に換算するとその量はかなり多いと考えられる。
【0018】
そこで、本発明は、ガス回収装置に残留した残留ガスの再利用を図り、ガス回収装置のガス回収率を向上させることを目的とする。
【0019】
【課題を解決するための手段】
本発明に係るガス回収方法は、被回収ガスが充填された装置に接続される吸引口と、被回収ガスを回収する高圧ガスボンベに接続される吐出口と、吸引口と吐出口を連通し、真空ポンプとコンプレッサを備えたガス回収通路と、ガス回収通路にそれぞれバルブを介して接続した複数のリザーブタンクとを備えたガス回収装置を用いて、真空ポンプによりガス回収通路及びリザーブタンク内を真空状態にし、次いでリザーブタンクのバルブを閉めた状態で被回収ガスが充填された装置に接続し、真空ポンプ及びコンプレッサにより被回収ガスが充填された装置から被回収ガスを高圧ガスボンベに回収する被回収ガス回収動作後に、リザーブタンクのバルブを順番に開閉してガス回収通路に残留した被回収ガスをリザーブタンクに順次回収することを特徴とする。
【0020】
本発明に係るガス回収装置は、被回収ガスが充填された装置に接続される吸引口と、被回収ガスを回収する高圧ガスボンベに接続される吐出口と、吸引口と吐出口に連通し、真空ポンプとコンプレッサを備えたガス回収通路とを備えたガス回収装置において、ガス回収通路にそれぞれバルブを介して接続した複数のリザーブタンクとを備え、真空ポンプによりガス回収通路及びリザーブタンク内を真空状態にし、次いでリザーブタンクのバルブを閉めた状態で被回収ガスが充填された装置に接続し、真空ポンプ及びコンプレッサにより被回収ガスが充填された装置から被回収ガスを高圧ガスボンベに回収する被回収ガス回収動作後に、リザーブタンクのバルブを順番に開閉操作することにより、ガス回収通路に残留した被回収ガスをリザーブタンクに順次回収することを特徴とする。
【0021】
リザーブタンクの容積はガス回収通路の体積よりも大きいことが望ましい。
【0022】
また、ガス回収通路に設けた第1気圧計と、リザーブタンクに設けた第2気圧計と、リザーブタンクのバルブを開閉操作する制御装置とを備え、制御装置は、ガス回収通路に残留した被回収ガスを回収する残留ガス回収時において第1気圧計と第2気圧計の測定値が同じ値になったときに、残留ガスを貯留しているリザーブタンクのバルブを閉め、次に残留ガスを貯留するリザーブタンクのバルブを開くように、リザーブタンクのバルブを順番に開閉操作することを特徴とする。
【0023】
【発明の実施の形態】
以下、本発明に係るガス回収方法及びガス回収装置を6フッ化硫黄ガスの回収に適用した実施形態を図1及び図2に基づいて説明する。なお、図1及び図2において、図4に示したガス回収装置(A)と同様の部材には同一の符号を付す。
【0024】
このガス回収装置(B)は、図1に示すように、ガス回収通路58に4本のリザーブタンク(11,12,13,14)を取付けたものである。リザーブタンク(11,12,13,14)は、ガス回収通路58において、吸引用真空ポンプ62よりも吸引口56側に取付けてある。なお、図1と図2において、21はガス回収通路58の気圧を測定する気圧計、22はリザーブタンク(11,12,13,14)をガス回収通路58に接続するホース23の気圧を測定する気圧計である。また、このリザーブタンク(11,12,13,14)の容積はそれぞれ24lであり、ホース55とガス回収通路58の体積の合計は約20lである。
【0025】
このガス回収装置(B)の使用方法について説明する。
【0026】
このガス回収装置(B)は、まず、高電圧装置51のホース取付口51aと高圧ガスボンベ53のホース取付口53aのバルブをそれぞれ閉めた状態で、ホース54と55を高電圧装置51及び高圧ガスボンベ53に接続し、かつ、リザーブタンク(11,12,13,14)のガス取込口(15,16,17,18)のバルブを開けた状態で、チェック用真空ポンプ61を作動させる。これにより、ホース54、ガス回収通路58及びホース55の気密性を確保すると共に、ホース54、ホース55、ガス回収通路58及びリザーブタンク(11,12,13,14)を真空にして、ガスを回収したときに高圧ガスボンベ53内に不純物が混じらないようにする。
【0027】
次に、リザーブタンク(11,12,13,14)のガス取込口(15,16,17,18)のバルブとチェック用真空ポンプ61のホース取付口67のバルブを閉め、高電圧装置51のホース取付口51aのバルブと高圧ガスボンベ53のホース取付口53aのバルブを開けて、高電圧装置51内の6フッ化硫黄ガスを、ホース54からガス回収通路58に導入し、コンプレッサ64で圧縮し、更に、冷却器65で液化して、ホース55を通して高圧ガスボンベ53に回収する。そして、高電圧装置51内の6フッ化硫黄ガスの気圧が低下すれば、吸引用真空ポンプ62を作動させて、高電圧装置51内が真空になるまで6フッ化硫黄ガスを回収する。
【0028】
高電圧装置51が真空になった状態で、高電圧装置51のホース取付口51aのバルブと、高圧ガスボンベ53のホース取付口53aのバルブを閉めてガスの回収を終える。なお、ホース54は高電圧装置51と同様真空になっているので、図2に示すように、ガスの回収が終わったときに、ガス回収装置本体52の吸引口56のバルブを閉めて、ホース54を外しておくと良い。
