JPH0633860B2 - Ultra low temperature liquefied gas supply method - Google Patents

Ultra low temperature liquefied gas supply method

Info

Publication number
JPH0633860B2
JPH0633860B2 JP18542385A JP18542385A JPH0633860B2 JP H0633860 B2 JPH0633860 B2 JP H0633860B2 JP 18542385 A JP18542385 A JP 18542385A JP 18542385 A JP18542385 A JP 18542385A JP H0633860 B2 JPH0633860 B2 JP H0633860B2
Authority
JP
Japan
Prior art keywords
liquefied gas
temperature
pump
precooling
low temperature
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP18542385A
Other languages
Japanese (ja)
Other versions
JPS6246098A (en
Inventor
安平 谷
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Japan Oxygen Co Ltd
Original Assignee
Japan Oxygen Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Japan Oxygen Co Ltd filed Critical Japan Oxygen Co Ltd
Priority to JP18542385A priority Critical patent/JPH0633860B2/en
Publication of JPS6246098A publication Critical patent/JPS6246098A/en
Publication of JPH0633860B2 publication Critical patent/JPH0633860B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C13/00Details of vessels or of the filling or discharging of vessels
    • F17C13/02Special adaptations of indicating, measuring, or monitoring equipment
    • F17C13/026Special adaptations of indicating, measuring, or monitoring equipment having the temperature as the parameter
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C9/00Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2223/00Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/01Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
    • F17C2223/0146Two-phase
    • F17C2223/0153Liquefied gas, e.g. LPG, GPL
    • F17C2223/0161Liquefied gas, e.g. LPG, GPL cryogenic, e.g. LNG, GNL, PLNG
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2227/00Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/01Propulsion of the fluid
    • F17C2227/0128Propulsion of the fluid with pumps or compressors
    • F17C2227/0135Pumps
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2250/00Accessories; Control means; Indicating, measuring or monitoring of parameters
    • F17C2250/04Indicating or measuring of parameters as input values
    • F17C2250/0404Parameters indicated or measured
    • F17C2250/0439Temperature

Landscapes

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

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、超低温液化ガスを貯槽から液化ガス加圧ポン
プによりボンベ等の容器や需要先に加圧供給する超低温
液化ガス供給方法に関する。
TECHNICAL FIELD The present invention relates to a method for supplying ultra-low temperature liquefied gas from a storage tank under pressure to a container such as a cylinder or a customer by a liquefied gas pressure pump.

〔従来の技術〕[Conventional technology]

従来の超低温液化ガス供給方法を第2図の配管系統図に
基づいて説明すると、弁1,2,3,4を開いて超低温
液化ガス貯槽5内の超低温液化ガスにより液化ガス加圧
ポンプ6内をパージして洗滌したり、供給中ポンプ6内
で液化ガスの気化を抑えるため予冷をしているが、これ
を手動で行っているのが実情である。
The conventional ultra-low temperature liquefied gas supply method will be described with reference to the piping system diagram of FIG. 2. The valves 1, 2, 3 and 4 are opened, and the ultra-low temperature liquefied gas in the ultra-low temperature liquefied gas storage tank 5 is used to pump the liquefied gas pressurizing pump 6. Is pre-cooled in order to suppress vaporization of the liquefied gas in the pump 6 during supply, but this is done manually.

即ち、液化ガス加圧ポンプ6の予冷が完了したことを弁
2,4から噴出する液化ガスの量を視認して液化ガス加
圧ポンプ6を起動し、弁2,4を閉じて超低温液化ガス
を気化器7に送液し、高圧気化ガスとしてボンベ等の容
器8に充填している。
That is, the liquefied gas pressurizing pump 6 is started by observing the amount of the liquefied gas ejected from the valves 2 and 4 when the precooling of the liquefied gas pressurizing pump 6 is completed, and the valves 2 and 4 are closed to close the ultra-low temperature liquefied gas. Is sent to the vaporizer 7 and is filled in a container 8 such as a cylinder as high-pressure vaporized gas.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

