Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0333967B2 - - Google Patents
[go: Go Back, main page]

JPH0333967B2 - - Google Patents

Info

Publication number
JPH0333967B2
JPH0333967B2 JP1807983A JP1807983A JPH0333967B2 JP H0333967 B2 JPH0333967 B2 JP H0333967B2 JP 1807983 A JP1807983 A JP 1807983A JP 1807983 A JP1807983 A JP 1807983A JP H0333967 B2 JPH0333967 B2 JP H0333967B2
Authority
JP
Japan
Prior art keywords
flow rate
liquid pump
supply liquid
vaporizer
pump
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
Application number
JP1807983A
Other languages
Japanese (ja)
Other versions
JPS59145421A (en
Inventor
Akira Narai
Michio Shibata
Katsutoshi Fukumoto
Kunyuki Yukishiro
Tadashi Kizawa
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.)
Mitsubishi Heavy Industries Ltd
Chiyoda Corp
Original Assignee
Mitsubishi Heavy Industries Ltd
Chiyoda Chemical Engineering and Construction 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 Mitsubishi Heavy Industries Ltd, Chiyoda Chemical Engineering and Construction Co Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP1807983A priority Critical patent/JPS59145421A/en
Publication of JPS59145421A publication Critical patent/JPS59145421A/en
Publication of JPH0333967B2 publication Critical patent/JPH0333967B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Feeding And Controlling Fuel (AREA)

Description

【発明の詳細な説明】 本発明は、蒸発ドラム及びリボイラから成る気
化器、例えばLPG焚きボイラへLPGガスを供給
する気化等に供給液を供給するポンプがトリツプ
したときの供給液流量制御方法に関するものであ
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for controlling the flow rate of a feed liquid when a pump that supplies the feed liquid to a vaporizer consisting of an evaporation drum and a reboiler, such as a vaporizer that supplies LPG gas to an LPG-fired boiler, trips. It is something.

従来の気化器の供給液流量制御方法を、第1図
に示す実施例を参照して説明する。
A conventional method for controlling the flow rate of a feed liquid in a vaporizer will be described with reference to an embodiment shown in FIG.

第1図の実施例は、低温のLPGを熱媒にてガ
ス化し、このLPGガスをLPG焚きボイラに燃料
として供給するリボイラと蒸発ドラムとよりなる
気化器に適用したものである。
The embodiment shown in FIG. 1 is applied to a vaporizer consisting of a reboiler and an evaporator drum that gasifies low-temperature LPG using a heat medium and supplies this LPG gas as fuel to an LPG-fired boiler.

蒸発ドラム1の塔底にはレベル検出器9が設け
られ、このレベル検出器9の出力端はレベル調節
計10の入力端に接続される。レベル調節計10
の出力はドラムレベル制御系のフイードバツク信
号(訂正信号)として供給液量調節計13に送信
され、この調節計13にてこの訂正信号と供給液
流量検出器11及び変換器12によつて得られる
供給液流量検出信号とが合致するように操作信号
が算出されて供給液流量調節弁14に与えられ、
この調節弁14は前記操作信号に従つて動作され
る。
A level detector 9 is provided at the bottom of the evaporating drum 1, and the output end of this level detector 9 is connected to the input end of a level controller 10. Level controller 10
The output is sent as a feedback signal (correction signal) for the drum level control system to the supply liquid amount controller 13, and the controller 13 obtains this correction signal, the supply liquid flow rate detector 11, and the converter 12. An operation signal is calculated and given to the supply liquid flow rate control valve 14 so that it matches the supply liquid flow rate detection signal,
This control valve 14 is operated according to the operation signal.

