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JP4437575B2 - Equipment and method for intermittent operation of low boiling point liquid pump - Google Patents
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JP4437575B2 - Equipment and method for intermittent operation of low boiling point liquid pump - Google Patents

Equipment and method for intermittent operation of low boiling point liquid pump Download PDF

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Publication number
JP4437575B2
JP4437575B2 JP30171999A JP30171999A JP4437575B2 JP 4437575 B2 JP4437575 B2 JP 4437575B2 JP 30171999 A JP30171999 A JP 30171999A JP 30171999 A JP30171999 A JP 30171999A JP 4437575 B2 JP4437575 B2 JP 4437575B2
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liquid
liquid level
low
pump
low boiling
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JP2001123964A (en
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康雄 国府田
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IHI Corp
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IHI Corp
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Description

【0001】
【発明の属する技術分野】
本発明は、低沸点液用ポンプを間欠運転する間欠運転設備とその方法に関する。
【0002】
【従来の技術】
LNG,LPG等(以下、低沸点液と呼ぶ)を扱う貯蔵設備や化学プラントでは、配管の保冷等のために、低沸点液を常時少量流す場合がある。この場合、図4(A)に例示するような気密容器(ドラム)を設け、このドラム1に保冷等に用いた低沸点液を低沸点液ライン2から常時流入させて一時的に貯め、ドラム内の液面が所定の高い液位H(レベルH)に達した時点で低沸点液用ポンプ3を起動し、所定の低い液位L(レベルL)まで下がった時点でポンプを停止する間欠運転を行う場合がある。なお、この場合、レベルH、Lは例えば液位センサ4を用いて検出する。
【0003】
【発明が解決しようとする課題】
上述した低沸点液用ポンプの間欠運転では、ポンプ停止から再起動までの時間が長いと、その間の入熱により低沸点液全体が飽和状態に近い状態になっているため、ポンプ起動時にキャビテーションが発生してポンプトリップが発生しやすい問題点があった。
【0004】
すなわち、インペラの回転によりインペラの周囲に低圧部分(例えばまわりより100mmAq程度低い部分)が必ず生じるため、ポンプの確実な起動のためには、この低圧部分で低沸点液が気化しないように、その部分の気化圧力(飽和圧力)より大きい静圧が作用している必要がある。この静圧に相当する液圧又は液深をNPSH(Net Positive Suction Head)と呼ぶ。
【0005】
しかし、LNG,LPG等の低沸点液をドラム内で長時間保持すると、図4(B)に示すように、深い位置にある低沸点液であってもその位置の液圧(図で実線)に相当する飽和圧力(図で破線)に近い状態になっているため、低沸点液全体が飽和状態に近い状態にあり、インペラが回転してインペラの周囲に低圧部分が生じると、その部分が必ずその部分の飽和圧力より低くなってしまい、キャビテーションが発生してしまう。
【0006】
そのため、従来の低沸点液用ポンプの間欠運転では、ポンプ停止から再起動までの時間が長いほど、ポンプトリップが発生しやすく、ある程度の頻度でトリップが発生した。
【0007】
従って、ポンプトリップを本質的に回避するためには、ライン2から常時流入する低沸点液の流量にバランスする吐出量のポンプを選定し、これを連続運転する必要があった。しかし、この場合には、連続運転コストがかかるばかりでなく、流入する低沸点液の流量が少量すぎる場合にはポンプの容量に応じた低沸点液の供給をあえて行う必要があった。
【0008】
本発明はかかる問題点を解決するために創案されたものである。すなわち、本発明の目的は、低沸点液を常時流入させて一時的に貯め、これをポンプトリップを引き起こすことなく確実にポンプを間欠運転させて排出することができる低沸点液用ポンプの間欠運転設備とその方法を提供することにある。
【0009】
【課題を解決するための手段】