ところが、この方法の場合、手動で弁操作等を行ってい
るため操作員の経験にたよるものであって、液化ガス加
圧ポンプ6の予冷完了確認が難しく、また、予冷時の超
低温液化ガスの消費量が多く、さらに予冷を行ったにも
拘らず液化ガス加圧ポンプ6の起動後予冷不足あるいは
該ポンプ6の稼働中の温度上昇等の原因によりキャビテ
ーションを起こし、ポンプの空打原因となり、これによ
って、例えば、液化酸素加圧ポンプにおいては、ポンプ
のグランド部の過熱により発火爆発事故に結びつく危険
があり、これを防ぐには常に視覚による監視で判断して
防止していた。
However, in the case of this method, it is difficult to confirm the precooling completion of the liquefied gas pressurizing pump 6 because the valve operation is manually performed, and it is difficult to confirm the precooling of the liquefied gas pressurizing pump 6. Consuming a large amount of water and causing cavitation due to insufficient precooling after activation of the liquefied gas pressurizing pump 6 or temperature rise during operation of the pump 6 despite the fact that precooling was performed, causing the pump to run dry. As a result, for example, in a liquefied oxygen pressurizing pump, there is a risk of causing an ignition and explosion accident due to overheating of the gland portion of the pump, and in order to prevent this, it is always judged visually to prevent it.

そこで本発明は、液化ガス加圧ポンプの系内パージ、予
冷、起動を自動的に行って、液化ガス加圧ポンプに発生
するキャビテーションやこれに起因する空打を防止して
安全確保及び省力化を図った超低温液化ガス供給方法を
提供することを目的としている。
Therefore, the present invention automatically performs in-system purging, pre-cooling and starting of the liquefied gas pressurizing pump to prevent cavitation generated in the liquefied gas pressurizing pump and idling resulting therefrom, ensuring safety and saving labor. It is an object of the present invention to provide an ultra-low temperature liquefied gas supply method for achieving the above.

〔課題を解決するための手段〕[Means for Solving the Problems]

上記目的達成のため本発明は、超低温液化ガス貯槽の超
低温液化ガスを液化ガス加圧ポンプによりボンベ等の容
器に加圧供給する超低温液化ガス供給方法において、前
記液化ガス加圧ポンプの吐出側に設けた温度測定センサ
により液化ガス加圧ポンプ内の温度を検知し、この検知
した温度を、予冷完了温度及びキャビテーション発生温
度を予め設定した温度指示設定器で測温し、前記各設定
温度への到達を検出してシーケンス制御器に送信すると
ともに、該シーケンス制御器は、予冷完了温度到達信号
を受信したときに液化ガス加圧ポンプの予冷終了操作,
該ポンプの起動,送液用の弁操作を含む予冷完了シーケ
ンスを行い、キャビテーション発生温度到達信号を受信
したときに液化ガス加圧ポンプの停止,パージ用の弁操
作,該ポンプの予冷開始を含むポンプ再予冷シーケンス
を行うことを特徴としている。
In order to achieve the above object, the present invention provides an ultra-low temperature liquefied gas supply method for supplying ultra-low temperature liquefied gas from an ultra-low temperature liquefied gas storage tank to a container such as a cylinder under pressure by a liquefied gas pressure pump. The temperature measuring sensor provided detects the temperature inside the liquefied gas pressurizing pump, and the detected temperature is measured by the temperature indicator setting device that sets the precooling completion temperature and the cavitation generation temperature in advance. When the arrival at the precooling completion temperature is detected and transmitted to the sequence controller, the sequence controller, when receiving the precooling completion temperature reaching signal, precooling end operation of the liquefied gas pressurizing pump
A precooling completion sequence including activation of the pump and valve operation for liquid transfer is performed, and when the cavitation generation temperature reaching signal is received, liquefied gas pressurization pump is stopped, valve operation for purging is included, and precooling start of the pump is included. It is characterized by performing a pump pre-cooling sequence.

〔作用〕[Action]

したがって、超低温液化ガスをボンベ等の容器へ加圧供
給する場合には、液化ガス加圧ポンプが所定温度に冷却
されると、温度測定センサで検知した液化ガス加圧ポン
プ内の温度を温度指示設定器で測温し、この温度が予め
設定された予冷完了温度に到達すると、予冷完了温度到
達信号をシーケンス制御器に送信し、この予冷完了温度
到達信号を受信したシーケンス制御器により、液化ガス
加圧ポンプの予冷を終了し、該ポンプを起動するととも
に、送液用の弁を操作してボンベ等の容器への超低温液
化ガスの供給を開始する。
Therefore, when supplying ultra-low temperature liquefied gas to a container such as a cylinder under pressure, when the liquefied gas pressure pump is cooled to a predetermined temperature, the temperature inside the liquefied gas pressure pump detected by the temperature measurement sensor is indicated as a temperature. When the temperature is measured by the setting device and this temperature reaches the preset pre-cooling completion temperature, the pre-cooling completion temperature reaching signal is sent to the sequence controller, and the sequence controller receiving this pre-cooling completion temperature reaching signal causes the liquefied gas The precooling of the pressurizing pump is completed, the pump is started, and the valve for liquid feeding is operated to start the supply of the ultra-low temperature liquefied gas to the container such as the cylinder.