また、蒸発ドラム1の塔頂には圧力検出器30
が設けられ、同圧力検出器30にて蒸発ドラム圧
力を検出し、その検出信号はドラム圧力調節計3
1の入力として与えられる。ドラム圧力調節計3
1の出力はドラム圧力を所定値に保つための訂正
信号となつて熱媒流量調節計34に送信され、こ
の調節計34にて前記ドラム圧力調節計31の出
力信号と熱媒流量検出器32及び変換器33によ
つて得られる熱媒流量検出信号とが合致するよう
に操作信号が算出されて熱媒流量調節弁35に与
えられ、この調節弁35は前記の操作信号に従つ
て動作される。
Additionally, a pressure detector 30 is installed at the top of the evaporation drum 1.
The pressure detector 30 detects the evaporating drum pressure, and the detection signal is sent to the drum pressure regulator 3.
1 input. Drum pressure regulator 3
The output of No. 1 becomes a correction signal for keeping the drum pressure at a predetermined value and is sent to the heating medium flow rate controller 34, which then uses the output signal of the drum pressure controller 31 and the heating medium flow rate detector 32. An operation signal is calculated so that the heat medium flow rate detection signal obtained by the converter 33 and the heat medium flow rate detection signal coincide with each other, and is applied to the heat medium flow rate control valve 35, which is operated in accordance with the operation signal. Ru.

一方、供給管3への液は駆動機20により駆動
される供給液ポンプ21により供給される。又、
LPG焚きボイラに燃料を供給する気化器は安定
供給が強く要求されるため、供給液ポンプ等は複
数台設け、1台がトリツプしても必らず予備機が
自動起動するようにしている。駆動機22により
駆動される供給液ポンプ23はこのためのもので
ある。即ち、供給液ポンプ21が過電流やポンプ
の差圧低等の異常を生じたとき、トリツプ検出器
24で検知し、トリツプ装置25により駆動機2
0を停止(供給液ポンプ21を停止)させると共
に、予備機起動装置26により駆動機22を起動
し、予備供給液ポンプ23を自動起動するように
なつている。また符号27は供給液ポンプ23の
トリツプ検出器、28は駆動機22を停止させる
トリツプ装置である。
On the other hand, the liquid to the supply pipe 3 is supplied by a supply liquid pump 21 driven by a driver 20. or,
Because the vaporizer that supplies fuel to the LPG-fired boiler requires a stable supply, multiple supply pumps are installed so that even if one trips, a standby unit will automatically start up. The feed liquid pump 23 driven by the driver 22 is for this purpose. That is, when an abnormality occurs in the supply liquid pump 21 such as an overcurrent or a low differential pressure of the pump, the trip detector 24 detects the abnormality, and the trip device 25 detects an abnormality in the drive unit 2.
0 (stops the supply liquid pump 21), the drive machine 22 is started by the reserve machine starting device 26, and the reserve supply liquid pump 23 is automatically started. Further, reference numeral 27 is a trip detector for the supply liquid pump 23, and 28 is a trip device for stopping the driving machine 22.

今、負荷が安定し、供給液ポンプ21にて液を
供給している状態において、供給液ポンプ21に
異常が生じた場合、トリツプ検出器24が働き、
トリツプ装置25、駆動機20が動作し、供給液
ポンプ21はトリツプすることとなる。
If an abnormality occurs in the supply liquid pump 21 while the load is stable and the liquid is being supplied by the supply liquid pump 21, the trip detector 24 will be activated.
The trip device 25 and driver 20 operate, and the supply liquid pump 21 is tripped.

一方、トリツプ検出器24が働いたことによ
り、予備機起動装置26が動作し、駆動機22が
起動され、予備供給液ポンプ23が起動されるこ
ととなる。ところが、前述の予備機自動起動期間
中に於いて、一時的に液流量が低下する(不足す
る)ため、供給液流量検出器11の出力、さらに
は変換器12の出力は低下する。従つて供給液流
量調節計13は調節弁14を全開方向に操作する
ことになる。従つて、予備供給液ポンプ23の起
動時、供給管3から一時的に多量の液が蒸発ドラ
ム1に流れるため、供給ポンプヘツダ29の圧力
が回復せず、予備供給液ポンプ23のトリツプ検
出器27(差圧低による検出)が動作し、トリツ
プ装置28が動作して駆動機22、即ち予備供給
液ポンプ23はトリツプしてしまう。即ち供給液
ポンプ21も予備供給液ポンプ23も同時に停止
してしまい、供給液が供給できなくなり、蒸発ド
ラム1の液レベルは低下し、ついには気化器の運
転を続行できなくなり、ひいてはボイラを停止せ
ざるを得なくなる事態に至る。
On the other hand, since the trip detector 24 is activated, the standby machine starting device 26 is activated, the drive machine 22 is started, and the standby liquid pump 23 is started. However, during the above-mentioned automatic start-up period of the standby machine, the liquid flow rate temporarily decreases (is insufficient), so the output of the supply liquid flow rate detector 11 and further the output of the converter 12 decreases. Therefore, the supply liquid flow rate controller 13 operates the control valve 14 in the fully open direction. Therefore, when the preliminary supply liquid pump 23 is started, a large amount of liquid temporarily flows from the supply pipe 3 to the evaporation drum 1, so that the pressure in the supply pump header 29 does not recover, and the trip detector 27 of the preliminary supply liquid pump 23 (Detection based on low differential pressure) is activated, the trip device 28 is activated, and the driver 22, that is, the preliminary supply liquid pump 23 is tripped. In other words, both the feed liquid pump 21 and the preliminary feed liquid pump 23 stop at the same time, making it impossible to supply the feed liquid, causing the liquid level in the evaporator drum 1 to drop, eventually making it impossible to continue operating the vaporizer, and eventually stopping the boiler. A situation arises where they are forced to do so.

