JP4326715B2 - Gas filling apparatus and method - Google Patents

Gas filling apparatus and method Download PDF

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Publication number
JP4326715B2
JP4326715B2 JP2001094973A JP2001094973A JP4326715B2 JP 4326715 B2 JP4326715 B2 JP 4326715B2 JP 2001094973 A JP2001094973 A JP 2001094973A JP 2001094973 A JP2001094973 A JP 2001094973A JP 4326715 B2 JP4326715 B2 JP 4326715B2
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gas
filling
liquefied gas
tank
low
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JP2002295796A (en
JP2002295796A5 (en
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美智春 松田
篤 小林
勉 野木
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Taiyo Nippon Sanso Corp
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Taiyo Nippon Sanso Corp
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Description

【0001】
【発明の属する技術分野】
本発明は、ガス充填装置及び方法に関し、詳しくは、液化ガス貯槽内に貯留した液化ガスを、昇圧ポンプを使用せずに昇圧してガス容器に充填する装置及び方法に関する。
【0002】
【従来の技術】
図4は、従来のガス充填装置の一例を示す系統図である。このガス充填装置は、ガス充填部11に供給するガスを液状で貯留する液化ガス貯槽12と、該液化ガス貯槽12から導出した低温液化ガスを所要圧力に圧縮する往復動式の液化ガスポンプ13と、該液化ガスポンプ13で圧縮された低温液化ガスを大気空気等の熱源で蒸発させる蒸発器14とを有しており、該蒸発器14で蒸発したガスを前記ガス充填部11に供給して各ガス容器15,16内に所定圧力で充填するように形成されている。
【0003】
なお、ガス充填部11に供給するガスを所要圧力に昇圧する手段として、前記液化ガスポンプ13に代えて、蒸発後のガスを昇圧するガス圧縮機を使用することもできるが、供給するガス量が同じ場合、ガス圧縮機は液化ガスポンプに比べて大型になり、圧縮動力が嵩むとともに設置スペースも大きくなり、さらに騒音も大きいことから、その採用は限定的であり、ガス供給量が少量のときや供給圧力が低いときに採用されるのみである。すなわち、ガス供給量が多い場合や、供給圧力が10MPa程度以上の場合は、昇圧手段として液化ガスポンプが用いられている。
【0004】
【発明が解決しようとする課題】
しかし、液化ガスポンプにおいても、ガス圧縮機に比べて音量が小さいとはいえ、設置場所によっては、その駆動部から発生する騒音が問題となることがあり、また、定期的な分解を伴うメンテナンスを行う必要があるという問題がある。
【0005】
さらに、液化ガスポンプは、吸入圧力が高いほど昇圧をスムーズに行えるため、液化ガス貯槽12と液化ガスポンプ13とに高低差を設けておくことが好ましいが、液化ガス貯槽12が小型の可搬式液化ガス貯槽である場合は、高低差を稼ぐことができないので、その結果、液化ガスポンプの性能を十分に引き出せずに液化ガスの圧縮効率が低下することになってしまう。
【0006】
そこで本発明は、昇圧手段に供給される低温液化ガスの圧力が低くても十分な昇圧性能を有し、駆動音等の騒音も発生しない静かな昇圧手段を使用したガス充填装置及び方法を提供することを目的としている。
【0007】
【課題を解決するための手段】
上記目的を達成するため、本発明のガス充填装置は、液化ガス貯槽に貯留された液化ガスを所定圧力に昇圧してガス容器に充填する装置であって、低温液化ガスを貯留する液化ガス貯槽と、該液化ガス貯槽から導出した低温液化ガスを一時貯留する加圧槽と、該加圧槽から導出した低温液化ガスを蒸発させて加圧槽内に再導入することによって加圧槽内を加圧する加圧蒸発器と、加圧槽から導出した前記低温液化ガスを蒸発させる蒸発器と、該蒸発器で蒸発したガスをガス容器に充填するガス充填部と、前記加圧槽内に貯留した低温液化ガス量を測定する測定手段とを備え、前記測定手段は、前記ガス充填部におけるガス容器の容量、本数及び圧力を入力することにより、加圧槽内に貯留すべき低温液化ガス量を算出する演算手段を備えていることを特徴としている。
【0008】
また、本発明のガス充填方法は、液化ガス貯槽に貯留された液化ガスを所定圧力に昇圧してガス容器に充填する方法であって、液化ガス貯槽内に貯留されている低温液化ガスを導出して加圧槽に導入するに当たり、前記ガス容器に充填するガスの総量及び圧力から必要とする液化ガス量を算出して導入するとともに、該加圧槽から導出した低温液化ガスを加圧蒸発器に導入して蒸発させた後、加圧槽内に再導入することによって加圧槽内を加圧し、加圧された低温液化ガスを加圧槽から導出して蒸発器により全量蒸発させ、蒸発後のガスをガス充填部で前記ガス容器に充填することを特徴としている。
【0009】
【発明の実施の形態】
図1は、本発明のガス充填装置の一形態例を示す系統図である。このガス充填装置は、ガス充填部21でガス容器22,23に充填するためのガスを低温液化ガスの状態で貯留する液化ガス貯槽24と、該液化ガス貯槽24から導出した低温液化ガスを一時貯留する加圧槽25と、該加圧槽25から導出した低温液化ガスを蒸発させて加圧槽25内に再導入することによって加圧槽25内を加圧する加圧蒸発器26と、加圧槽25から導出した前記低温液化ガスを蒸発させる蒸発器27と、前記加圧槽25内に貯留した低温液化ガス量を測定する測定手段としてのロードセル28とを備えており、前記蒸発器27で蒸発したガスを、前記ガス充填部21に供給して各ガス容器22,23にそれぞれ充填するように形成している。