また、超低温液化ガスのボンベ等の容器への加圧供給中
に液化ガス加圧ポンプ内の温度が上昇した場合には、温
度測定センサで検知して温度指示設定器で測温した液化
ガス加圧ポンプ内の温度が予め設定されたキャビテーシ
ョン発生温度に到達すると、キャビテーション発生温度
到達信号をシーケンス制御器に送信し、このキャビテー
ション発生温度到達信号を受信したシーケンス制御器に
より、液化ガス加圧ポンプを停止するとともに、予冷ガ
スパージ用の弁を操作して、該ポンプの再予冷を開始す
る。
If the temperature inside the liquefied gas pressure pump rises during the pressurized supply of ultra-low temperature liquefied gas to a container such as a cylinder, the liquefied gas pressure detected by the temperature measurement sensor and measured by the temperature indicator When the temperature inside the pressure pump reaches the preset cavitation generation temperature, it sends a cavitation generation temperature arrival signal to the sequence controller, and the sequence controller that receives this cavitation generation temperature arrival signal operates the liquefied gas pressurization pump. At the same time as stopping, the precooling gas purge valve is operated to start reprecooling of the pump.

この再予冷により、液化ガス加圧ポンプが予冷完了温度
までに冷却されると、シーケンス制御器により、液化ガ
ス加圧ポンプが起動するとともに、送液用の弁が操作さ
れてボンベ等の容器への超低温液化ガスの供給が再び開
始される。
When the liquefied gas pressurizing pump is cooled to the precooling completion temperature by this re-precooling, the liquefied gas pressurizing pump is started by the sequence controller, and at the same time, the liquid feeding valve is operated to transfer it to a container such as a cylinder. The supply of the ultra-low temperature liquefied gas is restarted.

〔実施例〕〔Example〕

以下、本発明の一実施例を第1図の配管系統図に基づい
て説明する。
An embodiment of the present invention will be described below with reference to the piping system diagram of FIG.

電気計装盤10または遠隔電気計装盤11の自動液化加
圧スイッチを入れると、シーケンス制御器12が作動し
て、自動弁13,14,15が開となり、超低温液化ガ
ス貯槽16より超低温液化ガスが自動弁13を通り液化
ガス加圧ポンプ17内に供給され、自動弁18及び送液
用の自動弁19までの間の系内を15秒間パージする。
When the automatic liquefaction pressurizing switch of the electric instrumentation panel 10 or the remote electric instrumentation panel 11 is turned on, the sequence controller 12 is activated and the automatic valves 13, 14 and 15 are opened, and the ultra-low temperature liquefied gas storage tank 16 liquefies the ultra-low temperature liquefaction. Gas is supplied into the liquefied gas pressurizing pump 17 through the automatic valve 13, and the inside of the system between the automatic valve 18 and the automatic valve 19 for liquid transfer is purged for 15 seconds.

15秒間パージされた後、自動弁14が閉となり、同時
に自動弁18が開となって、該自動弁18を通った気化
ガスは超低温液化ガス貯槽16上部に至り、該貯槽16
内の超低温液化ガスの液面を加圧して過冷液状態を作り
だす。
After being purged for 15 seconds, the automatic valve 14 is closed and at the same time the automatic valve 18 is opened, and the vaporized gas passing through the automatic valve 18 reaches the upper portion of the ultra low temperature liquefied gas storage tank 16 and the storage tank 16
The liquid surface of the ultra-low temperature liquefied gas inside is pressurized to create a supercooled liquid state.

この間、液化ガス加圧ポンプ17を経てパージ用の自動
弁15からパージされるガスにより該ポンプ17の予冷
が行われている。
During this period, the pump 17 is pre-cooled by the gas purged from the automatic purge valve 15 via the liquefied gas pressurizing pump 17.