本発明によれば、所定の低沸点液ライン(2)から常時流入する低沸点液を一時的に貯めるための気密容器(1)と、該気密容器内の低沸点液を排出するための低沸点液用ポンプ(3)と、気密容器内の高低の液位を検出して排出するための液位センサー(4)とを備え、液位が所定の高液位Hに達した時点で低沸点液用ポンプを起動し、所定の低液位Lまで下がった時点でポンプを停止する低沸点液用ポンプの間欠運転設備において、
開閉弁(11)を有し気密容器(1)に低沸点液を供給する補給ライン(12)と、前記高液位Hよりも低い中間液位Mを検出する中間液位センサー(14)と、開閉弁(11)を制御する制御装置(16)とを備え、該制御装置により、中間液位Mを検出しかつ低沸点液用ポンプの停止中に、前記補給ラインより低沸点液を短時間に供給し、液位が高液位Hに達した時点で供給を停止し、
前記中間液位Mは、高液位Hとの液圧差がインペラの回転により生じる負圧よりも大きく設定されている、ことを特徴とする低沸点液用ポンプの間欠運転設備が提供される。
【0010】
また、本発明によれば、所定の低沸点液ライン(2)から常時流入する低沸点液を一時的に貯めるための気密容器(1)と、該気密容器内の低沸点液を排出するための低沸点液用ポンプ(3)と、気密容器内の高低の液位を検出して排出するための液位センサー(4)とを備え、液位が所定の高液位Hに達した時点で低沸点液用ポンプを起動し、所定の低液位Lまで下がった時点でポンプを停止する低沸点液用ポンプの間欠運転方法において、
開閉弁(11)を有し気密容器(1)に低沸点液を供給する補給ライン(12)と、前記高液位Hよりも低い中間液位Mを検出する中間液位センサー(14)とを備え、中間液位Mを検出しかつ低沸点液用ポンプの停止中に、前記補給ラインより低沸点液を短時間に供給し、液位が高液位Hに達した時点で供給を停止し、
前記中間液位Mは、高液位Hとの液圧差がインペラの回転により生じる負圧よりも大きく設定されている、ことを特徴とする低沸点液用ポンプの間欠運転方法が提供される。
【0011】
本発明の好ましい実施形態によれば、前記補給ライン(12)の流量は、低沸点液ライン(2)の流量より十分に大きく設定されている
【0012】
上記本発明の装置及び方法によれば、気密容器(1)内の液位が所定の高い液位Hに達する前に、中間液位センサー(14)で高液位Hよりも低い中間液位Mを検出して、制御装置(16)により開閉弁(11)を開き補給ライン(12)から低沸点液を短時間に高液位Hまで供給(補給)することができる。この補給により、気密容器(1)内の液位が高液位Hと中間液位Mとの差の分上昇するので、補給前にあった低沸点液の圧力がその分上昇し、補給前に低沸点液全体が飽和状態に近い状態にある場合でも全体が上昇液位分高くなり、過冷却状態となる。従って、インペラが回転してインペラの周囲に低圧部分が生じても、その部分を飽和圧力より高く維持でき、キャビテーションの発生を防止することができる。
【0013】
【発明の実施の形態】
以下本発明の好ましい実施形態について図面を参照して説明する。なお、各図において共通する部分には同一の符号を付し、重複した説明を省略する。
【0014】
図1は、本発明による低沸点液用ポンプの間欠運転設備の全体構成図である。この図に示すように、本発明の間欠運転設備10は、気密容器1(ドラム)、低沸点液用ポンプ3及び液位センサー4を備える。気密容器1は、十分に保冷された容器であり、低沸点液ライン2から常時流入する低沸点液を一時的に貯めるようになっている。この低沸点液は、例えば、LNG,LPG等であり、配管の保冷等のために常時少量流したその残量(未気化分)である。従って、気密容器1に流入した時点で、低沸点液の一部は既に気化し、図示しないガスラインからBOG処理設備に供給されるようになっている。
【0015】
また、低沸点液用ポンプ3は、低沸点液ライン2から常時流入する低沸点液の流量よりも十分に大きい吐出量を有し、気密容器1内の低沸点液を所定の高液位Hから低液位Lまで短時間に排出できるようになっている。
【0016】
更に、液位センサー4は、気密容器1内の高低H,Lの液位を検出するセンサーである。この液位センサー4は、例えばフロート式、静電容量式、差圧式等であり、高液位H及び低液位Lで制御信号を出力できるようになっている。この構成により、後述する制御装置又は別の独立した制御装置により、気密容器1内の液位が所定の高液位Hに達した時点で低沸点液用ポンプ3を起動し、所定の低液位Lまで下がった時点でポンプ3を停止する。
【0017】
本発明の低沸点液用ポンプの間欠運転設備10は、更に、補給ライン12、中間液位センサー14及び制御装置16を備える。補給ライン12は、図示しない低沸点液ラインから低沸点液を独立に供給するようになっている。このラインから供給される低沸点液は、十分に冷却され飽和温度より低い過冷却状態になっているのが好ましい。
また補給ライン12には遠隔操作が可能な開閉弁11(例えば、電磁弁)が設けられている。更に、この開閉弁11を開いた場合に、補給ライン12の流量が低沸点液ライン2の流量より十分に大きくなるように設定されている。この補給ライン12の流量は、後述する補給により中間液位Mから高液位Hに達する間に、その前に気密容器1内あった低沸点液が再び飽和状態にならないような流量に設定する。
【0018】
中間液位センサー14は、前述した低液位Lよりは高く、高液位Hよりは低く中間液位Mを検出するようになっている。この中間液位Mは、高液位Hとの液圧差ΔPがインペラの回転により生じる負圧よりも十分大きく(例えば、300mmAq以上に)設定されている。なお、この中間液位センサー14は、液位センサー4と同様に、例えばフロート式、静電容量式、差圧式等であり、中間液位Hで制御信号を出力できるようになっている。