【0010】
前記液化ガス貯槽24と前記加圧槽25とは、切換弁31、送液元弁32を備えた配管33で接続されており、切換弁31と送液元弁32との間及び送液元弁32と加圧槽25との間には、低温液化ガスを液封したときの安全対策として安全弁34,35がそれぞれ設けられている。なお、切換弁31は、図に破線で示すように、複数の液化ガス貯槽24,24aを使用するときに、各切換弁31,31aを切換開閉して連続的に低温液化ガスを供給するときに用いるものであり、液化ガス貯槽が1基だけの場合は省略することができる。
【0011】
また、加圧槽25には、槽内のガスをパージするためのパージ弁36が設けられており、加圧蒸発器26の入口側配管37には加圧元弁38が設けられ、出口側配管39には圧力計40が設けられている。なお、この加圧槽25に接続される各配管は、前記ロードセル28による重量測定を正確に行うようにするため、柔軟性を有する断熱フレキシブルチューブを使用することが望ましい。
【0012】
この加圧槽25から前記蒸発器27を経てガス充填部21に接続する配管41には、圧力計42が設けられるとともに、その下流で複数の充填系列、例えば第1充填系列43と第2充填系列44とに、それぞれ送ガス元弁45,46を介して分岐しており、各充填系列43,44には、圧力計47,48と安全弁49,50とがそれぞれ設けられている。
【0013】
前記ロードセル28は、演算手段51及び制御手段52が設けられている。演算手段51は、前記ガス充填部21における各ガス容器22,23の容量、本数及び圧力とガスの種類とを入力することにより、加圧槽25内に貯留すべき低温液化ガス量を算出するものであって、制御手段52は、演算手段51等からの情報に基づいて各弁の開閉制御等を行うように形成されている。
【0014】
以下、上述のように形成したガス充填装置で各ガス容器22,23に所定圧力のガスを充填する手順を説明する。まず、各ガス容器22,23を各充填系列43,44にセットする。このとき、各ガス容器22,23の容積は同じであってもよく、異なっていてもよいが、一つの充填系列にセットするガス容器の充填圧力は同じ圧力に揃えるようにする。次に、前記演算手段51に、ガス容器の容量、本数及び圧力とガスの種類とを入力する。
【0015】
図2は、この入力操作の流れを示すフローチャートであって、まず、ステップ61でガスの種類を入力する。なお、このガス充填装置で充填するガスが一種類だけの場合は、ステップ61でのガスの種類の入力は不要である。次に、ステップ62で各ガス容器内に残っているガスの圧力、すなわち、容器内残圧を圧力計47,48から読取る。このステップ62は、ガス容器内にガスが残っている状態で増充填を行う場合にのみ行うステップであり、パージ操作を行った空容器内にガスを充填する場合は不要である。
【0016】
そして、ステップ63でガス容器の容積を入力し、ステップ64でガス容器の本数を入力する。容積が異なるガス容器に同時にガスの充填を行う場合は、ステップ63とステップ64とを繰返して各容積に対するそれぞれの本数を入力していく。最後にステップ65で充填圧力を入力すると、ガス容器の総容積と充填圧力とから合計充填ガス量を算出することができ、これを低温液化ガスの重量に換算すれば、液化ガス貯槽24から加圧槽25に移送する低温液化ガス量を算出することができる。
【0017】
なお、このときの低温液化ガス量には、加圧槽25の容積をはじめとして、加圧蒸発器26や蒸発器27、各配管41,43等の容積が加算された補正値となり、ガス容器内を実ガスでパージする際には、パージロスも含めた補正を行うようにし、さらに、各部の温度を測定して温度補正も行うことにより、必要な低温液化ガス量をより正確に算出することができる。
【0018】
上述のようにして必要事項を入力し、充填開始を指示する。なお、充填開始時には切換弁31以外は閉じ状態となっているものとする。まず、充填開始に伴って送液元弁32及びパージ弁36が開き、液化ガス貯槽24から前記加圧槽25に向けての送液が開始される。液化ガス貯槽24からの低温液化ガスは、各配管や弁を冷却することによって気化し、当初はガスのみが加圧槽25に流入するが、このガスはパージ弁36から外部に放出される。
【0019】
低温液化ガスの通路が十分に冷却され、加圧槽25も十分に冷却されると、加圧槽25内に低温液化ガスが溜まり始める。加圧槽25内に流入した低温液化ガス量は、前記ロードセル28によって計測され、その計測値が、前述のようにして算出した低温液化ガス量に到達すると、制御手段52からの信号によって送液元弁32及びパージ弁36が閉じられ、液化ガス貯槽24から前記加圧槽25への低温液化ガスの送液が終了する。
【0020】
次に、加圧元弁38及び送ガス元弁45,46が開き、加圧槽25内の加圧と各ガス容器へのガス充填が始まる。加圧元弁38が開くと、加圧槽25内の低温液化ガスの一部が入口側配管37を通って加圧蒸発器26に流入し、該加圧蒸発器26で大気空気等の熱源により加熱されて蒸発し、出口側配管39を経て加圧槽25内に再導入される。このように、加圧蒸発器26で蒸発させたガスを加圧槽25に再導入することにより、液体から気体に変化したときの体積膨張によって加圧槽25内が徐々に加圧される。この加圧状況は圧力計40により測定され、圧力が上昇しすぎたときには加圧元弁38を一時閉鎖する。
【0021】
加圧された低温液化ガスは、加圧槽25から前記蒸発器27に流入し、大気空気等によって加熱されることにより全量が蒸発し、各充填系列43,44に分岐して送ガス元弁45,46を通り、各ガス容器22,23内に充填される。そして、加圧槽25内の低温液化ガスの全量が蒸発したときに、各ガス容器22,23内に所定圧力のガスがそれぞれ充填されたことになるので、各弁を閉じて充填操作が終了する。また、充填操作の終了は、各充填系列43,44に設けた圧力計47,48によって確認することができる。