この液化ガス加圧ポンプ17内の温度は、該ポンプ17
の吐出側直近部に設けた温度測定センサ20で検知し
て、電気計装盤10に設けた温度指示設定器21で測温
されている。
The temperature inside the liquefied gas pressurizing pump 17 depends on the pump 17
The temperature is measured by the temperature measuring sensor 20 provided in the immediate vicinity of the discharge side and the temperature is measured by the temperature instruction setting device 21 provided in the electric instrumentation board 10.

該温度指示設定器21には、予冷完了温度及びキャビテ
ーション発生温度が予め設定されており、温度指示設定
器21で測定した温度と設定されている予冷完了温度及
びキャビテーション発生温度とを比較し、測定した温度
がこれらの設定温度に到達した際に、予冷完了温度到達
信号及びキャビテーション発生温度到達信号をシーケン
ス制御器12に送信する。この予冷完了温度は、例えば
150℃〜−120℃に設定され、キャビテーション発
生温度は、例えば予冷完了温度より数10℃高い温度に
設定されている。
The pre-cooling completion temperature and the cavitation generation temperature are preset in the temperature instruction setting device 21, and the pre-cooling completion temperature and the cavitation generation temperature that are set by the temperature instruction setting device 21 are compared and measured. When the set temperature reaches these set temperatures, the precooling completion temperature reaching signal and the cavitation generation temperature reaching signal are transmitted to the sequence controller 12. The precooling completion temperature is set to, for example, 150 ° C. to −120 ° C., and the cavitation generation temperature is set to a temperature that is higher than the precooling completion temperature by several 10 ° C., for example.

したがって、温度指示設定器21で測温された液化ガス
加圧ポンプ17内の温度が、前記予冷完了温度に到達す
るまでパージ用に自動弁15を開にして、前記ポンプ1
7内の予冷が続行される。
Therefore, the automatic valve 15 is opened for purging until the temperature in the liquefied gas pressurizing pump 17 measured by the temperature instruction setting device 21 reaches the precooling completion temperature, and the pump 1
Pre-cooling in 7 continues.

そして、液化ガス加圧ポンプ17内の温度が予冷完了温
度に到達すると、温度指示設定器21は、予冷完了温度
到達信号をシーケンス制御器12に送信し、該シーケン
ス制御器12が予冷完了温度到達信号を受信すると、シ
ーケンス制御器12の予冷完了シーケンスにより、液化
ガス加圧ポンプ17の予冷を終了して、該ポンプ17を
起動する。
When the temperature in the liquefied gas pressurizing pump 17 reaches the precooling completion temperature, the temperature instruction setting device 21 transmits a precooling completion temperature arrival signal to the sequence controller 12, and the sequence controller 12 reaches the precooling completion temperature. Upon receiving the signal, the sequence controller 12 completes the precooling of the liquefied gas pressurizing pump 17 and starts the pump 17 by the precooling completion sequence.

液化ガス加圧ポンプ17の起動後、15秒経過すると、
シーケンス制御器12により、パージ用の自動弁15が
閉じられ、送液用の自動弁19が開となり、送ガス気化
器22または超低温液化ガス充填設備23への超低温液
化ガスの供給が開始される。
After the liquefied gas pressurizing pump 17 is started, 15 seconds have passed,
The sequence controller 12 closes the automatic purging valve 15 and opens the liquid feeding automatic valve 19 to start the supply of the ultra low temperature liquefied gas to the gas feeding vaporizer 22 or the ultra low temperature liquefied gas filling facility 23. .

このように、液化ガス加圧ポンプ17の吐出側の温度と
予冷完了温度とを温度指示設定器21で比較することに
よって、シーケンス制御器12に予冷完了温度到達信号
を送り、シーケンス制御器12により、液化ガス加圧ポ
ンプ17の予冷を終了して、該ポンプ17を起動すると
ともに、パージ用の自動弁15を閉、送液用の自動弁1
9を開として、超低温液化ガスの供給を開始するので、
液化ガス加圧ポンプ17を超低温液化ガスの無駄なく確
実に予冷することができ、該ポンプ17の予冷不足によ
るキャビテーションの発生を防止できる。
In this way, by comparing the temperature on the discharge side of the liquefied gas pressurizing pump 17 and the precooling completion temperature with the temperature instruction setting device 21, a precooling completion temperature reaching signal is sent to the sequence controller 12, and the sequence controller 12 causes The pre-cooling of the liquefied gas pressurizing pump 17 is completed, the pump 17 is started, the automatic valve 15 for purging is closed, and the automatic valve 1 for liquid transfer 1
Since 9 is opened and the supply of ultra low temperature liquefied gas is started,
The liquefied gas pressurizing pump 17 can be surely precooled without waste of ultra-low temperature liquefied gas, and cavitation due to insufficient precooling of the pump 17 can be prevented.