【0019】
制御装置16は、少なくとも中間液位センサー14の制御信号を受け、開閉弁11を開閉制御するようになっている。すなわち、この制御装置16により、低沸点液用ポンプ3の停止中に、中間液位センサー14により中間液位Mを検出すると、その制御信号を受けて開閉弁11を全開し補給ライン12より低沸点液を供給し、短時間に液位が高液位Hに達した時点で開閉弁11を全閉して供給を停止する。なお、低沸点液用ポンプ3の運転中には、中間液位センサー14により中間液位Mを検出しても、この制御を行わず、開閉弁11を全閉に保持したままにするように、インターロックが設けられている。
また、この例では、制御装置16により、上述した液位センサー4の制御信号を受け、低沸点液用ポンプ3の起動・停止も制御する。
【0020】
図2は、本発明の間欠運転方法のフロー図である。この図に示すように、本発明の低沸点液用ポンプの間欠運転方法は、(1)中間液位Mを検出しかつ低沸点液用ポンプ3の停止中に、補給ライン12より低沸点液を短時間に供給し、液位が高液位Hに達した時点で供給を停止する補給ステップS1と、(2)液位が所定の高液位Hに達した時点で低沸点液用ポンプ3を起動し、所定の低液位Lまで下がった時点でポンプ3を停止する排出ステップS2とからなる。
通常の作動状態では、所定の低沸点液ライン2から気密容器1内に低沸点液が常時少量流入する「待機状態」が長く続いた後、補給ステップS1が始まり、次いで排出ステップS2が行われる。その後、最初の待機状態に戻り、これが繰り返して行われる。
【0021】
図3は、本発明の間欠運転方法における低沸点液の液圧変化を示す説明図である。LNG,LPG等の低沸点液をドラム内で長時間保持すると、図3に示すように、深い位置にある低沸点液であってもその位置の液圧(図で実線Aで示す)に相当する飽和圧力(図で破線で示す)に近い状態になっているため、低沸点液全体が飽和状態に近い状態にある。従って、この状態でインペラが回転しインペラの周囲に低圧部分が生じると、その部分が必ずその部分の飽和圧力より低くなってしまい、キャビテーションが発生してしまう。
【0022】
上述した本発明の装置及び方法によれば、この状態で低沸点液が徐々に増加し、気密容器1内の液位が高液位Hよりも低い中間液位Mに達すると、制御装置16により開閉弁11を開き補給ライン12から低沸点液が短時間に高液位Hまで供給(補給)される。この補給により、気密容器1内の液位が高液位Hと中間液位Mとの差ΔPの分上昇するので、図に実線Bで示すように、補給前にあった低沸点液の圧力がその分上昇し、過冷却状態となる。従って、インペラが回転してインペラの周囲に低圧部分が生じても、その部分を飽和圧力より高く維持でき、キャビテーションの発生を防止することができる。
【0023】
なお本発明は以上述べた実施形態に限定されるものではなく、発明の要旨を逸脱しない範囲で種々の変更が可能である。
【0024】
【発明の効果】
上述したように、本発明により、間欠運転ポンプの安定起動が得られ、かつ連続運転よりも運転コストの低減が図れる。すなわち、本発明の低沸点液用ポンプの間欠運転設備とその方法は、低沸点液を常時流入させて一時的に貯め、これをポンプトリップを引き起こすことなく確実にポンプを間欠運転させて排出することができる、等の優れた効果を有する。
【図面の簡単な説明】
【図1】本発明による低沸点液用ポンプの間欠運転設備の全体構成図である。
【図2】本発明の間欠運転方法のフロー図である。
【図3】本発明における低沸点液の液圧変化を示す説明図である。
【図4】従来の間欠運転手段の説明図である。
【符号の説明】
1 気密容器(ドラム)
2 低沸点液ライン
3 低沸点液用ポンプ
4 液位センサ
10 間欠運転設備
11 開閉弁
12 補給ライン
14 中間液位センサー
16 制御装置
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an intermittent operation facility for intermittently operating a low boiling point liquid pump and a method therefor.
[0002]
[Prior art]
In storage facilities and chemical plants that handle LNG, LPG, etc. (hereinafter referred to as low-boiling liquid), a small amount of low-boiling liquid may be allowed to flow constantly for the purpose of keeping pipes cold. In this case, an airtight container (drum) as illustrated in FIG. 4A is provided, and the low-boiling liquid used for cold storage or the like is always allowed to flow into the drum 1 from the low-boiling liquid line 2 to be temporarily stored. The low boiling liquid pump 3 is started when the liquid level in the inside reaches a predetermined high liquid level H (level H), and the pump is stopped when the liquid level drops to a predetermined low liquid level L (level L). There is a case of driving. In this case, the levels H and L are detected using the liquid level sensor 4, for example.