また、予備供給液ポンプ23の起動ができたと
しても、調節弁が一時的に大きく開いているた
め、これがドラムレベル制御系への外乱となり、
ドラムレベルが大幅に振れ、安全運転を損なうこ
ととなる。
Furthermore, even if the preliminary supply liquid pump 23 can be started, the control valve is temporarily wide open, which causes disturbance to the drum level control system.
The drum level will fluctuate significantly, impairing safe driving.

さらに、供給液は蒸発ドラム1内LPG液に比
べ非常に低温であり、この低温供給液量が大幅に
振れることによりヒートバランスがくずれ、蒸発
ドラム1の圧力も変動することとなる。
Furthermore, the feed liquid is at a much lower temperature than the LPG liquid in the evaporator drum 1, and the large fluctuation in the amount of the low-temperature feed liquid causes the heat balance to collapse and the pressure in the evaporator drum 1 to fluctuate.

上述の現象を避けるには、供給液ポンプトリツ
プ後、供給液ポンプヘツダ圧力が回復するまでの
期間、供給液流量調節弁14の開度を供給液ポン
プトリツプ前の値に保つておけばよい。
In order to avoid the above-mentioned phenomenon, the opening degree of the feed liquid flow control valve 14 may be maintained at the value before the feed liquid pump trip until the feed liquid pump header pressure recovers after the feed liquid pump trip.

このためのロジツクは簡単であり、また供給液
流量調節弁14を前述のように一定とする期間は
短かくてよく、蒸発ドラムレベル制御系への影響
は小さい。
The logic for this is simple, and the period during which the feed liquid flow control valve 14 is kept constant as described above may be short, and the effect on the evaporating drum level control system is small.

本発明は上記事情に鑑みなされたもので、従来
の欠点を解消した気化器の供給液流量制御方法を
提供することを目的とするものである。
The present invention has been made in view of the above circumstances, and an object of the present invention is to provide a method for controlling the flow rate of a feed liquid in a vaporizer that eliminates the conventional drawbacks.

本発明によれば、ポンプから気化器に供給する
液の流量を気化器の液レベルに応じて制御する流
量調節弁を備えた気化器において、任意の供給液
ポンプのトリツプを検出し、その信号に同期して
流量調節弁の操作信号をトリツプ直前の値とする
ようにし、その後予備供給液ポンプが起動するこ
とによりポンプ吐出側圧力が所定値以上に回復す
る時まで操作信号の値を保持し、回復後、流量調
節弁の操作信号は気化器の液レベルに応じて制御
するよう復帰させることを特徴とする気化器の供
給液流量制御方法が提供される。
According to the present invention, in a vaporizer equipped with a flow rate control valve that controls the flow rate of liquid supplied from the pump to the vaporizer according to the liquid level in the vaporizer, a trip of an arbitrary supply liquid pump is detected and a signal thereof is detected. The operation signal of the flow rate control valve is set to the value immediately before the trip in synchronization with the trip, and the value of the operation signal is held until the pump discharge side pressure recovers to a predetermined value or higher by starting the preliminary supply liquid pump. There is provided a method for controlling the flow rate of a liquid supplied to a vaporizer, characterized in that, after recovery, the operation signal of the flow control valve is returned to be controlled in accordance with the liquid level of the vaporizer.