【0022】
このように、ロードセル28で加圧槽25の重量を測定し、あらかじめ算出して補正を加えた充填ガス量に相当する低温液化ガス量を加圧槽25内に送液してから充填操作を開始することにより、加圧槽25内の低温液化ガスが全量蒸発してロードセル28の測定重量が送液開始前の重量に復帰した時点を充填終了と判断することができるので、充填ガス量を算出する元となる前記容器容積、容器本数及び充填圧力を入力するだけで自動的にガス充填を行うことができる。また、加圧槽25内の低温液化ガス量を測定することによって必要量の低温液化ガスを加圧槽25に送液できるので、充填操作終了時に加圧槽25に必要量以上の低温液化ガスが残存することがなく、この残存した低温液化ガスを放出することによる低温液化ガスのロスも低減することができる。
【0023】
そして、上述のように、充填するガスの昇圧を、加圧槽25と加圧蒸発器26との組合わせで行うことにより、液化ガスポンプの駆動音のような騒音を発生することがなくなり、また、液化ガス貯槽24から加圧槽25への送液は、パージ弁36が開いて略大気圧状態の加圧槽25に低温液化ガスを送込めばよいので、液化ガス貯槽24の貯液圧力が低く、高低差を稼げない場合であっても、例えば小型の可搬式液化ガス貯槽の場合でも送液操作に支障を来すことはない。
【0024】
図3は、複数の充填系列における充填圧力がそれぞれ異なる場合の入力操作の流れを示すフローチャートである。最初のステップ71は、ガスの種類を入力するステップであり、このステップ71も前記同様に省略することができる。また、前記ステップ62と同様の容器内残圧を読取るステップを付加することもできる。次に、ステップ72で充填系列を入力し、ステップ73及びステップ74で、該充填系列における容器容積の入力及び容器本数の入力を、前記ステップ63,64と同様にして行う。さらに、ステップ75で該充填系列における充填圧力を入力する。これで一つの系列における必要事項の入力が終了したことになる。続いて、ステップ72に戻り、次の充填系列を入力し、ステップ73及びステップ74で容器容積の入力及び容器本数の入力を行い、ステップ75で該充填系列における充填圧力を入力する。充填圧力が異なる充填系列が3系列以上ある場合は、ステップ72〜75を繰返して各充填系列の容器容積、容器本数、充填圧力を入力する。なお、充填系列が3系列以上の場合、その中の2系列以上が同じ充填圧力の場合は、同じ充填圧力の複数の系列をまとめて入力することができる。
【0025】
そして、前記同様にして所定量の低温液化ガスを加圧槽25に送液した後、充填操作を開始して各充填系列43,44の各ガス容器22,23へのガス充填を行う。このときの充填操作は、各充填系列についてそれぞれ単独で行ってもよく、全充填系列で同時に開始して各充填系列がそれぞれ所定圧力になったときに終了するようにしてもよい。
【0026】
各充填系列毎に単独で充填操作を行う場合は、例えば、最初に第1充填系列43の送ガス元弁45を開、第2充填系列44の送ガス元弁46を閉として第1充填系列43の充填操作を行い、該第1充填系列43に設けた圧力計47が第1充填系列43の設定圧力に到達したときに、送ガス元弁45を閉じて第1充填系列43における充填操作を終了する。続いて、送ガス元弁46を開き、第2充填系列44の充填操作を行う。この第2充填系列44の充填操作が最終の充填操作の場合は、加圧槽25内の低温液化ガスの全量が蒸発したときが充填操作の終了となる。また、第3,第4の充填系列が存在する場合は、第2充填系列44の圧力計48が設定圧力に到達したときに送ガス元弁46を閉じ、次の充填系列の充填操作に移ればよい。
【0027】
一方、全充填系列で同時に充填操作を開始した場合は、各充填系列毎にそれぞれ圧力を監視し、充填圧力が低い充填系列、例えば、第2充填系列44の充填圧力より第1充填系列43の充填圧力が低く設定されている場合は、第1充填系列43の圧力計47が設定圧力に到達したときに送ガス元弁45を閉じて第1充填系列43における充填操作を終了し、第2充填系列44は、そのまま充填操作を継続して設定圧力になるまで充填操作を行えばよい。すなわち、設定された重点圧力が低い充填系列の送ガス元弁を圧力計の測定値に基づいて順次閉じていくことにより、前記充填系列の充填操作を同時に行うことができる。
【0028】
なお、低温液化ガス量を測定する測定手段は、前記ロードセル28に限らず、他の重量測定手段を用いることもでき、加圧槽25を僅かに上下方向に変位可能に設置して変位量を測定したり、また、加圧槽25内の液面を測定したりしても、低温液化ガス量を測定することが可能である。さらに、充填操作は、ガスの種類等によって所定の操作で行うことができ、ガス容器内のパージや真空排気を行うようにしてもよい。
【0029】
また、液化ガス貯槽24から加圧槽25への送液量の算出を別の計算機で行い、加圧槽25の重量変化を確認しながら手動で送液操作を行うことも可能である。さらに、充填操作の対象が同じ場合は、すなわち、決まった容積のガス容器の決まった本数に決まった圧力でガスの充填を行う場合は、前述の図2,図3に示したような入力操作は不要であり、充填操作開始時に決まった量の低温液化ガスを液化ガス貯槽24から加圧槽25に送液すればよい。
【0030】
【発明の効果】
以上説明したように、本発明によれば、充填するガスの昇圧に液化ガスポンプやガス圧縮機を使用しないので、騒音を発生することがなく、メンテナンスに要する時間や費用も削減できる。さらに、加圧槽内の低温液化ガス量を測定することによって必要十分な量の低温液化ガスを加圧槽に送液することができるので、低温液化ガスのロスも低減することができる。また、充填対象となるガス容器の容積や本数、圧力から充填する総ガス量を算出して加圧槽への送液量を設定することにより、低温液化ガスのロスも低減することができる。
【図面の簡単な説明】
【図1】 本発明のガス充填装置の一形態例を示す系統図である。
【図2】 充填操作を行う際の入力操作の流れを示すフローチャートである。
【図3】 複数の充填系列における充填圧力がそれぞれ異なる場合の入力操作の流れを示すフローチャート図である。
【図4】 従来のガス充填装置の一例を示す系統図である。
【符号の説明】