液化ガス加圧ポンプ17から吐出された超低温液化ガス
は、送ガス気化器22または超低温液化ガス充填設備2
3に送液される。送ガス気化器22に送液された超低温
液化ガスは、送ガス気化器22で気化ガスとなって、高
圧ガス充填設備24に送られボンベ等の高圧ガス容器2
5に充填される。また、超低温液化ガス充填設備23に
送液された超低温液化ガスは、超低温液化ガス容器(図
示せず)に充填される。
The ultra low temperature liquefied gas discharged from the liquefied gas pressurizing pump 17 is supplied to the gas feed vaporizer 22 or the ultra low temperature liquefied gas filling facility 2
It is sent to 3. The ultra-low temperature liquefied gas sent to the gas sending vaporizer 22 becomes vaporized gas in the gas sending vaporizer 22, is sent to the high pressure gas filling facility 24, and is sent to the high pressure gas container 2 such as a cylinder.
5 is filled. Moreover, the ultra-low temperature liquefied gas sent to the ultra-low temperature liquefied gas filling facility 23 is filled in an ultra-low temperature liquefied gas container (not shown).

尚、高圧ガス充填設備24と超低温液化ガス充填設備2
3との切替は、切換弁26,27の自動あるいは手動操
作によって行う。
The high-pressure gas filling equipment 24 and the ultra-low temperature liquefied gas filling equipment 2
The switching with 3 is performed by automatic or manual operation of the switching valves 26 and 27.

次に、液化ガス加圧ポンプ17の運転の続行中に該ポン
プ17内の温度が上昇した場合には、該ポンプ17内の
温度を温度測定センサ20で検知し、この検知した温度
を温度指示設定器21で測温し、この温度が温度指示設
定器21に設定されたキャビテーション発生温度に到達
すると、温度指示設定器21からキャビテーション発生
温度到達信号をシーケンス制御器12に送信する。
Next, when the temperature inside the pump 17 rises while the liquefied gas pressurizing pump 17 continues to operate, the temperature inside the pump 17 is detected by the temperature measuring sensor 20, and the detected temperature is indicated by a temperature instruction. When the temperature is measured by the setting device 21 and this temperature reaches the cavitation generation temperature set in the temperature instruction setting device 21, the temperature instruction setting device 21 transmits a cavitation generation temperature arrival signal to the sequence controller 12.

シーケンス制御器12がキャビテーション発生温度到達
信号を受信すると、シーケンス制御器12のポンプ再予
冷シーケンスにより、液化ガス加圧ポンプ17を停止す
るとともに、送液用の自動弁19を閉じ、パージ用の自
動弁15を開いて該ポンプ17の再予冷を開始する。
When the sequence controller 12 receives the cavitation generation temperature reaching signal, the pump re-precooling sequence of the sequence controller 12 stops the liquefied gas pressurizing pump 17, closes the automatic liquid feeding valve 19, and automatically purges the gas. The valve 15 is opened and the re-precooling of the pump 17 is started.

この再予冷により、液化ガス加圧ポンプ17が予冷完了
温度までに冷却されると、前記同様のシーケンス制御器
12の予冷完了シーケンスにより、パージ用の自動弁1
5が閉じ、液化ガス加圧ポンプ17が起動するととも
に、送液用の自動弁19が開いて超低温液化ガスの供給
が再び開始される。
When the liquefied gas pressurizing pump 17 is cooled to the pre-cooling completion temperature by this re-pre-cooling, the automatic purge valve 1 is purged by the pre-cooling completion sequence of the sequence controller 12 similar to the above.
5 is closed, the liquefied gas pressurizing pump 17 is started, the automatic valve 19 for liquid transfer is opened, and the supply of the ultra-low temperature liquefied gas is restarted.