本発明によれば、供給液ポンプトリツプ時に円
滑に予備供給液ポンプを自動起動せしめ、供給液
流量を安定に供給し、ひいては気化器の運転を安
定化することができるのである。
According to the present invention, it is possible to smoothly and automatically start the preliminary supply liquid pump when the supply liquid pump trips, thereby stably supplying the flow rate of the supply liquid, thereby stabilizing the operation of the vaporizer.

また上記方法をとつているので、供給液ポンプ
トリツプ時に、一時的に多量の液が蒸発ドラムに
流れることもなく、供給液ポンプヘツダの圧力も
速やかに回復し、予備供給液ポンプの自動起動も
円滑に行なわれ、蒸発ドラムレベルの変動も抑制
することができる。
In addition, since the above method is adopted, when the supply liquid pump trips, a large amount of liquid does not temporarily flow into the evaporation drum, the pressure in the supply liquid pump header quickly recovers, and the automatic start-up of the preliminary supply liquid pump is smooth. This also makes it possible to suppress fluctuations in the evaporator drum level.

以下第2図に例示した本発明の好適な実施例に
ついて詳述する。第2図において、第1図と同等
の要素は同一参照符号で示してある。
A preferred embodiment of the present invention illustrated in FIG. 2 will be described in detail below. In FIG. 2, elements that are equivalent to those in FIG. 1 are designated by the same reference numerals.

第2図において、参照符号100は供給液ポン
プヘツダ圧力検出器であり、この出力を供給液ポ
ンプトリツプ・予備供給液ポンプ起動完了判断装
置101(以下判断装置と略記する)に送出す
る。判断装置101は出力をリレー102の駆動
信号、アナログメモリ103のモード切換信号
(トラツキングモード/ホールドモード)、供給液
流量調節計13のモード切換信号(自動/手動)
として用いるべく各々に送出する。
In FIG. 2, reference numeral 100 is a feed liquid pump header pressure detector, and its output is sent to a feed liquid pump trip/preparation feed liquid pump activation completion judgment device 101 (hereinafter abbreviated as judgment device). The judgment device 101 outputs the drive signal of the relay 102, the mode switching signal (tracking mode/hold mode) of the analog memory 103, and the mode switching signal (automatic/manual) of the supply liquid flow rate controller 13.
It is sent to each of them for use as a.

判断装置101は供給液ポンプヘツダ圧力検出
器100の出力の低下により任意の供給液ポンプ
(従来例の説明では、供給液ポンプ23を予備機
としたが、供給液ポンプ21を予備機として運用
することもある。)のトリツプを検出判断し、リ
レー102をアナログメモリ103側に切換える
と共に、アナログメモリ103をホールドモード
とし、調節弁14の開度をトリツプ前の値に固定
させる。また供給液流量調節計13を手動モード
とする。
The determination device 101 determines whether an arbitrary supply liquid pump (in the explanation of the conventional example, the supply liquid pump 23 was used as a standby machine, but the feed liquid pump 21 is operated as a standby machine) due to a decrease in the output of the feed liquid pump header pressure detector 100. ) is detected and judged, the relay 102 is switched to the analog memory 103 side, the analog memory 103 is set to the hold mode, and the opening degree of the control valve 14 is fixed at the value before the trip. Further, the supply liquid flow rate controller 13 is set to manual mode.

さらに、判断装置10は供給液ポンプヘツダ圧
力検出器100の出力回復により予備供給液ポン
プの起動が完了したと判断し、リレー102を供
給液流量調節計13の出力側に切換えると共に供
給液流量調節計13を自動とする。これによつて
供給液流量調節弁14の開度はアナログメモリ1
03により固定されていた開度を初期値として供
給流量調節計13の訂正信号により操作変更され
るようになり、供給液流量制御系はトリツプ前の
制御方法に戻る。この際、アナログメモリ103
は供給液流量調節計13の出力をトラツキングす
るモードとなる。
Further, the determination device 10 determines that the start-up of the preliminary supply pump is completed due to the recovery of the output of the supply liquid pump header pressure detector 100, and switches the relay 102 to the output side of the supply liquid flow rate controller 13, and also switches the relay 102 to the output side of the supply liquid flow rate controller 13. 13 is set to automatic. As a result, the opening degree of the supply liquid flow rate control valve 14 is determined by the analog memory 1.
The opening degree fixed by 03 is set as an initial value and the operation is changed by the correction signal from the supply flow rate controller 13, and the supply liquid flow rate control system returns to the control method before the trip. At this time, the analog memory 103
is a mode in which the output of the supply liquid flow rate controller 13 is tracked.