【0029】
次に、以下の手順でホース55及びガス回収通路58に残留した残留ガスをリザーブタンク(11,12,13,14)に暫定的に貯留する。
【0030】
まず、残留ガスの貯留時の状態を示す図2において、減圧調整弁66を開いて冷却器65から吐出口57側のガス回収通路58及びホース55に溜まった高圧ガスを、真空になっている吸引用真空ポンプ62から吸引口56側のガス回収通路58に逃して、冷却器65から吐出口57側のガス回収通路58及びホース55を減圧する。これにより、ガス回収通路58内での残留ガスの流通が可能となる。
【0031】
次に、1本目のリザーブタンク11のガス取込口15のバルブを開ける。リザーブタンク11は、ガスを回収する前に真空にしてあるので、ガス取込口15のバルブを開けることにより、リザーブタンク11とガス回収通路58の気圧が均一になるまで残留ガスを吸引することができる。なお、所要の時間が経てば気圧は均一になり、気圧計21と22の値が同じ値になることで、均一になったことを確認することができる。
【0032】
これにより、リザーブタンク11と(ホース55+ガス回収通路58)の体積比により、残留ガスのうち約54.4%(24/44)の残留ガスを1本目のリザーブタンク11に暫定的に貯留することができる。また、この段階で、ガス回収通路58に残留したガスは、残留ガス回収前に比べて約45.6%(20/44)となる。
【0033】
次に、1本目のリザーブタンク11のガス取込口15のバルブを閉めて、2本目のリザーブタンク12のガス取込口16のバルブを開ける。2本目のリザーブタンク12は、1本目のリザーブタンク11と同様、真空であるからガス取込口16のバルブを開けることにより、リザーブタンク12とガス回収通路58の気圧が均一になるまで残留ガスを吸引することができる。これにより、リザーブタンク12と(ホース55+ガス回収通路58)の体積比により、全残留ガスのうち24.8%{(20/44)×(24/44)}の残留ガスを2本目のリザーブタンク12に暫定的に貯留することができる。
【0034】
以下、同様に、3本目のリザーブタンク13と4本目のリザーブタンク14のガス取込口17と18のバルブを順番に開閉して残留ガスを吸引する。
【0035】
これにより、3本目のリザーブタンク13には、全残留ガスのうち11.3%{(20/44)2×(24/44)}の残留ガスを貯留することができ、4本目のリザーブタンク14には、全残留ガスのうち5.1%{(20/44)3×(24/44)}の残留ガスを貯留することができる。この結果、最終的にガス回収通路58に残留する6フッ化硫黄ガスは、全残留ガスの約4.4%となる。
【0036】
即ち、このガス回収装置(B)によると、図3に示すように、1本目〜4本目のリザーブタンク(11,12,13,14)のガス取込口(15,16,17,18)のバルブを順番に開閉することで、従来回収しきれずに、大気中に放出されていた残留ガスを各リザーブタンク(11,12,13,14)に段階的に吸引することができ、残留ガスの約96%を貯留することが可能となる。
【0037】
次に、リザーブタンク(11,12,13,14)に貯留した6フッ化硫黄ガスの再利用について説明する。
【0038】
リザーブタンク(11,12,13,14)に貯留した6フッ化硫黄ガスは、再び高電圧装置51から6フッ化硫黄ガスを抜き取る作業をするまでは、リザーブタンク(11,12,13,14)内に保管する。
【0039】
そして、再び高電圧装置51から6フッ化硫黄ガスを抜き取る作業をするとき、リザーブタンク(11,12,13,14)のガス取込口(15,16,17,18)のバルブを閉じたままで、上述のように、ホース54とホース55を接続してチェック用真空ポンプ61を作動させ、ホース54、ガス回収通路58及びホース55を真空にする。
【0040】
そして、リザーブタンク(11,12,13,14)のガス取込口(15,16,17,18)のバルブを開けて6フッ化硫黄ガスの回収を開始することで、リザーブタンク(11,12,13,14)内の6フッ化硫黄ガスを高圧ガスボンベ53に回収すると共に、リザーブタンク(11,12,13,14)を真空にすることができる。そして、ガス回収が終了したとき、リザーブタンク(11,12,13,14)のガス取込口(15,16,17,18)のバルブを閉めて各リザーブタンク(11,12,13,14)を真空にする。
【0041】
そして、ガス回収後、再びリザーブタンク(11,12,13,14)のガス取込口(15,16,17,18)のバルブを順番に開閉することによって、ガス回収通路58に残留した残留ガスをリザーブタンク(11,12,13,14)内に吸引して貯留することができる。
【0042】
これにより、リザーブタンク(11,12,13,14)に吸引した6フッ化硫黄ガスを高圧ガスタンク53に回収して、メンテナンス後に高電圧装置51内に供給して再利用を図ることができる。
【0043】
以上、本発明の一実施形態に係るガス回収装置について説明したが、本発明のガス回収装置は上記実施形態に限定されない。
【0044】