このように、液化ガス加圧ポンプ17の吐出側の温度と
キャビテーション発生温度とを温度指示設定器21で比
較することによって、シーケンス制御器12にキャビテ
ーション発生温度到達信号を送り、シーケンス制御器1
2により、液化ガス加圧ポンプ17の運転を停止して、
送液用の自動弁19を閉じ、バージ用の自動弁15を開
いて再予冷を行うので、液化ガス加圧ポンプ17の運転
の続行中に該ポンプ17内の温度が上昇しても、キャビ
テーションの発生前に該ポンプ17の運転を停止するこ
とができ、キャビテーションに起因する空打を防止でき
る。
In this way, by comparing the temperature on the discharge side of the liquefied gas pressurizing pump 17 and the cavitation generation temperature with the temperature instruction setting device 21, the cavitation generation temperature reaching signal is sent to the sequence controller 12, and the sequence controller 1
2, the operation of the liquefied gas pressure pump 17 is stopped,
Since the automatic valve 19 for liquid transfer is closed and the automatic valve 15 for barge is opened for re-precooling, even if the temperature inside the liquefied gas pressurizing pump 17 rises during the operation of the liquefied gas pressurizing pump 17, cavitation is increased. It is possible to stop the operation of the pump 17 before the occurrence of, and it is possible to prevent idling due to cavitation.

さらに、液化ガス加圧ポンプ17の運転を停止した後、
引続き再予冷を開始するので、安全確保及び省力化を図
りながら自動的に超低温液化ガスを再び供給することが
できる。
Furthermore, after stopping the operation of the liquefied gas pressure pump 17,
Since re-precooling is subsequently started, the ultra-low temperature liquefied gas can be automatically supplied again while ensuring safety and saving labor.

以上のように、シーケンス制御器12は、温度指示設定
器21からの予冷完了温度到達信号及びキャビテーショ
ン発生温度到達信号を受信して、温度制御による予冷完
了シーケンス及びポンプ再予冷シーケンスを行うもので
あるが、その他に、以下に示す圧力制御によるポンプ停
止シーケンス及びポンプ再起動シーケンス等も行ってい
る。
As described above, the sequence controller 12 receives the precooling completion temperature reaching signal and the cavitation generation temperature reaching signal from the temperature instruction setting device 21, and performs the precooling completion sequence and the pump reprecooling sequence by temperature control. However, in addition, the following pump stop sequence and pump restart sequence by pressure control are also performed.

即ち、液化ガス加圧ポンプ17から吐出され、送ガス気
化器22で気化して高圧ガス充填設備24に送られた気
化ガスは、圧力センサ28,29により高圧ガス容器2
5内の圧力を検知されて、自動弁30,31の切替で自
動的に高圧ガス容器25に充填される。一方、超低温液
化ガス充填設備23に送液された超低温液化ガスは、液
面検知用リミットスイッチ32,33により自動弁3
4,35を切換て自動的に超低温液化ガス容器(図示せ
ず)に充填される。
That is, the vaporized gas discharged from the liquefied gas pressurizing pump 17, vaporized by the gas vaporizer 22 and sent to the high pressure gas filling facility 24 is pressurized by the pressure sensors 28 and 29.
The pressure inside 5 is detected, and the high pressure gas container 25 is automatically filled by switching the automatic valves 30 and 31. On the other hand, the ultra-low temperature liquefied gas sent to the ultra-low temperature liquefied gas filling equipment 23 is automatically controlled by the liquid level detection limit switches 32 and 33.
4, 5 and 35 are switched to automatically fill an ultra-low temperature liquefied gas container (not shown).

そして、これらの充填中に、充填系統の配管内圧力が設
定圧力以上に上昇すると、圧力センサ36,37からの
ボンプ停止信号を受信して、シーケンス制御器12のポ
ンプ停止シーケンスにより自動的に液化ガス加圧ポンプ
17の運転が停止され、停止と同時に自動弁13,1
8,19が閉じ、パージ用の自動弁15が開いて自動弁
13から自動弁18及び自動弁13から送液用の自動弁
19間の系内圧力を放出し、充填が中断される。
When the pressure in the piping of the filling system rises above the set pressure during these fillings, a pump stop signal from the pressure sensors 36 and 37 is received, and liquefaction is automatically performed by the pump stop sequence of the sequence controller 12. The operation of the gas pressurizing pump 17 is stopped, and at the same time as the stop, the automatic valves 13, 1
8 and 19 are closed, the automatic purge valve 15 is opened, the internal system pressure between the automatic valve 13 and the automatic valve 18 and the automatic valve 13 for liquid delivery is released from the automatic valve 13, and the filling is interrupted.