今、負荷が安定し、供給液ポンプ21にて液を
供給している状態において、供給液ポンプ21に
異常が生じた場合、従来の制御方法と同様に予備
供給液ポンプ23が起動される。この際、判断装
置101にて供給液ポンプヘツダ圧力が低下して
いる期間(供給液ポンプがトリツプして予備供給
液ポンプが起動完了するまでの期間)供給液流量
調節弁14の開度が固定されているため従来のよ
うに、多量の液が蒸発ドラム1に流れ出ることも
なく、供給液ポンプヘツダの圧力も速やかに回復
し、予備供給液ポンプの自動起動も速やかに行な
われる。従つて従来のように蒸発ドラムレベルや
圧力が大幅に振れるようなこともなく、ましてや
気化器停止のような事態に陥ることもなくなつ
た。
Now, when the load is stable and liquid is being supplied by the supply liquid pump 21, if an abnormality occurs in the supply liquid pump 21, the preliminary supply liquid pump 23 is started as in the conventional control method. At this time, the judgment device 101 determines that the opening degree of the supply liquid flow rate control valve 14 is fixed during the period when the supply liquid pump header pressure is decreasing (the period from when the supply liquid pump trips to when the pre-supply liquid pump completes startup). Therefore, a large amount of liquid does not flow into the evaporating drum 1 as in the conventional case, the pressure in the supply liquid pump header quickly recovers, and the preliminary supply liquid pump is quickly automatically started. Therefore, unlike in the past, the evaporating drum level and pressure do not fluctuate significantly, and there is no longer a situation where the vaporizer stops.

なお、本発明の好適な実施例では供給液ポンプ
2台設置の場合について述べたが、本発明はこの
特定の実施例に限定されるものではなく2台以上
の複数台設置の場合についても適用できる。
Although the preferred embodiment of the present invention has been described with respect to the case in which two supply liquid pumps are installed, the present invention is not limited to this specific embodiment, and can also be applied to the case where two or more pumps are installed. can.

また、本実施例では供給液ポンプトリツプ及び
予備供給液ポンプ自動起動時の判断を供給液ポン
プのヘツダ圧力の低下及び上昇により行なつた
が、実際の供給液ポンプトリツプ信号及び予備供
給液ポンプ自動起動信号を用いても同様な効果を
なし得るものである。
In addition, in this embodiment, the determination of whether to trip the supply liquid pump or automatically start the pre-supply liquid pump was made based on the decrease and increase in the header pressure of the supply liquid pump, but the actual supply liquid pump trip signal and the automatic start-up signal of the pre-supply liquid pump are used. A similar effect can be achieved by using .

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は従来の気化器の供給液流量制御方法を
例示する説明図、第2図は本発明による気化器の
供給液流量制御方法を例示する説明図である。 1……蒸発ドラム、3……供給管、4……ボイ
ラ、9……レベル検出器、10……レベル調節
計、11……供給液流量検出器、12……変換
器、13……供給液流量調節計、14……供給液
流量調節弁、20……駆動機、21……供給液ポ
ンプ、22……駆動機、23……供給液ポンプ、
24……トリツプ検出器、25……トリツプ装
置、26……予備機起動装置、27……トリツプ
検出器、28……トリツプ装置、30……圧力検
出器、31……ドラム圧力調節計、32……熱媒
流量検出器、33……変換器、34……熱媒流量
調節計、35……熱媒流量調節弁、100……供
給液ポンプヘツダ圧力検出器、101……供給液
ポンプトリツプ・予備供給液ポンプ起動完了判断
装置、102……リレー、103……アナログメ
モリ。
FIG. 1 is an explanatory view illustrating a conventional method for controlling the flow rate of a feed liquid in a vaporizer, and FIG. 2 is an explanatory view illustrating a method for controlling the flow rate of a feed liquid in a vaporizer according to the present invention. DESCRIPTION OF SYMBOLS 1... Evaporation drum, 3... Supply pipe, 4... Boiler, 9... Level detector, 10... Level controller, 11... Supply liquid flow rate detector, 12... Converter, 13... Supply Liquid flow rate controller, 14... Supply liquid flow rate control valve, 20... Drive machine, 21... Supply liquid pump, 22... Drive machine, 23... Supply liquid pump,
24... Trip detector, 25... Trip device, 26... Standby machine starting device, 27... Trip detector, 28... Trip device, 30... Pressure detector, 31... Drum pressure regulator, 32 ... Heat medium flow rate detector, 33 ... Converter, 34 ... Heat medium flow rate controller, 35 ... Heat medium flow rate control valve, 100 ... Supply liquid pump header pressure detector, 101 ... Supply liquid pump trip/spare Supply liquid pump start completion determination device, 102...Relay, 103...Analog memory.