[0003]
[Problems to be solved by the invention]
In the intermittent operation of the low-boiling liquid pump described above, if the time from the pump stop to restart is long, the entire low-boiling liquid is close to saturation due to heat input during that time, so cavitation occurs when the pump is started. There was a problem that the pump trip occurred easily.
[0004]
That is, since the impeller rotation always causes a low pressure portion around the impeller (for example, a portion lower by about 100 mmAq than the surroundings), in order to start the pump reliably, the low boiling point liquid is not vaporized at this low pressure portion. It is necessary that a static pressure larger than the vaporization pressure (saturation pressure) of the part is acting. The fluid pressure or fluid depth corresponding to this static pressure is called NPSH (Net Positive Suction Head).
[0005]
However, when a low boiling point liquid such as LNG or LPG is held in the drum for a long time, as shown in FIG. 4B, even if the low boiling point liquid is in a deep position, the liquid pressure at that position (solid line in the figure) Since the entire low boiling point liquid is in a state close to saturation, and the impeller rotates and a low pressure part is generated around the impeller, that part is It always becomes lower than the saturation pressure of the part, and cavitation occurs.
[0006]
Therefore, in the intermittent operation of the conventional low boiling liquid pump, the longer the time from the pump stop to the restart, the more likely the pump trip occurs, and the trip occurred at a certain frequency.
[0007]
Therefore, in order to essentially avoid the pump trip, it is necessary to select a pump with a discharge amount that balances the flow rate of the low-boiling liquid constantly flowing from the line 2 and to continuously operate the pump. However, in this case, not only the continuous operation cost is required, but when the flow rate of the low boiling liquid flowing in is too small, it is necessary to dare to supply the low boiling liquid according to the capacity of the pump.