充填設備23,24系統の配管内圧力が設定値以下にな
ると、圧力センサ36,37からのポンプ再起動信号を
受信して、シーケンス制御器12のポンプ再起動シーケ
ンスにより自動的に自動弁13,18が開となり、液化
ガス加圧ポンプ17の予冷が開始され、上述した予冷操
作を行って、超低温液化ガスの供給が再び行われる。
When the pressure in the piping of the filling equipment 23, 24 system becomes equal to or lower than the set value, a pump restart signal from the pressure sensors 36, 37 is received, and the automatic valve 13, automatically by the pump restart sequence of the sequence controller 12, 18 is opened, precooling of the liquefied gas pressurizing pump 17 is started, the above-described precooling operation is performed, and the ultra low temperature liquefied gas is supplied again.

〔発明の効果〕〔The invention's effect〕

本発明は上記のように、超低温液化ガス貯槽の超低温液
化ガスを液化ガス加圧ポンプによりボンベ等の容器に加
圧供給するに際し、液化ガス加圧ポンプの吐出側に設け
た温度測定センサにより液化ガス加圧ポンプ内の温度を
検知し、この検知した温度を、予冷完了温度及びキャビ
テーション発生温度を予め設定した温度指示設定器で測
温し、前記各設定温度への到達を検出してシーケンス制
御器に送信するとともに、シーケンス制御器は、予冷完
了温度到達信号を受信したときに液化ガス加圧ポンプの
予冷終了操作,該ポンプの起動,送液用の弁操作を含む
予冷完了シーケンスを行い、キャビテーション発生温度
到達信号を受信したときに液化ガス加圧ポンプの停止,
バージ用の弁操作,該ポンプの予冷開始を含むポンプ再
予冷シーケンスを行うようにしたので、液化ガス加圧ポ
ンプを超低温液化ガスの無駄なく確実に予冷することが
でき、該ポンプの予冷不足によるキャビテーションの発
生を防止でき、かつ、液化ガス加圧ポンプの運転の続行
中に該ポンプ内の温度が上昇しても、キャビテーション
の発生前に該ポンプの運転を停止することができ、キャ
ビテーションに起因する空打を防止でき、しかも、液化
ガス加圧ポンプの運転を停止した後、引続き再予冷を開
始することにより、安全確保及び省力化を図りながら自
動的に超低温液化ガスを再び供給することができる。
INDUSTRIAL APPLICABILITY As described above, the present invention liquefies the ultra low temperature liquefied gas in the ultra low temperature liquefied gas storage tank by pressurizing and supplying it to a container such as a cylinder by the liquefied gas pressure pump by using a temperature measurement sensor provided on the discharge side of the liquefied gas pressure pump. The temperature inside the gas pressurizing pump is detected, and the detected temperature is measured by a temperature indicator setting device that sets the precooling completion temperature and the cavitation generation temperature in advance. The sequence controller performs a precooling completion sequence including precooling ending operation of the liquefied gas pressurizing pump, starting of the pump, and valve operation for liquid transfer when the precooling completion temperature reaching signal is received. When the cavitation generation temperature arrival signal is received, the liquefied gas pressure pump is stopped,
Since the pump re-precooling sequence including the valve operation for the barge and the start of precooling of the pump is performed, the liquefied gas pressurizing pump can be surely precooled without waste of ultra-low temperature liquefied gas, and the precooling of the pump is insufficient. The occurrence of cavitation can be prevented, and even if the temperature inside the liquefied gas pressure pump rises during the operation of the pump, the operation of the pump can be stopped before the occurrence of cavitation. In addition, it is possible to prevent re-cooling and to automatically supply the ultra-low temperature liquefied gas again while ensuring safety and saving labor by stopping the operation of the liquefied gas pressurizing pump and continuing the re-precooling. it can.

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明に係る超低温液化ガス供給方法の一実施
例を示す配管系統図、第2図は従来の超低温液化ガス供
給方法の配管系統図である。 12……シーケンス制御器、13,14,18……自動
弁、15……パージ用の自動弁、16……超低温液化ガ
ス貯槽、17……液化ガス加圧ポンプ、19……送液用
の自動弁、20……温度測定センサ、21……温度指示
設定器、22……送ガス気化器、23……超低温液化ガ
ス充填設備、24……高圧ガス充填設備、25……高圧
ガス容器
FIG. 1 is a piping system diagram showing an embodiment of an ultra-low temperature liquefied gas supply method according to the present invention, and FIG. 2 is a piping system diagram of a conventional ultra-low temperature liquefied gas supply method. 12 ... Sequence controller, 13, 14, 18 ... Automatic valve, 15 ... Automatic valve for purging, 16 ... Ultra low temperature liquefied gas storage tank, 17 ... Liquefied gas pressurizing pump, 19 ... For liquid transfer Automatic valve, 20 ... Temperature measuring sensor, 21 ... Temperature indication setting device, 22 ... Gas vaporizer, 23 ... Ultra low temperature liquefied gas filling facility, 24 ... High pressure gas filling facility, 25 ... High pressure gas container