Claims (1)

【特許請求の範囲】[Claims] 1 ポンプから気化器に供給する液の流量を気化
器の液レベルに応じて制御する流量調節弁を備え
た気化器において、任意の供給液ポンプのトリツ
プを検出し、その信号に同期して流量調節弁の操
作信号をトリツプ直前の値とするようにし、その
後予備供給液ポンプが起動することによりポンプ
吐出側圧力が所定値以上に回復する時まで操作信
号の値を保持し、回復後、流量調節弁の操作信号
は気化器の液レベルに応じて制御するよう復帰さ
せることを特徴とする気化器の供給液流量制御方
法。
1. In a vaporizer equipped with a flow control valve that controls the flow rate of liquid supplied from the pump to the vaporizer according to the liquid level in the vaporizer, a trip of any supplied liquid pump is detected and the flow rate is adjusted in synchronization with the signal. The operation signal of the control valve is set to the value immediately before tripping, and the value of the operation signal is held until the pump discharge side pressure recovers to a predetermined value or higher by starting the preliminary supply liquid pump, and after recovery, the flow rate increases. A method for controlling the flow rate of a liquid supplied to a vaporizer, characterized in that the operation signal of the control valve is returned to be controlled according to the liquid level of the vaporizer.
JP1807983A 1983-02-08 1983-02-08 Controlling method of flow rate of supplying liquid for evaporator Granted JPS59145421A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1807983A JPS59145421A (en) 1983-02-08 1983-02-08 Controlling method of flow rate of supplying liquid for evaporator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1807983A JPS59145421A (en) 1983-02-08 1983-02-08 Controlling method of flow rate of supplying liquid for evaporator

Publications (2)

Publication Number Publication Date
JPS59145421A JPS59145421A (en) 1984-08-20
JPH0333967B2 true JPH0333967B2 (en) 1991-05-21

Family

ID=11961638

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1807983A Granted JPS59145421A (en) 1983-02-08 1983-02-08 Controlling method of flow rate of supplying liquid for evaporator

Country Status (1)

Country Link
JP (1) JPS59145421A (en)

Also Published As

Publication number Publication date
JPS59145421A (en) 1984-08-20

Similar Documents

Publication Publication Date Title
JPH0333967B2 (en)
JP3818459B2 (en) Boiler control device
WO1998043025A2 (en) Improved control for absorption chillers
JP7498884B2 (en) Hot water storage system
JP4773692B2 (en) Liquefied petroleum gas supply equipment
JP3960467B2 (en) Water supply method in unit control operation of multi-pipe once-through boiler
JPH08200608A (en) Water supply flow rate control method for thermal power plant
JPS6239655B2 (en)
JP2886800B2 (en) Water heater
JPH11287404A (en) Control method for feed water of boiler
JP2519282B2 (en) Deaerator water level control system
JP7707515B2 (en) Hot water storage system
JPH11108302A (en) System for supplying and using steam
JP2000121036A (en) Liquefied gas supply circuit
JPS599442A (en) Control of heat source equipment
JPH0783404A (en) Controlling method for feed water flow rate regulating valve of boiler
JPH0565763B2 (en)
JPH07180508A (en) Deaerator pressure controller
JPS6229679B2 (en)
JPS596498A (en) Liquefied gas evaporation device utilizing atmospheric heat
JPS6248761B2 (en)
JPS6313081B2 (en)
JPH09145894A (en) Reactor feedwater control system for boiling water nuclear power plant
JPH11230502A (en) Control device for steam drum and method of operating exhaust heat recovery boiler provided with steam drum
JPH0584428B2 (en)