JPS6232319A - Detector for liquid level - Google Patents

Detector for liquid level

Info

Publication number
JPS6232319A
JPS6232319A JP17107385A JP17107385A JPS6232319A JP S6232319 A JPS6232319 A JP S6232319A JP 17107385 A JP17107385 A JP 17107385A JP 17107385 A JP17107385 A JP 17107385A JP S6232319 A JPS6232319 A JP S6232319A
Authority
JP
Japan
Prior art keywords
water
pipe
tank
storage tank
pressure
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.)
Pending
Application number
JP17107385A
Other languages
Japanese (ja)
Inventor
Setsuo Nonaka
野中 節雄
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP17107385A priority Critical patent/JPS6232319A/en
Publication of JPS6232319A publication Critical patent/JPS6232319A/en
Pending legal-status Critical Current

Links

Landscapes

  • Measurement Of Levels Of Liquids Or Fluent Solid Materials (AREA)

Abstract

PURPOSE:To detect a liquid level in a water tank with high accuracy by a difference between the lower end pressure of the reference pressure detecting pipe and the bottom pressure of the water tank by providing a reference pressure detecting pipe in the water tank. CONSTITUTION:Condensation from a condensate pump is supplied to a deaerating chamber 2 through a condensate pipe 1 and atomized by a spray valve 5, and mixed and heated and temperature-raised by steam from a heating steam pipe 3 and is once stored in the water tank 4 through a connecting pipe 6. The stored water is supplied to a boiler through a downcast pipe 8. The reference pressure detecting pipe 12 is provided in the tank 4 and the lower end of the detecting pipe 12 pierces through the lower part of the tank 4 and is connected with the high pressure side of a differential pressure type liquid-level detector 16 and a connecting pipe 15 connected with the lower part of the tank 4 is connected with the low pressure side of the detector 16. Further, the water filling piping 11 pours a small quantity of condensation which is overflowed from an opening part of the upper end of the detecting pipe 12 in the tank 4. Then, since the different pressures are applied to the high pressure side and the low pressure side of the detector 16 respectively, the detector 16 detects these differential pressures which are transmitted to a level gage 18 to measure a water level of the tank 4.

Description

【発明の詳細な説明】 〔発明の利用分野〕 本発明はタービンプラントにおける液位検出に係り、特
に、飽和水を使用する熱交換器の液位検出に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] The present invention relates to liquid level detection in a turbine plant, and more particularly to liquid level detection in a heat exchanger using saturated water.

〔発明の背景〕[Background of the invention]

従来の装置は、特開昭48−58201号公報に記載の
ように、差圧式の水位検出器にょシ貯水タンクの水位を
測定するに当り、貯水タンク内の上部にオーバーフロ一
孔とバランス孔を設けたりザーバを配設し、このリザー
バの上部に補給水の供給口を設は脱気器入口の復水管よ
り抽水して、この供給口に注水し、さらに、このリザー
バの低部に連通管の一端を連結し、この連通管を貯水タ
ンクの外壁を貫通して差圧式液位検出器の高圧側に連結
し、この差圧式液位検出器の低圧側を貯水タンクの底部
に連結した導圧管に連絡して貯水タンクの水位を測定し
てい念。
As described in Japanese Unexamined Patent Publication No. 48-58201, the conventional device uses a differential pressure type water level detector to measure the water level of a water storage tank. A make-up water supply port is installed at the top of this reservoir, and water is extracted from the condensate pipe at the deaerator inlet, injected into this supply port, and then communicated with the bottom of this reservoir. One end of the pipe was connected, and this communication pipe was passed through the outer wall of the water storage tank and connected to the high pressure side of a differential pressure type liquid level detector, and the low pressure side of this differential pressure type liquid level detector was connected to the bottom of the water storage tank. Please be sure to measure the water level in the water tank by connecting to the impulse pipe.