[0008]
The present invention has been made to solve such problems. That is, an object of the present invention is to intermittently operate a low-boiling-point liquid pump that allows a low-boiling point liquid to always flow in and temporarily store it and reliably discharge the pump without causing a pump trip. It is to provide facilities and methods.
[0009]
[Means for Solving the Problems]
According to the present invention, an airtight container (1) for temporarily storing a low boiling point liquid that always flows from a predetermined low boiling point liquid line (2), and a low pressure point for discharging the low boiling point liquid in the airtight container. A boiling-point liquid pump (3) and a liquid level sensor (4) for detecting and discharging the high and low liquid levels in the hermetic container are provided, and the liquid level is low when the liquid level reaches a predetermined high liquid level H. In the intermittent operation equipment of the low boiling liquid pump that starts the boiling liquid pump and stops the pump when it has fallen to a predetermined low liquid level L,
A replenishment line (12) having an on-off valve (11) for supplying a low boiling point liquid to the hermetic container (1), an intermediate liquid level sensor (14) for detecting an intermediate liquid level M lower than the high liquid level H, And a control device (16) for controlling the on-off valve (11). The control device detects the intermediate liquid level M and shortens the low-boiling point liquid from the replenishment line while the low-boiling point liquid pump is stopped. Supply at the time, stop the supply when the liquid level reaches the high liquid level H ,
The intermediate liquid level M is set such that the hydraulic pressure difference from the high liquid level H is set to be larger than the negative pressure generated by the rotation of the impeller, and intermittent operation equipment for a low boiling liquid pump is provided.
[0010]
Further, according to the present invention, the air-tight container (1) for temporarily storing the low-boiling liquid that always flows from the predetermined low-boiling liquid line (2), and the low-boiling liquid in the air-tight container are discharged. When the liquid level reaches a predetermined high liquid level H, the low boiling liquid pump (3) and the liquid level sensor (4) for detecting and discharging the high and low liquid levels in the hermetic container In the intermittent operation method of the low-boiling-point liquid pump that starts the low-boiling-point liquid pump and stops the pump when the pump reaches a predetermined low liquid level L,
A replenishment line (12) having an on-off valve (11) for supplying a low boiling point liquid to the hermetic container (1), an intermediate liquid level sensor (14) for detecting an intermediate liquid level M lower than the high liquid level H, The low boiling point liquid is supplied from the replenishment line in a short time while the intermediate liquid level M is detected and the pump for the low boiling point liquid is stopped, and the supply is stopped when the liquid level reaches the high liquid level H. And
The intermediate liquid level M is set such that the hydraulic pressure difference from the high liquid level H is set to be larger than the negative pressure generated by the rotation of the impeller, and the intermittent operation method of the low boiling liquid pump is provided.
[0011]
According to a preferred embodiment of the present invention, the flow rate of the supply line (12) is set from sufficiently large flow of low-boiling fluid line (2).
[0012]
According to the apparatus and method of the present invention, the intermediate liquid level lower than the high liquid level H by the intermediate liquid level sensor (14) before the liquid level in the airtight container (1) reaches the predetermined high liquid level H. M is detected, and the control device (16) opens the on-off valve (11) to supply (supplement) the low boiling point liquid from the replenishment line (12) to the high liquid level H in a short time. By this replenishment, the liquid level in the airtight container (1) increases by the difference between the high liquid level H and the intermediate liquid level M, so the pressure of the low boiling point liquid before replenishment rises by that amount, and before replenishment. Even when the entire low-boiling liquid is in a state close to saturation, the whole becomes high by the rising liquid level, and is in a supercooled state. Therefore, even if the impeller rotates and a low pressure portion is generated around the impeller, the portion can be maintained higher than the saturation pressure, and cavitation can be prevented.
[0013]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, preferred embodiments of the present invention will be described with reference to the drawings. In addition, the same code | symbol is attached | subjected to the common part in each figure, and the overlapping description is abbreviate | omitted.