例えば、リザーブタンクの本数は4本に限定されない。リザーブタンクの本数を多くすれば、残留ガスの貯留率はより向上する。また、リザーブタンクがガス回収通路の体積に対して十分に大きな容積を備えていれば、リザーブタンクは1本でも良い。また、各リザーブタンクの容積や、残留ガス貯留時のリザーブタンクの取込口のバルブを開放する順番は任意に変更することができる。
【0045】
また、上記した残留ガスの回収において、ガス回収通路58の気圧を測定する気圧計21と、リザーブタンク(11,12,13,14)の気圧を測定する気圧計22の値が同じ値になったときに、リザーブタンク(11,12,13,14)のガス取込口(15,16,17,18)のバルブを上述した順番で自動的に開閉操作するように構成した制御装置を設けて残留ガスの回収を自動化しても良い。
【0046】
【発明の効果】
本発明に係るガス回収装置は、真空ポンプよりも吸引口側のガス回収通路に、ホース並びにガス回収通路内の残留ガスを暫定的に貯留するためのリザーブタンクを配設したので、ガス回収通路に残留したガスをリザーブタンクに吸引して再利用を図ることができ、ガスの回収率の飛躍的に向上させることができる。
【0047】
前記リザーブタンクを複数備え、前記残留ガスを貯留するときに、各リザーブタンクを順番に開閉して貯留するので、各リザーブタンクに残留ガスを段階的に吸引することができ残留ガスの貯留率が向上する。
【0048】
前記リザーブタンクの容積は、前記ガス回収通路の体積よりも大きくしたので、リザーブタンクに効率よく残留ガスを吸引することができる。
【0049】
また、 また、ガス回収通路に設けた第1気圧計と、リザーブタンクに設けた第2気圧計と、リザーブタンクのバルブを開閉操作する制御装置とを備え、制御装置を、ガス回収通路に残留した被回収ガスを回収する残留ガス回収時において第1気圧計と第2気圧計の測定値が同じ値になったときに、残留ガスを貯留しているリザーブタンクのバルブを閉め、次に残留ガスを貯留するリザーブタンクのバルブを開くように、リザーブタンクのバルブを順番に開閉操作するように構成したので、リザーブタンクへの残留ガスの吸引作業を自動化することができる。
【図面の簡単な説明】
【図1】 本発明の一実施形態に係るガス回収装置の概略を示す図。
【図2】 本発明の一実施形態に係るガス回収装置の残留ガス吸引時の状態を示す図。
【図3】 本発明の一実施形態に係るガス回収装置の残留ガスの貯留率を示す図。
【図4】 ガス回収装置の概略を示す図。
【符号の説明】
11〜14 リザーブタンク
51 高電圧装置
51a 高電圧装置側のホース取付口
52 ガス回収装置
53 高圧ガスボンベ
53a 高圧ガスボンベ側のホース取付口
54,55 ホース
56 吸引口
57 吐出口
58 ガス回収通路
61 チェック用真空ポンプ
62 吸引用真空ポンプ
63 ガス溜り部
64 コンプレッサ
65 冷却器
66 減圧調整弁
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a gas recovery method and a gas recovery apparatus that, for example, sucks a gas to be recovered from an apparatus filled with the gas to be charged and recovers the gas in a high-pressure gas cylinder.
[0002]
[Prior art]
As an apparatus filled with the gas to be recovered, for example, a high voltage apparatus such as a substation equipment is filled with sulfur hexafluoride gas (SF6) excellent in insulation inside at a high pressure and disposed inside. High voltage machines are prevented from short-circuiting.
[0003]
This sulfur hexafluoride gas is not a gas that adversely affects the human body, but as a result of recent research, it has been found that it is a gas that affects global warming. Therefore, we are trying to collect and recycle sulfur hexafluoride gas from environmental measures to prevent global warming. That is, when maintaining the high voltage device, the gas recovery device sucks the sulfur hexafluoride gas in the high voltage device and collects it in the high pressure gas cylinder. It is filled with sulfur gas.