21…ガス充填部、22,23…ガス容器、24…液化ガス貯槽、25…加圧槽、26…加圧蒸発器、27…蒸発器、28…ロードセル、31…切換弁、32…送液元弁、33…配管、34,35…安全弁、36…パージ弁、37…入口側配管、38…加圧元弁、39…出口側配管、40…圧力計、41…配管、42…圧力計、43…第1充填系列、44…第2充填系列、45,46…送ガス元弁、47,48…圧力計、49,50…安全弁、51…演算手段、52…制御手段
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a gas filling apparatus and method, and more particularly to an apparatus and method for boosting and filling a gas container with a liquefied gas stored in a liquefied gas storage tank without using a booster pump.
[0002]
[Prior art]
FIG. 4 is a system diagram showing an example of a conventional gas filling apparatus. This gas filling device includes a liquefied gas storage tank 12 that stores a gas supplied to the gas filling section 11 in a liquid state, a reciprocating liquefied gas pump 13 that compresses a low-temperature liquefied gas derived from the liquefied gas storage tank 12 to a required pressure, and And an evaporator 14 for evaporating the low-temperature liquefied gas compressed by the liquefied gas pump 13 with a heat source such as atmospheric air, and the gas evaporated by the evaporator 14 is supplied to the gas filling unit 11 to The gas containers 15 and 16 are formed so as to be filled with a predetermined pressure.
[0003]
As a means for boosting the gas supplied to the gas filling unit 11 to a required pressure, a gas compressor that boosts the gas after evaporation can be used in place of the liquefied gas pump 13. In the same case, the gas compressor is larger than the liquefied gas pump, the compression power is increased, the installation space is increased, and the noise is also large, so the adoption is limited, and when the gas supply amount is small, Only used when supply pressure is low. That is, when the gas supply amount is large, or when the supply pressure is about 10 MPa or more, a liquefied gas pump is used as the pressure increasing means.
[0004]
[Problems to be solved by the invention]
However, although the volume of a liquefied gas pump is lower than that of a gas compressor, noise generated from the drive unit may be a problem depending on the installation location, and maintenance involving periodic disassembly is required. There is a problem that needs to be done.
[0005]
Further, since the liquefied gas pump can smoothly increase the pressure as the suction pressure is higher, it is preferable to provide a difference in level between the liquefied gas storage tank 12 and the liquefied gas pump 13, but the liquefied gas storage tank 12 is a small portable liquefied gas. In the case of a storage tank, a difference in height cannot be gained, and as a result, the liquefied gas compression efficiency is lowered without sufficiently extracting the performance of the liquefied gas pump.