[0014]
FIG. 1 is an overall configuration diagram of intermittent operation equipment for a low boiling point liquid pump according to the present invention. As shown in this figure, the intermittent operation equipment 10 of the present invention includes an airtight container 1 (drum), a low boiling point liquid pump 3 and a liquid level sensor 4. The airtight container 1 is a sufficiently cooled container, and temporarily stores a low-boiling liquid that always flows from the low-boiling liquid line 2. The low boiling point liquid is, for example, LNG, LPG or the like, and is the remaining amount (unvaporized portion) that is always supplied in a small amount for keeping the pipe cold. Therefore, at the time of flowing into the airtight container 1, a part of the low boiling point liquid is already vaporized and supplied to the BOG processing facility from a gas line (not shown).
[0015]
The low-boiling liquid pump 3 has a discharge amount sufficiently larger than the flow rate of the low-boiling liquid that always flows from the low-boiling liquid line 2, and the low-boiling liquid in the hermetic container 1 is discharged to a predetermined high liquid level H. To a low liquid level L in a short time.
[0016]
Further, the liquid level sensor 4 is a sensor that detects the high and low H and L liquid levels in the airtight container 1. The liquid level sensor 4 is, for example, a float type, a capacitance type, a differential pressure type or the like, and can output a control signal at a high liquid level H and a low liquid level L. With this configuration, when the liquid level in the hermetic container 1 reaches a predetermined high liquid level H by the control device described later or another independent control device, the low boiling point liquid pump 3 is started, and the predetermined low liquid The pump 3 is stopped at the time when it has lowered to the position L.
[0017]
The intermittent operation equipment 10 for the low boiling point liquid pump of the present invention further includes a replenishment line 12, an intermediate liquid level sensor 14, and a control device 16. The replenishment line 12 supplies a low boiling point liquid independently from a low boiling point liquid line (not shown). The low boiling point liquid supplied from this line is preferably sufficiently cooled and in a supercooled state lower than the saturation temperature.
The replenishment line 12 is provided with an on-off valve 11 (for example, a solenoid valve) that can be operated remotely. Further, when the on-off valve 11 is opened, the flow rate of the replenishment line 12 is set to be sufficiently larger than the flow rate of the low boiling liquid line 2. The flow rate of the replenishment line 12 is set such that the low-boiling point liquid in the hermetic container 1 before reaching the high liquid level H by replenishment to be described later does not become saturated again. .
[0018]
The intermediate liquid level sensor 14 is configured to detect the intermediate liquid level M that is higher than the low liquid level L and lower than the high liquid level H. This intermediate liquid level M is set such that the hydraulic pressure difference ΔP with respect to the high liquid level H is sufficiently larger than the negative pressure generated by the rotation of the impeller (for example, 300 mmAq or more). The intermediate liquid level sensor 14 is, for example, a float type, a capacitance type, a differential pressure type, etc., like the liquid level sensor 4, and can output a control signal at the intermediate liquid level H.
[0019]
The control device 16 receives at least a control signal from the intermediate liquid level sensor 14 and controls opening / closing of the on-off valve 11. That is, when the intermediate liquid level M is detected by the intermediate liquid level sensor 14 while the low boiling point liquid pump 3 is stopped by the control device 16, the control valve 16 receives the control signal and fully opens the on-off valve 11. The boiling liquid is supplied, and when the liquid level reaches the high liquid level H in a short time, the on-off valve 11 is fully closed to stop the supply. During the operation of the low-boiling liquid pump 3, even if the intermediate liquid level M is detected by the intermediate liquid level sensor 14, this control is not performed and the on-off valve 11 is kept fully closed. Interlock is provided.
Further, in this example, the control device 16 receives the control signal of the liquid level sensor 4 described above, and controls the start / stop of the low boiling point liquid pump 3.