[0004]
As shown in FIG. 4, the gas recovery apparatus (A) includes a gas recovery apparatus main body 52, a hose 54 that connects the high voltage apparatus 51 to the gas recovery apparatus main body 52, and a high-pressure gas cylinder 53 connected to the gas recovery apparatus main body 52. A hose 55 is provided.
[0005]
One end of the hose 54 is connected to the suction port 56 of the gas recovery device main body 52, and the other end is connected to the hose attachment port 51 a of the high voltage device 51. The hose 55 has one end connected to the discharge port 57 of the gas recovery apparatus main body 52 and the other end connected to the hose attachment port 53 a of the high-pressure gas cylinder 53.
[0006]
A gas recovery passage 58 extending from the suction port 56 to the discharge port 57 is formed inside the gas recovery device main body 52.
[0007]
The gas recovery passage 58 includes a check vacuum pump 61, a suction vacuum pump 62, a gas reservoir 63, a compressor 64, a cooler 65, and a pressure reducing adjustment valve 66 in order from the suction port 56 side.
[0008]
The check vacuum pump 61 is a vacuum pump for checking the gas tightness of the gas recovery device (A) before starting recovery of sulfur hexafluoride gas.
[0009]
The suction vacuum pump 62 is a vacuum pump for sucking sulfur hexafluoride gas from the high voltage device 51 into the gas recovery passage 58. The gas reservoir 63 is a part for temporarily holding the sucked sulfur hexafluoride gas and introducing it into the compressor 64 in a stable state. The compressor 64 compresses the sucked sulfur hexafluoride gas into a high-pressure gas. The cooler 65 cools and liquefies sulfur hexafluoride gas. In addition, since the liquefied sulfur hexafluoride gas flows through the hose 55 connecting the high-pressure gas cylinder 53 and the gas recovery apparatus main body 52, a pressure-resistant and heat-insulating hose having pressure resistance and heat insulation is adopted.
[0010]
The pressure reducing adjustment valve 66 is a valve provided in a bypass passage 69 that connects the discharge port 57 side to the suction port 56 side from the suction vacuum pump 62 by the cooler 65 of the gas recovery passage 58. The high-pressure gas accumulated in the gas recovery passage 58 on the high-pressure gas cylinder 53 side is introduced into the gas recovery passage 58 on the suction port 56 side from the suction vacuum pump 62, and the gas recovery passage 58 on the high-pressure gas cylinder 53 side is introduced from the cooler 65. Used when depressurizing, usually in a closed state.
[0011]
Hereinafter, the gas recovery procedure in the gas recovery apparatus (A) will be described in order.
[0012]
I. It is confirmed that the gas tightness of the gas recovery device (A) is secured. Specifically, the hose 54 and the hose 55 are connected to the high voltage device 51 and the high pressure gas cylinder 53 with the valve of the hose attachment port 51 a of the high voltage device 51 and the hose attachment port 53 a of the high pressure gas cylinder 53 closed. Attach and check vacuum pump 61 to activate hose 54, gas recovery passage 58 and hose 55 inside gas recovery device main body 52, and confirm that there are no leak points in hose 54, gas recovery passage 58 and hose 55. To do.
[0013]
This is to prevent sulfur hexafluoride gas from leaking into the atmosphere during gas recovery and mixing the atmosphere into the gas recovery passage 58. In addition, the airtightness of the device is confirmed by making a vacuum, and at the same time as confirming the airtightness, before starting the gas recovery, the air in the gas recovery passage 58 is discharged to recover the sulfur hexafluoride gas. This is to prevent impurities from being mixed in the high-pressure gas cylinder 53.
[0014]
II. Next, the valve of the hose attachment port 67 of the vacuum pump 61 for check is closed, and the valves of the hose attachment port 51a of the high voltage device 51 and the hose attachment port 53a of the high pressure gas cylinder 53 are opened. Sulfur fluoride gas is introduced into the gas recovery passage 58, stored in the gas reservoir 63 of the gas recovery passage 58, compressed by the compressor 64, further liquefied by the cooler 65, and recovered by the high pressure gas cylinder 53 through the hose 55. To do. When the atmospheric pressure of the sulfur hexafluoride gas in the high voltage device 51 decreases, the suction vacuum pump 62 is operated to recover the sulfur hexafluoride gas until the inside of the high voltage device 51 becomes vacuum.
[0015]
III. With the high-voltage device 51 in a vacuum state, the valve of the hose attachment port 51a of the high-voltage device 51 and the valve of the hose attachment port 53a of the high-voltage gas cylinder 53 are closed, and the recovery of sulfur hexafluoride gas is completed. The sulfur hexafluoride gas in the high voltage gas cylinder 53 is supplied again into the high voltage device 51 and reused after maintenance.