[0006]
Accordingly, the present invention provides a gas filling apparatus and method using a quiet pressure-up means that has sufficient pressure-up performance even when the pressure of the low-temperature liquefied gas supplied to the pressure-up means is low and does not generate noise such as driving noise. The purpose is to do.
[0007]
[Means for Solving the Problems]
In order to achieve the above object, a gas filling device of the present invention is a device for boosting a liquefied gas stored in a liquefied gas storage tank to a predetermined pressure and filling the gas container, wherein the liquefied gas storage tank stores a low-temperature liquefied gas. And a pressurized tank for temporarily storing the low-temperature liquefied gas derived from the liquefied gas storage tank, and the inside of the pressurized tank by evaporating the low-temperature liquefied gas derived from the pressurized tank and reintroducing it into the pressurized tank. and pressurizing evaporator pressurizing, an evaporator for evaporating the low-temperature liquefied gas derived from the pressurized圧槽, a gas-filled portion of the gas evaporated in the evaporator is filled in the gas container, in the prior SL pressurized圧槽and a measuring means for measuring the pooled low temperature liquefied gas amount, before Symbol measuring means, the capacity of the gas container in the gas filling unit, by inputting the number and pressure, low temperature liquefied to be stored in a pressurized圧槽Computation means to calculate the amount of gas It is characterized in that.
[0008]
Further, the gas filling method of the present invention is a method of increasing the liquefied gas stored in the liquefied gas storage tank to a predetermined pressure and filling the gas container, wherein the low-temperature liquefied gas stored in the liquefied gas storage tank is derived. When introducing into the pressurized tank, the required amount of liquefied gas is calculated and introduced from the total amount and pressure of the gas filled in the gas container, and the low-temperature liquefied gas derived from the pressurized tank is pressurized and evaporated. After introducing into the vessel and evaporating, pressurize the inside of the pressurized tank by reintroducing it into the pressurized tank, lead out the pressurized low-temperature liquefied gas from the pressurized tank and evaporate the whole amount by the evaporator, The gas container is filled with the gas after evaporation in a gas filling section.
[0009]
DETAILED DESCRIPTION OF THE INVENTION
FIG. 1 is a system diagram showing an embodiment of the gas filling apparatus of the present invention. This gas filling device temporarily stores a liquefied gas storage tank 24 for storing the gas for filling the gas containers 22 and 23 in the gas filling section 21 in a state of a low temperature liquefied gas, and a low temperature liquefied gas derived from the liquefied gas storage tank 24. A pressurized tank 25 to be stored; a pressurized evaporator 26 that pressurizes the pressurized tank 25 by evaporating the low-temperature liquefied gas derived from the pressurized tank 25 and reintroducing it into the pressurized tank 25; An evaporator 27 for evaporating the low-temperature liquefied gas derived from the pressure tank 25 and a load cell 28 as a measuring means for measuring the amount of the low-temperature liquefied gas stored in the pressurization tank 25 are provided. The gas evaporated in this step is supplied to the gas filling unit 21 to fill the gas containers 22 and 23, respectively.
[0010]
The liquefied gas storage tank 24 and the pressurizing tank 25 are connected by a pipe 33 having a switching valve 31 and a liquid supply source valve 32, and between the switch valve 31 and the liquid supply source valve 32 and the liquid supply source. Safety valves 34 and 35 are provided between the valve 32 and the pressurizing tank 25 as safety measures when the low-temperature liquefied gas is sealed. In addition, as shown by the broken line in the figure, when the switching valve 31 uses a plurality of liquefied gas storage tanks 24 and 24a, the switching valve 31 and 31a are switched to open and close to supply low-temperature liquefied gas continuously. It can be omitted if there is only one liquefied gas storage tank.
[0011]
The pressurizing tank 25 is provided with a purge valve 36 for purging the gas in the tank, the inlet side pipe 37 of the pressurizing evaporator 26 is provided with a pressurizing source valve 38, and the outlet side A pressure gauge 40 is provided in the pipe 39. In addition, it is desirable that each piping connected to the pressurizing tank 25 uses a heat insulating flexible tube having flexibility in order to accurately measure the weight by the load cell 28.
[0012]
A pipe 41 connected to the gas filling unit 21 from the pressure tank 25 through the evaporator 27 is provided with a pressure gauge 42 and a plurality of filling lines, for example, a first filling line 43 and a second filling line downstream thereof. Branches to the series 44 via gas supply source valves 45 and 46, respectively, and pressure gauges 47 and 48 and safety valves 49 and 50 are provided in the filling series 43 and 44, respectively.
[0013]
The load cell 28 is provided with calculation means 51 and control means 52. The computing means 51 calculates the amount of low-temperature liquefied gas to be stored in the pressurizing tank 25 by inputting the capacity, number and pressure of each gas container 22 and 23 in the gas filling unit 21 and the type of gas. The control means 52 is configured to perform opening / closing control of each valve based on information from the calculation means 51 and the like.