リザーバ及び連結管を貯水タンク内に配設し、連結管上
端に設けたリザーバに注水しているため連結管内の水は
自然対流以外VCは、流動することがなく、従って、連
結管内水温と貯水タンク水温が一致し、貯水タンク内圧
力が安定している場合には、連結管内水比重と貯水タン
ク内比重が同一となり、精度良く貯水タンク内液位を検
出していた。しかし、貯水タンク内圧力が急低下すると
、貯水がフラッシュを発生し、激しい場合には、フラッ
シュした水面は500箪以上も盛る現象がある。この時
、連結管内の水温も貯水タンク内水温と同一であるため
、同様にフラッシュして、リザ−ハの水面を盛上げるが
、リザーバのオーバーフロ一孔より貯水タンク内に流出
してしまうなめ、連結管内の静水頭が小ざくなり、貯水
タンク液位に誤差を生じる問題があった。
Since the reservoir and the connecting pipe are arranged in a water storage tank, and water is injected into the reservoir provided at the upper end of the connecting pipe, the water in the connecting pipe does not flow except through natural convection, and therefore, the water temperature inside the connecting pipe and the stored water When the tank water temperatures match and the pressure inside the water storage tank is stable, the specific gravity of the water in the connecting pipe and the specific gravity inside the water storage tank are the same, and the liquid level in the water storage tank can be detected with high accuracy. However, if the pressure inside the water storage tank suddenly drops, the stored water will flush, and in severe cases, the flushed water surface can rise by more than 500 cubic meters. At this time, the water temperature in the connecting pipe is the same as the water temperature in the water storage tank, so it flushes in the same way and raises the water surface in the reservoir, but it does not flow out into the water storage tank from the overflow hole in the reservoir. There was a problem in that the hydrostatic head in the connecting pipe became small, causing an error in the water level in the water storage tank.

一方、特開昭59−197828号公報に記載のように
、リザーバを貯水タンクの外部に設は冷却水を導圧等の
下側より注入する方式では、導圧管がタンク外部にある
ため、貯水タンク内圧の急低下時にも、リザーバ内の水
はほとんどフラッシュすること汀ないが、貯水タンク内
水温よりリザーバ下部の導圧管内水温は、通常、約10
〜100C低くく、特に、加熱蒸気が供給されている起
動時VCは、100C以上の温度差が生じる等、運転条
件により貯水タンク内水温とリザーバ下部の導圧管内水
温度差が変化するため、液位測定の誤差が大きくなる問
題があった。
On the other hand, as described in Japanese Patent Application Laid-Open No. 59-197828, in a method in which the reservoir is installed outside the water storage tank and the cooling water is injected from the lower side of the pressure impulse, etc., since the impulse pipe is outside the tank, the water storage Even when the tank internal pressure suddenly drops, the water in the reservoir hardly flushes, but the water temperature in the impulse pipe below the reservoir is usually about 10% lower than the water temperature in the storage tank.
The temperature difference between the water temperature in the water storage tank and the water temperature in the impulse pipe at the bottom of the reservoir changes depending on the operating conditions, such as a temperature difference of 100C or more, especially at startup when heating steam is supplied to the VC. There was a problem that the error in liquid level measurement became large.

〔発明の目的〕[Purpose of the invention]

本発明の目的は貯水タンク圧力と温度が変化した場合も
貯水タンク内液位を精度良く検出可能な液位検出装置を
提供することにある。
An object of the present invention is to provide a liquid level detection device that can accurately detect the liquid level in a water storage tank even when the pressure and temperature of the water storage tank change.

〔発明の概要〕[Summary of the invention]