[0016]
[Problems to be solved by the invention]
It is desirable that all the sulfur hexafluoride gas is recovered in the high pressure gas cylinder 53. However, according to the above procedure, most of the sulfur hexafluoride gas is recovered in the high-pressure gas cylinder 53, but as shown in black in FIG. 4, the hose 55 and the gas recovery passage 58 are connected to the high-pressure gas cylinder 53. There remains residual sulfur hexafluoride gas that cannot be recovered, and this residual gas is released into the atmosphere after the recovery operation is completed.
[0017]
In particular, since the sulfur hexafluoride gas remaining in the hose 55 from the cooler 65 of the gas recovery passage 58 is liquefied, the amount is considered to be considerably large when converted to a state where it is vaporized to atmospheric pressure at room temperature.
[0018]
Therefore, an object of the present invention is to reuse the residual gas remaining in the gas recovery device and improve the gas recovery rate of the gas recovery device.
[0019]
[Means for Solving the Problems]
The gas recovery method according to the present invention includes a suction port connected to an apparatus filled with a gas to be recovered, a discharge port connected to a high-pressure gas cylinder that recovers the gas to be recovered, and a suction port and the discharge port. Using a gas recovery device that includes a gas recovery passage including a vacuum pump and a compressor, and a plurality of reserve tanks connected to the gas recovery passage through valves, the vacuum recovery pump and the inside of the reserve tank are evacuated. Connected to the device filled with the gas to be collected with the valve of the reserve tank closed, and then collected the gas to be collected from the device filled with the gas to be collected by the vacuum pump and compressor into the high pressure gas cylinder After the gas recovery operation, the reserve tank valves are sequentially opened and closed to sequentially recover the gas to be recovered remaining in the gas recovery passage to the reserve tank. The features.
[0020]
The gas recovery device according to the present invention communicates with a suction port connected to a device filled with a gas to be recovered, a discharge port connected to a high-pressure gas cylinder for recovering the gas to be recovered, a suction port and a discharge port, A gas recovery apparatus including a vacuum pump and a gas recovery passage equipped with a compressor includes a plurality of reserve tanks each connected to the gas recovery passage through a valve, and the vacuum recovery pump and the inside of the reserve tank are evacuated. Connected to the device filled with the gas to be collected with the valve of the reserve tank closed, and then collected the gas to be collected from the device filled with the gas to be collected by the vacuum pump and compressor into the high pressure gas cylinder After the gas recovery operation, the gas to be recovered remaining in the gas recovery passage is reserved by opening and closing the valves of the reserve tank in order. Wherein the sequentially recovered link.
[0021]
The volume of the reserve tank is preferably larger than the volume of the gas recovery passage.
[0022]
In addition, a first barometer provided in the gas recovery passage, a second barometer provided in the reserve tank, and a control device that opens and closes the valve of the reserve tank are provided. When recovering residual gas, when the measured values of the first barometer and second barometer become the same value, the valve of the reserve tank storing the residual gas is closed, and then the residual gas is The reserve tank valve is sequentially opened and closed so that the reserve tank valve to be stored is opened .
[0023]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, an embodiment in which a gas recovery method and a gas recovery device according to the present invention are applied to recovery of sulfur hexafluoride gas will be described with reference to FIGS. 1 and 2. In FIGS. 1 and 2, the same members as those in the gas recovery apparatus (A) shown in FIG.
[0024]
As shown in FIG. 1, this gas recovery device (B) has four reserve tanks (11, 12, 13, 14) attached to a gas recovery passage 58. The reserve tanks (11, 12, 13, 14) are attached to the suction port 56 side of the suction vacuum pump 62 in the gas recovery passage 58. In FIGS. 1 and 2, 21 is a barometer for measuring the pressure in the gas recovery passage 58, and 22 is the pressure in the hose 23 for connecting the reserve tank (11, 12, 13, 14) to the gas recovery passage 58. It is a barometer. The reserve tanks (11, 12, 13, 14) each have a volume of 24 l, and the total volume of the hose 55 and the gas recovery passage 58 is approximately 20 l.
[0025]
A method of using this gas recovery device (B) will be described.
[0026]
First, the gas recovery device (B) is configured such that the hoses 54 and 55 are connected to the high voltage device 51 and the high pressure gas cylinder with the valves of the hose attachment port 51a of the high voltage device 51 and the hose attachment port 53a of the high pressure gas cylinder 53 closed. 53 and the check vacuum pump 61 is operated with the valves of the gas intake ports (15, 16, 17, 18) of the reserve tanks (11, 12, 13, 14) opened. As a result, the airtightness of the hose 54, the gas recovery passage 58 and the hose 55 is ensured, and the hose 54, the hose 55, the gas recovery passage 58 and the reserve tanks (11, 12, 13, 14) are evacuated to supply gas. Impurities are prevented from being mixed in the high-pressure gas cylinder 53 when recovered.