[0014]
Hereinafter, a procedure for filling the gas containers 22 and 23 with a gas having a predetermined pressure using the gas filling apparatus formed as described above will be described. First, the gas containers 22 and 23 are set in the filling lines 43 and 44, respectively. At this time, the volumes of the gas containers 22 and 23 may be the same or different, but the filling pressures of the gas containers set in one filling line are made to be the same. Next, the capacity, number and pressure of the gas container and the type of gas are input to the calculation means 51.
[0015]
FIG. 2 is a flowchart showing the flow of this input operation. First, in step 61, the type of gas is input. If there is only one type of gas to be filled with this gas filling device, it is not necessary to input the type of gas at step 61. Next, in step 62, the pressure of the gas remaining in each gas container, that is, the residual pressure in the container is read from the pressure gauges 47 and 48. This step 62 is a step performed only when the additional filling is performed in a state where the gas remains in the gas container, and is unnecessary when the empty container subjected to the purge operation is filled with the gas.
[0016]
In step 63, the volume of the gas container is input, and in step 64, the number of gas containers is input. When the gas containers having different volumes are filled with gas at the same time, step 63 and step 64 are repeated to input the numbers corresponding to the respective volumes. Finally, when the filling pressure is input in step 65, the total filling gas amount can be calculated from the total volume of the gas container and the filling pressure. If this is converted into the weight of the low-temperature liquefied gas, it is added from the liquefied gas storage tank 24. The amount of low-temperature liquefied gas transferred to the pressure vessel 25 can be calculated.
[0017]
Note that the amount of the low-temperature liquefied gas at this time is a correction value obtained by adding the volume of the pressurized evaporator 26, the evaporator 27, the pipes 41, 43, and the like, in addition to the volume of the pressurized tank 25. When purging the interior with real gas, correction including purge loss is performed, and furthermore, the temperature of each part is measured and temperature correction is also performed to calculate the required amount of low-temperature liquefied gas more accurately Can do.
[0018]
The necessary items are input as described above, and the start of filling is instructed. In addition, it is assumed that the parts other than the switching valve 31 are closed at the start of filling. First, with the start of filling, the liquid supply source valve 32 and the purge valve 36 are opened, and liquid supply from the liquefied gas storage tank 24 toward the pressure tank 25 is started. The low-temperature liquefied gas from the liquefied gas storage tank 24 is vaporized by cooling each pipe and valve, and initially only the gas flows into the pressurizing tank 25, but this gas is released to the outside from the purge valve 36.
[0019]
When the passage of the low-temperature liquefied gas is sufficiently cooled and the pressurized tank 25 is also sufficiently cooled, the low-temperature liquefied gas begins to accumulate in the pressurized tank 25. The amount of the low-temperature liquefied gas flowing into the pressurizing tank 25 is measured by the load cell 28. When the measured value reaches the amount of the low-temperature liquefied gas calculated as described above, the liquid is sent by a signal from the control means 52. The main valve 32 and the purge valve 36 are closed, and the supply of the low-temperature liquefied gas from the liquefied gas storage tank 24 to the pressurizing tank 25 is completed.
[0020]
Next, the pressurization source valve 38 and the gas supply source valves 45 and 46 are opened, and pressurization in the pressurization tank 25 and gas filling into each gas container are started. When the pressurizing source valve 38 is opened, a part of the low-temperature liquefied gas in the pressurizing tank 25 flows into the pressurized evaporator 26 through the inlet side pipe 37, and the pressurized evaporator 26 generates a heat source such as atmospheric air. Is heated and evaporated, and is reintroduced into the pressure tank 25 through the outlet side pipe 39. Thus, by re-introducing the gas evaporated by the pressure evaporator 26 into the pressure tank 25, the inside of the pressure tank 25 is gradually pressurized by the volume expansion when it changes from a liquid to gas. This pressurization state is measured by the pressure gauge 40, and when the pressure rises too much, the pressurization source valve 38 is temporarily closed.
[0021]
The pressurized low-temperature liquefied gas flows from the pressurizing tank 25 into the evaporator 27 and is heated by atmospheric air or the like to evaporate the entire amount, branching to the respective filling lines 43 and 44, and the gas supply source valve The gas containers 22 and 23 are filled through the gas tanks 45 and 46. When the entire amount of the low-temperature liquefied gas in the pressurizing tank 25 is evaporated, the gas containers 22 and 23 are filled with the gas of a predetermined pressure, so that the filling operation is finished by closing the valves. To do. The completion of the filling operation can be confirmed by pressure gauges 47 and 48 provided in the filling lines 43 and 44, respectively.
[0022]
Thus, the weight of the pressurizing tank 25 is measured by the load cell 28, and the filling operation is performed after the low-temperature liquefied gas amount corresponding to the pre-calculated and corrected filling gas amount is fed into the pressurizing tank 25. By starting, it can be determined that the filling is completed when the low-temperature liquefied gas in the pressurized tank 25 is completely evaporated and the measured weight of the load cell 28 returns to the weight before the start of liquid feeding. Gas filling can be automatically performed only by inputting the container volume, the number of containers, and the filling pressure, which are to be calculated. In addition, since the required amount of low-temperature liquefied gas can be sent to the pressurized tank 25 by measuring the amount of low-temperature liquefied gas in the pressurized tank 25, the amount of low-temperature liquefied gas exceeding the required amount in the pressurized tank 25 at the end of the filling operation. Does not remain, and the loss of the low-temperature liquefied gas due to the discharge of the remaining low-temperature liquefied gas can be reduced.