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】超低温液化ガス貯槽の超低温液化ガスを液
化ガス加圧ポンプによりボンベ等の容器に加圧供給する
超低温液化ガス供給方法において、前記液化ガス加圧ポ
ンプの吐出側に設けた温度測定センサにより液化ガス加
圧ポンプ内の温度を検知し、この検知した温度を、予冷
完了温度及びキャビテーション発生温度を予め設定した
温度指示設定器で測温し、前記各設定温度への到達を検
出してシーケンス制御器に送信するとともに、該シーケ
ンス制御器は、予冷完了温度到達信号を受信したときに
液化ガス加圧ポンプの予冷終了操作,該ポンプの起動,
送液用の弁操作を含む予冷完了シーケンスを行い、キャ
ビテーション発生温度到達信号を受信したときに液化ガ
ス加圧ポンプの停止,パージ用の弁操作,該ポンプの予
冷開始を含むポンプ再予冷シーケンスを行うことを特徴
とする超低温液化ガス供給方法。
1. A method for supplying ultra-low temperature liquefied gas from an ultra-low temperature liquefied gas storage tank to a container such as a cylinder under pressure by means of a liquefied gas pressure pump, in which a temperature measurement is provided on the discharge side of the liquefied gas pressure pump. The temperature inside the liquefied gas pressurizing pump is detected by the sensor, and the detected temperature is measured by the temperature instruction setter that sets the precooling completion temperature and the cavitation generation temperature in advance, and the arrival at each of the set temperatures is detected. And transmits to the sequence controller, the sequence controller, when receiving the precooling completion temperature reaching signal, terminates the precooling of the liquefied gas pressurizing pump, starts the pump,
A precooling completion sequence including a valve operation for liquid transfer is performed, and when a cavitation generation temperature reaching signal is received, a liquefied gas pressurizing pump is stopped, a valve operation for purging is performed, and a pump reprecooling sequence including precooling start of the pump is performed. A method for supplying ultra-low temperature liquefied gas, which is characterized in that it is performed.
JP18542385A 1985-08-23 1985-08-23 Ultra low temperature liquefied gas supply method Expired - Lifetime JPH0633860B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18542385A JPH0633860B2 (en) 1985-08-23 1985-08-23 Ultra low temperature liquefied gas supply method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18542385A JPH0633860B2 (en) 1985-08-23 1985-08-23 Ultra low temperature liquefied gas supply method

Publications (2)

Publication Number Publication Date
JPS6246098A JPS6246098A (en) 1987-02-27
JPH0633860B2 true JPH0633860B2 (en) 1994-05-02

Family

ID=16170528

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18542385A Expired - Lifetime JPH0633860B2 (en) 1985-08-23 1985-08-23 Ultra low temperature liquefied gas supply method

Country Status (1)

Country Link
JP (1) JPH0633860B2 (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5360139A (en) * 1993-01-22 1994-11-01 Hydra Rig, Inc. Liquified natural gas fueling facility
JP2002054795A (en) * 2000-08-08 2002-02-20 Asahi Eng Co Ltd Liquefied gas pressurizer
JP2005299819A (en) * 2004-04-13 2005-10-27 Iwatani Internatl Corp Low-temperature liquefied gas filling device
JP5997122B2 (en) * 2013-10-15 2016-09-28 トヨタ自動車株式会社 Low temperature liquefied gas supply device and method
CN109538931A (en) * 2018-12-11 2019-03-29 米亚索乐装备集成(福建)有限公司 Control method, system and the gas supply system of anti-supercharging device cavitation
CN114046441B (en) * 2021-10-29 2023-08-15 济南华信流体控制有限公司 Automatic pressurization system for low-temperature liquefied gas
CN116293422B (en) * 2023-03-03 2024-09-24 查特深冷工程系统(常州)有限公司 Cryogenic liquid high-pressure gasification system with instant start function and control method

Also Published As

Publication number Publication date
JPS6246098A (en) 1987-02-27

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