[0027]
Next, the valve of the gas intake port (15, 16, 17, 18) of the reserve tank (11, 12, 13, 14) and the valve of the hose attachment port 67 of the check vacuum pump 61 are closed, and the high voltage device 51 is closed. The valve of the hose attachment port 51a and the valve of the hose attachment port 53a of the high pressure gas cylinder 53 are opened, and the sulfur hexafluoride gas in the high voltage device 51 is introduced from the hose 54 into the gas recovery passage 58 and compressed by the compressor 64. Further, it is liquefied by the cooler 65 and collected in the high-pressure gas cylinder 53 through the hose 55. When the atmospheric pressure of the sulfur hexafluoride gas in the high voltage device 51 decreases, the suction vacuum pump 62 is operated to recover the sulfur hexafluoride gas until the inside of the high voltage device 51 becomes vacuum.
[0028]
With the high-voltage device 51 in a vacuum state, the valve of the hose attachment port 51a of the high-voltage device 51 and the valve of the hose attachment port 53a of the high-pressure gas cylinder 53 are closed to finish the gas recovery. Since the hose 54 is in a vacuum similar to the high voltage device 51, as shown in FIG. 2, when the gas recovery is finished, the valve of the suction port 56 of the gas recovery device main body 52 is closed, and the hose 54 is closed. 54 should be removed.
[0029]
Next, the residual gas remaining in the hose 55 and the gas recovery passage 58 is provisionally stored in the reserve tank (11, 12, 13, 14) by the following procedure.
[0030]
First, in FIG. 2 showing the state when the residual gas is stored, the decompression regulating valve 66 is opened, and the high pressure gas accumulated in the gas recovery passage 58 and the hose 55 on the discharge port 57 side from the cooler 65 is evacuated. The gas is discharged from the suction vacuum pump 62 to the gas recovery passage 58 on the suction port 56 side, and the gas recovery passage 58 and the hose 55 on the discharge port 57 side are decompressed from the cooler 65. Thereby, the residual gas can be circulated in the gas recovery passage 58.
[0031]
Next, the valve of the gas intake port 15 of the first reserve tank 11 is opened. Since the reserve tank 11 is evacuated before the gas is collected, the residual gas is sucked until the pressure in the reserve tank 11 and the gas collection passage 58 becomes uniform by opening the valve of the gas intake port 15. Can do. It should be noted that the barometric pressure becomes uniform when the required time has elapsed, and it can be confirmed that the barometers 21 and 22 have the same value, thereby making it uniform.
[0032]
Thus, approximately 54.4% (24/44) of the residual gas is temporarily stored in the first reserve tank 11 according to the volume ratio of the reserve tank 11 and the (hose 55 + gas recovery passage 58). be able to. Further, at this stage, the gas remaining in the gas recovery passage 58 is about 45.6% (20/44) compared with that before the residual gas recovery.
[0033]
Next, the valve of the gas intake port 15 of the first reserve tank 11 is closed, and the valve of the gas intake port 16 of the second reserve tank 12 is opened. Since the second reserve tank 12 is vacuum like the first reserve tank 11, residual gas is maintained until the pressure in the reserve tank 12 and the gas recovery passage 58 becomes uniform by opening the valve of the gas intake port 16. Can be aspirated. As a result, 24.8% {(20/44) × (24/44)} of the residual gas in the total volume of the residual tank 12 by the volume ratio of the reserve tank 12 and (the hose 55 + the gas recovery passage 58) It can be temporarily stored in the tank 12.
[0034]
Thereafter, similarly, the valves of the gas intake ports 17 and 18 of the third reserve tank 13 and the fourth reserve tank 14 are sequentially opened and closed to suck the residual gas.
[0035]
Accordingly, 11.3% {(20/44) 2 × (24/44)} of the residual gas can be stored in the third reserve tank 13, and the fourth reserve tank can be stored. 14, the remaining gas of 5.1% {(20/44) 3 × (24/44)} among the total residual gas can be stored. As a result, the sulfur hexafluoride gas finally remaining in the gas recovery passage 58 is about 4.4% of the total residual gas.
[0036]
That is, according to this gas recovery device (B), as shown in FIG. 3, the gas intake ports (15, 16, 17, 18) of the first to fourth reserve tanks (11, 12, 13, 14). By opening and closing the valves in order, the residual gas that has not been recovered in the past and has been released into the atmosphere can be sucked into the respective reserve tanks (11, 12, 13, 14) step by step. It is possible to store about 96% of the total.
[0037]
Next, the reuse of sulfur hexafluoride gas stored in the reserve tanks (11, 12, 13, 14) will be described.