[0023]
As described above, the pressure of the gas to be filled is increased by the combination of the pressurized tank 25 and the pressurized evaporator 26, so that noise such as driving sound of the liquefied gas pump is not generated. The liquid supply from the liquefied gas storage tank 24 to the pressurizing tank 25 may be performed by supplying the low-temperature liquefied gas to the pressurizing tank 25 in an approximately atmospheric pressure state when the purge valve 36 is opened. Even if it is a case where the height difference is low and the height difference cannot be obtained, for example, even in the case of a small portable liquefied gas storage tank, the liquid feeding operation is not hindered.
[0024]
FIG. 3 is a flowchart showing a flow of an input operation when filling pressures in a plurality of filling sequences are different from each other. The first step 71 is a step of inputting the type of gas, and this step 71 can also be omitted as described above. Further, a step of reading the in-container residual pressure similar to the step 62 can be added. Next, a filling sequence is input in step 72, and in steps 73 and 74, the input of the container volume and the number of containers in the filling sequence is performed in the same manner as in steps 63 and 64. In step 75, the filling pressure in the filling series is input. This completes the input of necessary items in one series. Subsequently, returning to step 72, the next filling sequence is input, the container volume and the number of containers are input in step 73 and step 74, and the filling pressure in the filling sequence is input in step 75. If there are three or more filling series having different filling pressures, steps 72 to 75 are repeated to input the container volume, the number of containers, and the filling pressure of each filling series. When there are three or more filling series, and two or more of them have the same filling pressure, a plurality of series having the same filling pressure can be input together.
[0025]
Then, after a predetermined amount of low-temperature liquefied gas is sent to the pressurized tank 25 in the same manner as described above, the filling operation is started and the gas containers 22 and 23 of the filling series 43 and 44 are filled with gas. The filling operation at this time may be performed independently for each filling line, or may be started simultaneously for all filling lines and ended when each filling line reaches a predetermined pressure.
[0026]
When performing the filling operation independently for each filling line, for example, the first filling line is first opened by first opening the gas supply source valve 45 of the first filling line 43 and closing the gas supply source valve 46 of the second filling line 44. 43. When the pressure gauge 47 provided in the first filling line 43 reaches the set pressure of the first filling line 43, the gas supply valve 45 is closed and the filling operation in the first filling line 43 is performed. Exit. Subsequently, the gas supply source valve 46 is opened, and the filling operation of the second filling line 44 is performed. When the filling operation of the second filling line 44 is the final filling operation, the filling operation ends when the entire amount of the low-temperature liquefied gas in the pressurizing tank 25 has evaporated. When the third and fourth filling series exist, when the pressure gauge 48 of the second filling series 44 reaches the set pressure, the gas supply source valve 46 is closed and the next filling series can be filled. That's fine.
[0027]
On the other hand, when the filling operation is started simultaneously in all the filling lines, the pressure is monitored for each filling line, and the first filling line 43 has a lower filling pressure, for example, the first filling line 43 than the filling pressure of the second filling line 44. When the filling pressure is set low, when the pressure gauge 47 of the first filling line 43 reaches the set pressure, the gas supply source valve 45 is closed to finish the filling operation in the first filling line 43, and the second In the filling line 44, the filling operation may be continued until the set pressure is reached. That is, the filling operation of the filling system can be performed simultaneously by sequentially closing the gas supply source valves of the filling system having a set low priority pressure based on the measurement value of the pressure gauge.
[0028]
The measuring means for measuring the amount of low-temperature liquefied gas is not limited to the load cell 28, and other weight measuring means can be used. The pressurizing tank 25 is installed so as to be slightly displaceable in the vertical direction, and the amount of displacement is determined. It is possible to measure the amount of the low-temperature liquefied gas even if it is measured or the liquid level in the pressurized tank 25 is measured. Furthermore, the filling operation can be performed by a predetermined operation depending on the type of gas or the like, and the gas container may be purged or evacuated.
[0029]
It is also possible to calculate the amount of liquid fed from the liquefied gas storage tank 24 to the pressurizing tank 25 by another computer and manually perform the liquid feeding operation while checking the weight change of the pressurizing tank 25. Further, when the objects of the filling operation are the same, that is, when the gas filling is performed at a pressure determined by a fixed number of gas containers having a fixed volume, the input operation as shown in FIGS. Is not necessary, and a predetermined amount of the low-temperature liquefied gas may be sent from the liquefied gas storage tank 24 to the pressurizing tank 25 at the start of the filling operation.