[0020]
FIG. 2 is a flowchart of the intermittent operation method of the present invention. As shown in this figure, the intermittent operation method of the low-boiling liquid pump of the present invention is as follows. (1) The low-boiling liquid is detected from the replenishment line 12 while the intermediate liquid level M is detected and the low-boiling liquid pump 3 is stopped. Is supplied in a short time, and the supply step S1 is stopped when the liquid level reaches the high liquid level H, and (2) the pump for the low boiling point liquid when the liquid level reaches the predetermined high liquid level H. 3 and a discharge step S2 in which the pump 3 is stopped at the time when the pressure drops to a predetermined low liquid level L.
In a normal operation state, after a “standby state” in which a small amount of low-boiling liquid always flows into the airtight container 1 from the predetermined low-boiling liquid line 2 continues for a long time, the replenishment step S1 starts, and then the discharge step S2 is performed. . Thereafter, the process returns to the initial standby state, and this is repeated.
[0021]
FIG. 3 is an explanatory view showing a change in the liquid pressure of the low boiling point liquid in the intermittent operation method of the present invention. When a low boiling point liquid such as LNG or LPG is held in the drum for a long time, as shown in FIG. 3, even a low boiling point liquid at a deep position corresponds to the liquid pressure at that position (shown by a solid line A in the figure). Since the pressure is close to the saturation pressure (shown by the broken line in the figure), the entire low-boiling point liquid is in a state close to saturation. Therefore, when the impeller rotates in this state and a low pressure portion is generated around the impeller, the portion always becomes lower than the saturation pressure of the portion, and cavitation occurs.
[0022]
According to the apparatus and method of the present invention described above, when the low boiling point liquid gradually increases in this state and the liquid level in the airtight container 1 reaches the intermediate liquid level M lower than the high liquid level H, the control device 16 Thus, the on-off valve 11 is opened, and the low boiling point liquid is supplied (supplemented) from the replenishment line 12 to the high liquid level H in a short time. By this replenishment, the liquid level in the hermetic container 1 is increased by the difference ΔP between the high liquid level H and the intermediate liquid level M. Therefore, as shown by the solid line B in the figure, the pressure of the low boiling point liquid before replenishment Rises by that amount and enters a supercooled state. Therefore, even if the impeller rotates and a low pressure portion is generated around the impeller, the portion can be maintained higher than the saturation pressure, and cavitation can be prevented.
[0023]
The present invention is not limited to the embodiments described above, and various modifications can be made without departing from the scope of the invention.
[0024]
【The invention's effect】
As described above, according to the present invention, stable startup of the intermittent operation pump can be obtained, and the operation cost can be reduced as compared with continuous operation. That is, the low boiling liquid pump intermittent operation equipment and method according to the present invention allows the low boiling liquid to always flow in and temporarily store it, and reliably discharge the pump without causing a pump trip. And so on.
[Brief description of the drawings]
FIG. 1 is an overall configuration diagram of intermittent operation equipment of a pump for low boiling point liquid according to the present invention.
FIG. 2 is a flowchart of the intermittent operation method of the present invention.
FIG. 3 is an explanatory diagram showing a change in hydraulic pressure of a low boiling point liquid in the present invention.
FIG. 4 is an explanatory diagram of conventional intermittent operation means.