[0038]
Until the sulfur hexafluoride gas stored in the reserve tank (11, 12, 13, 14) is again extracted from the high voltage device 51, the reserve tank (11, 12, 13, 14) is used. ) Store in.
[0039]
When the sulfur hexafluoride gas is extracted again from the high voltage device 51, the valves of the gas intake ports (15, 16, 17, 18) of the reserve tanks (11, 12, 13, 14) are closed. As described above, the hose 54 and the hose 55 are connected to operate the check vacuum pump 61, and the hose 54, the gas recovery passage 58 and the hose 55 are evacuated.
[0040]
Then, by opening the valve of the gas intake port (15, 16, 17, 18) of the reserve tank (11, 12, 13, 14) and starting the collection of sulfur hexafluoride gas, the reserve tank (11, 12, 13, 14), the sulfur hexafluoride gas in the high-pressure gas cylinder 53 can be recovered, and the reserve tanks (11, 12, 13, 14) can be evacuated. When the gas recovery is completed, the valves of the gas intake ports (15, 16, 17, 18) of the reserve tanks (11, 12, 13, 14) are closed, and the reserve tanks (11, 12, 13, 14) are closed. ) To a vacuum.
[0041]
After the gas recovery, the valve remaining in the gas intake port (15, 16, 17, 18) of the reserve tank (11, 12, 13, 14) is opened and closed again in order, thereby remaining in the gas recovery passage 58. The gas can be sucked and stored in the reserve tanks (11, 12, 13, 14).
[0042]
Thereby, the sulfur hexafluoride gas sucked into the reserve tanks (11, 12, 13, 14) can be collected in the high-pressure gas tank 53 and supplied into the high-voltage device 51 after maintenance to be reused.
[0043]
The gas recovery apparatus according to the embodiment of the present invention has been described above, but the gas recovery apparatus of the present invention is not limited to the above embodiment.
[0044]
For example, the number of reserve tanks is not limited to four. If the number of reserve tanks is increased, the residual gas storage rate is further improved. Further, if the reserve tank has a sufficiently large volume with respect to the volume of the gas recovery passage, the number of reserve tanks may be one. Further, the volume of each reserve tank and the order in which the valves of the intake ports of the reserve tank when the residual gas is stored can be arbitrarily changed.
[0045]
In the above-described residual gas recovery, the barometer 21 that measures the pressure in the gas recovery passage 58 and the barometer 22 that measures the pressure in the reserve tank (11, 12, 13, 14) have the same value. Provided with a control device configured to automatically open and close the valves of the gas intake ports (15, 16, 17, 18) of the reserve tank (11, 12, 13, 14) in the order described above. The recovery of residual gas may be automated.
[0046]
【The invention's effect】
In the gas recovery apparatus according to the present invention, the hose and the reserve tank for temporarily storing the residual gas in the gas recovery passage are disposed in the gas recovery passage closer to the suction port than the vacuum pump. The remaining gas can be sucked into the reserve tank and reused, and the gas recovery rate can be greatly improved.
[0047]
A plurality of the reserve tanks are provided, and when storing the residual gas, the reserve tanks are opened and closed in order and stored, so that the residual gas can be sucked into each reserve tank in stages and the residual gas storage rate is increased. improves.
[0048]
Since the volume of the reserve tank is larger than the volume of the gas recovery passage, the residual gas can be efficiently sucked into the reserve tank.
[0049]
In addition, a first barometer provided in the gas recovery passage, a second barometer provided in the reserve tank, and a control device that opens and closes the valve of the reserve tank are provided, and the control device remains in the gas recovery passage. When the measured values of the first barometer and the second barometer become the same during the residual gas recovery to recover the recovered gas, the valve of the reserve tank storing the residual gas is closed, and then the residual gas Since the reserve tank valve is sequentially opened and closed so as to open the reserve tank valve for storing the gas, the work of sucking the residual gas into the reserve tank can be automated.
[Brief description of the drawings]
FIG. 1 is a diagram schematically showing a gas recovery apparatus according to an embodiment of the present invention.
FIG. 2 is a view showing a state when the residual gas is sucked by the gas recovery apparatus according to the embodiment of the present invention.
FIG. 3 is a view showing a residual gas storage rate of the gas recovery apparatus according to the embodiment of the present invention.
FIG. 4 is a diagram showing an outline of a gas recovery device.