[0030]
【The invention's effect】
As described above, according to the present invention, since no liquefied gas pump or gas compressor is used for boosting the gas to be filled, no noise is generated and the time and cost required for maintenance can be reduced. Further, by measuring the amount of the low-temperature liquefied gas in the pressurization tank, a necessary and sufficient amount of the low-temperature liquefied gas can be sent to the pressurization tank, so that the loss of the low-temperature liquefied gas can also be reduced. Moreover, the loss of the low-temperature liquefied gas can also be reduced by calculating the total amount of gas to be filled from the volume and number of gas containers to be filled, and the pressure, and setting the amount of liquid fed to the pressurizing tank.
[Brief description of the drawings]
FIG. 1 is a system diagram showing an embodiment of a gas filling apparatus according to the present invention.
FIG. 2 is a flowchart showing a flow of an input operation when performing a filling operation.
FIG. 3 is a flowchart showing a flow of input operation when filling pressures in a plurality of filling series are different from each other.
FIG. 4 is a system diagram showing an example of a conventional gas filling device.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 21 ... Gas filling part, 22, 23 ... Gas container, 24 ... Liquefied gas storage tank, 25 ... Pressurization tank, 26 ... Pressurization evaporator, 27 ... Evaporator, 28 ... Load cell, 31 ... Switching valve, 32 ... Liquid sending Source valve 33 ... Piping 34,35 ... Safety valve 36 ... Purge valve 37 ... Inlet side piping 38 ... Pressure source valve 39 ... Outlet side piping 40 ... Pressure gauge 41 ... Piping 42 ... Pressure gauge , 43 ... 1st filling series, 44 ... 2nd filling series, 45, 46 ... Gas supply source valve, 47, 48 ... Pressure gauge, 49, 50 ... Safety valve, 51 ... Calculation means, 52 ... Control means

Claims (2)

液化ガス貯槽に貯留された液化ガスを所定圧力に昇圧してガス容器に充填する装置であって、低温液化ガスを貯留する液化ガス貯槽と、該液化ガス貯槽から導出した低温液化ガスを一時貯留する加圧槽と、該加圧槽から導出した低温液化ガスを蒸発させて加圧槽内に再導入することによって加圧槽内を加圧する加圧蒸発器と、加圧槽から導出した前記低温液化ガスを蒸発させる蒸発器と、該蒸発器で蒸発したガスをガス容器に充填するガス充填部と、前記加圧槽内に貯留した低温液化ガス量を測定する測定手段とを備え、前記測定手段は、前記ガス充填部におけるガス容器の容量、本数及び圧力を入力することにより、加圧槽内に貯留すべき低温液化ガス量を算出する演算手段を備えていることを特徴とするガス充填装置。A device that boosts the liquefied gas stored in the liquefied gas storage tank to a predetermined pressure and fills the gas container with the liquefied gas storage tank for storing the low-temperature liquefied gas, and temporarily stores the low-temperature liquefied gas derived from the liquefied gas storage tank. A pressurized tank, a pressurized evaporator that pressurizes the inside of the pressurized tank by evaporating the low-temperature liquefied gas derived from the pressurized tank and reintroducing it into the pressurized tank, and the aforementioned derived from the pressurized tank An evaporator for evaporating the low-temperature liquefied gas, a gas filling unit for filling the gas container with the gas evaporated by the evaporator, and a measuring means for measuring the amount of the low-temperature liquefied gas stored in the pressurization tank, The measuring means comprises a calculating means for calculating the amount of low-temperature liquefied gas to be stored in the pressurized tank by inputting the capacity, number and pressure of the gas containers in the gas filling section. Filling equipment. 液化ガス貯槽に貯留された液化ガスを所定圧力に昇圧してガス容器に充填する方法であって、液化ガス貯槽内に貯留されている低温液化ガスを導出して加圧槽に導入するに当たり、前記ガス容器に充填するガスの総量及び圧力から必要とする液化ガス量を算出して導入するとともに、該加圧槽から導出した低温液化ガスを加圧蒸発器に導入して蒸発させた後、加圧槽内に再導入することによって加圧槽内を加圧し、加圧された低温液化ガスを加圧槽から導出して蒸発器により全量蒸発させ、蒸発後のガスをガス充填部で前記ガス容器に充填することを特徴とするガス充填方法 A method of increasing the pressure of the liquefied gas stored in the liquefied gas storage tank to a predetermined pressure and filling the gas container, in deriving the low-temperature liquefied gas stored in the liquefied gas storage tank and introducing it into the pressurized tank, After calculating and introducing the required amount of liquefied gas from the total amount and pressure of the gas filled in the gas container, after introducing the low-temperature liquefied gas derived from the pressurized tank into the pressurized evaporator and evaporating it, The inside of the pressurizing tank is pressurized by being reintroduced into the pressurizing tank, the pressurized low-temperature liquefied gas is led out from the pressurizing tank and evaporated in its entirety by the evaporator, and the gas after evaporation is the gas filling unit. A gas filling method comprising filling a gas container .
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JP5090823B2 (en) * 2007-08-29 2012-12-05 大陽日酸株式会社 Liquid gas delivery method
JP5077881B2 (en) * 2007-10-10 2012-11-21 千代田化工建設株式会社 Facility for receiving liquefied natural gas
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