[Explanation of symbols]
1 Airtight container (drum)
2 Low-boiling point liquid line 3 Low-boiling point liquid pump 4 Liquid level sensor 10 Intermittent operation equipment 11 On-off valve 12 Supply line 14 Intermediate liquid level sensor 16 Controller

Claims (3)

所定の低沸点液ライン(2)から常時流入する低沸点液を一時的に貯めるための気密容器(1)と、該気密容器内の低沸点液を排出するための低沸点液用ポンプ(3)と、気密容器内の高低の液位を検出して排出するための液位センサー(4)とを備え、液位が所定の高液位Hに達した時点で低沸点液用ポンプを起動し、所定の低液位Lまで下がった時点でポンプを停止する低沸点液用ポンプの間欠運転設備において、
開閉弁(11)を有し気密容器(1)に低沸点液を供給する補給ライン(12)と、前記高液位Hよりも低い中間液位Mを検出する中間液位センサー(14)と、開閉弁(11)を制御する制御装置(16)とを備え、該制御装置により、中間液位Mを検出しかつ低沸点液用ポンプの停止中に、前記補給ラインより低沸点液を短時間に供給し、液位が高液位Hに達した時点で供給を停止し、
前記中間液位Mは、高液位Hとの液圧差がインペラの回転により生じる負圧よりも大きく設定されている、ことを特徴とする低沸点液用ポンプの間欠運転設備。
An airtight container (1) for temporarily storing a low boiling liquid that always flows from a predetermined low boiling liquid line (2), and a low boiling liquid pump (3 for discharging the low boiling liquid in the airtight container) ) And a liquid level sensor (4) for detecting and discharging the high and low liquid levels in the hermetic container, and when the liquid level reaches a predetermined high liquid level H, the low boiling liquid pump is activated. In the intermittent operation equipment of the low-boiling-point liquid pump that stops the pump when it falls to a predetermined low liquid level L,
A replenishment line (12) having an on-off valve (11) for supplying a low boiling point liquid to the hermetic container (1), an intermediate liquid level sensor (14) for detecting an intermediate liquid level M lower than the high liquid level H, And a control device (16) for controlling the on-off valve (11). The control device detects the intermediate liquid level M and shortens the low-boiling point liquid from the replenishment line while the low-boiling point liquid pump is stopped. Supply at the time, stop the supply when the liquid level reaches the high liquid level H ,
The intermediate liquid level M is set to have a higher hydraulic pressure difference from the high liquid level H than a negative pressure generated by the rotation of the impeller .
前記補給ライン(12)の流量は、低沸点液ライン(2)の流量より十分に大きく設定されている、ことを特徴とする請求項1に記載の低沸点液用ポンプの間欠運転設備。The flow rate of the supply line (12) is sufficiently larger than the flow rate of the low-boiling fluid line (2), the intermittent operation equipment of low boiling liquid pump according to claim 1, characterized in that. 所定の低沸点液ライン(2)から常時流入する低沸点液を一時的に貯めるための気密容器(1)と、該気密容器内の低沸点液を排出するための低沸点液用ポンプ(3)と、気密容器内の高低の液位を検出して排出するための液位センサー(4)とを備え、液位が所定の高液位Hに達した時点で低沸点液用ポンプを起動し、所定の低液位Lまで下がった時点でポンプを停止する低沸点液用ポンプの間欠運転方法において、
開閉弁(11)を有し気密容器(1)に低沸点液を供給する補給ライン(12)と、前記高液位Hよりも低い中間液位Mを検出する中間液位センサー(14)とを備え、中間液位Mを検出しかつ低沸点液用ポンプの停止中に、前記補給ラインより低沸点液を短時間に供給し、液位が高液位Hに達した時点で供給を停止し、
前記中間液位Mは、高液位Hとの液圧差がインペラの回転により生じる負圧よりも大きく設定されている、ことを特徴とする低沸点液用ポンプの間欠運転方法。
An airtight container (1) for temporarily storing a low boiling liquid that always flows from a predetermined low boiling liquid line (2), and a low boiling liquid pump (3 for discharging the low boiling liquid in the airtight container) ) And a liquid level sensor (4) for detecting and discharging the high and low liquid levels in the hermetic container, and when the liquid level reaches a predetermined high liquid level H, the low boiling liquid pump is activated. In the intermittent operation method of the low-boiling-point liquid pump that stops the pump when the liquid level drops to a predetermined low liquid level L,
A replenishment line (12) having an on-off valve (11) for supplying a low boiling point liquid to the hermetic container (1), an intermediate liquid level sensor (14) for detecting an intermediate liquid level M lower than the high liquid level H, The low boiling point liquid is supplied from the replenishment line in a short time while the intermediate liquid level M is detected and the pump for the low boiling point liquid is stopped, and the supply is stopped when the liquid level reaches the high liquid level H. And
The intermediate liquid level M is set to have a higher hydraulic pressure difference from the high liquid level H than a negative pressure generated by the rotation of the impeller .
JP30171999A 1999-10-22 1999-10-22 Equipment and method for intermittent operation of low boiling point liquid pump Expired - Fee Related JP4437575B2 (en)

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