[Explanation of symbols]
11-14 Reserve tank 51 High voltage device
51a Hose attachment port 52 on the high voltage device side Gas recovery device 53 High pressure gas cylinder
53a Hose attachment port 54, 55 hose on the high pressure gas cylinder side
56 suction port
57 outlet
58 Gas recovery passage 61 Check vacuum pump 62 Suction vacuum pump 63 Gas reservoir 64 Compressor 65 Cooler 66 Depressurization regulating valve

Claims (4)

被回収ガスが充填された装置に接続される吸引口と、A suction port connected to an apparatus filled with the gas to be collected;
被回収ガスを回収する高圧ガスボンベに接続される吐出口と、A discharge port connected to a high-pressure gas cylinder for collecting the gas to be collected;
前記吸引口と吐出口を連通し、真空ポンプとコンプレッサを備えたガス回収通路と、A gas recovery passage that communicates the suction port and the discharge port and includes a vacuum pump and a compressor;
前記ガス回収通路にそれぞれバルブを介して接続した複数のリザーブタンクとを備えたガス回収装置を用いて、Using a gas recovery apparatus comprising a plurality of reserve tanks connected to the gas recovery passages via valves,
前記真空ポンプによりガス回収通路及びリザーブタンク内を真空状態にし、次いでリザーブタンクのバルブを閉めた状態で前記被回収ガスが充填された装置に接続し、前記真空ポンプ及びコンプレッサにより被回収ガスが充填された装置から被回収ガスを高圧ガスボンベに回収する被回収ガス回収動作後に、前記リザーブタンクのバルブを順番に開閉してガス回収通路に残留した被回収ガスを前記リザーブタンクに順次回収することを特徴とするガス回収方法。The gas recovery passageway and the reserve tank are evacuated by the vacuum pump, and then connected to the device filled with the gas to be recovered with the reserve tank valve closed, and the gas to be recovered is filled by the vacuum pump and the compressor. After the gas recovery operation for recovering the gas to be recovered from the installed device to the high pressure gas cylinder, the gas to be recovered remaining in the gas recovery passage is sequentially recovered in the reserve tank by sequentially opening and closing the valves of the reserve tank. Characterized gas recovery method.
被回収ガスが充填された装置に接続される吸引口と、A suction port connected to an apparatus filled with the gas to be collected;
被回収ガスを回収する高圧ガスボンベに接続される吐出口と、A discharge port connected to a high-pressure gas cylinder for collecting the gas to be collected;
前記吸引口と吐出口に連通し、真空ポンプとコンプレッサを備えたガス回収通路とを備えたガス回収装置において、In the gas recovery apparatus provided with a gas recovery passage provided with a vacuum pump and a compressor in communication with the suction port and the discharge port,
前記ガス回収通路にそれぞれバルブを介して接続した複数のリザーブタンクとを備え、A plurality of reserve tanks connected to the gas recovery passages via valves,
前記真空ポンプによりガス回収通路及びリザーブタンク内を真空状態にし、次いでリザーブタンクのバルブを閉めた状態で前記被回収ガスが充填された装置に接続し、前記真空ポンプ及びコンプレッサにより被回収ガスが充填された装置から被回収ガスを高圧ガスボンベに回収する被回収ガス回収動作後に、リザーブタンクのバルブを順番に開閉操作することにより、ガス回収通路に残留した被回収ガスを前記リザーブタンクに順次回収することを特徴とするガス回収装置。The gas recovery passageway and the reserve tank are evacuated by the vacuum pump, and then connected to the device filled with the gas to be recovered with the reserve tank valve closed, and the gas to be recovered is filled by the vacuum pump and the compressor. The recovered gas remaining in the gas recovery passage is sequentially recovered in the reserve tank by sequentially opening and closing the valve of the reserve tank after the recovered gas recovery operation for recovering the recovered gas from the apparatus to the high-pressure gas cylinder. A gas recovery apparatus characterized by that.
前記リザーブタンクの容積が、前記ガス回収通路の体積よりも大きいことを特徴とする請求項2に記載のガス回収装置。The gas recovery apparatus according to claim 2 , wherein a volume of the reserve tank is larger than a volume of the gas recovery passage. 前記ガス回収通路に設けた第1気圧計と、前記リザーブタンクに設けた第2気圧計と、前記リザーブタンクのバルブを開閉操作する制御装置とを備え、前記制御装置は、前記ガス回収通路に残留した被回収ガスを回収する残留ガス回収時において第1気圧計と第2気圧計の測定値が同じ値になったときに、前記残留ガスを貯留しているリザーブタンクのバルブを閉め、次に残留ガスを貯留するリザーブタンクのバルブを開くように、前記リザーブタンクのバルブを順番に開閉操作することを特徴とする請求項2に記載のガス回収装置A first barometer provided in the gas recovery passage; a second barometer provided in the reserve tank; and a control device that opens and closes a valve of the reserve tank; and the control device is provided in the gas recovery passage. When the measurement value of the first barometer and the second barometer becomes the same value during the recovery of the residual gas to recover the residual gas to be recovered, the valve of the reserve tank storing the residual gas is closed, and the next The gas recovery apparatus according to claim 2 , wherein the valve of the reserve tank is sequentially opened and closed so that the valve of the reserve tank that stores residual gas is opened.
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