差圧式液位検出器の測定誤差を無くするには、貯水タン
ク温度と基準圧力検出管内水温を同一にする必要があり
、このため、基準圧力検出管を貯水タンク内に配設する
が、貯水タンク圧力急低下時にも基準圧力検出管内の水
をフラッシュさせないための貯水タンク内水温より極〈
わずかに低温に保たれるよう脱気器入口復水を基準圧力
検出管の下端より少量注入し、上端の開口部より貯水タ
ンク内fオーバーフローきせる。注入された復水け、基
準圧力検出管内で貯水タンク水により徐々に加熱昇温さ
れながら、上方に移動し、やがて、基準圧力検出管の上
端の開口部よりオーバーフローするため基準圧力検出管
内水温は上部はど温度が高くなり、基準圧力検出管の中
部、下部でフランシュするととけない。従って、補給水
以上にオーバーフローすることもない。基準圧力検出管
の最上端部では極〈わずかなフラッシュを生じるがフラ
ッシュにより飛散し走水以上に、注水されるため、基準
圧力検出管の水位は一定に保つことが可能となり、基準
圧力検出管の下端圧力と、貯水タンク低部圧力の圧力差
より貯水タンクの液位を精度良く測定する。
In order to eliminate measurement errors with differential pressure type liquid level detectors, it is necessary to make the water storage tank temperature and the water temperature inside the reference pressure detection pipe the same.For this reason, the reference pressure detection pipe is installed inside the water storage tank, but the To prevent the water in the reference pressure detection pipe from flushing even when the tank pressure suddenly drops, the water temperature in the water storage tank should be
A small amount of condensate at the deaerator inlet is injected from the lower end of the reference pressure detection tube to keep it at a slightly lower temperature, and overflow is allowed to occur in the water storage tank through the opening at the upper end. The injected condensate moves upward while being gradually heated and heated by the storage tank water in the reference pressure detection tube, and eventually overflows from the opening at the upper end of the reference pressure detection tube, so the water temperature in the reference pressure detection tube decreases. The temperature in the upper part becomes high, and the middle and lower part of the reference pressure detection tube cannot be flanched. Therefore, there will be no overflow of more than make-up water. A very small flash occurs at the top end of the reference pressure detection tube, but the flash scatters and injects more water than the running water, making it possible to maintain a constant water level in the reference pressure detection tube. The liquid level in the water storage tank is accurately measured from the pressure difference between the lower end pressure of the tank and the lower pressure of the water storage tank.

〔発明の実施例〕[Embodiments of the invention]

以下、本発明の一実施例をlX1図により説明する。 Hereinafter, one embodiment of the present invention will be explained with reference to the 1X1 diagram.

復水ポンプより供給された復水は復水管lを通って脱気
室2に供給され、スプレ弁5にょシ霧化され、加熱蒸気
管3より供給された蒸気によって混合加熱昇温され、溶
存酸素を除去された水は連絡管6を通って貯水タンクI
C一旦貯水される。
The condensate supplied from the condensate pump is supplied to the degassing chamber 2 through the condensate pipe 1, where it is atomized by the spray valve 5, mixed and heated by steam supplied from the heating steam pipe 3, and dissolved. The water from which oxygen has been removed passes through the connecting pipe 6 to the water storage tank I.
C The water is temporarily stored.

貯水タンク4に貯水された水は、降水管8を経て給水ポ
ンプによりボイラに供給される。貯水タンク4vcは基
準圧力検出管12が配設されており、この基準圧力検出
管12の上端は貯水タンク4の上部で開口し、下端は貯
水タンク4の下部を貫通して導圧′W14を経て差圧式
液位検出器16の高圧側に連結され、貯水タンク下部に
連結した導圧管15は、差圧式液位検出器16の低圧側
に連結されている。注水配g11は復水管1と基準圧力
検出管12の下端に連結し、少量の復水を注入して基準
圧力検出管12の上端開口部よ、り貯水タンク4内にオ
ーバーフローするようになっている。
Water stored in the water storage tank 4 is supplied to the boiler via a downcomer pipe 8 by a water supply pump. The water storage tank 4vc is provided with a reference pressure detection pipe 12. The upper end of this reference pressure detection pipe 12 opens at the upper part of the water storage tank 4, and the lower end passes through the lower part of the water storage tank 4 to transmit a guiding pressure 'W14. A pressure guiding pipe 15 connected to the high pressure side of the differential pressure type liquid level detector 16 through the water storage tank and connected to the lower part of the water storage tank is connected to the low pressure side of the differential pressure type liquid level detector 16. The water injection pipe g11 is connected to the lower end of the condensate pipe 1 and the reference pressure detection pipe 12, and injects a small amount of condensate so that it overflows into the water storage tank 4 through the upper end opening of the reference pressure detection pipe 12. There is.

差圧式液位検出器16の高圧側VCは(1)式に示す圧
力Paが加わシ、低圧側には(2)式に示す圧力Ptが
加わるため、差圧式液位検出器は(3)式に示す差圧D
Pを検出して、液位計18に伝達し、貯水タンク4の水
位を測定するようになっている。
The pressure Pa shown in equation (1) is applied to the high pressure side VC of the differential pressure type liquid level detector 16, and the pressure Pt shown in equation (2) is applied to the low pressure side. Differential pressure D shown in the formula
P is detected and transmitted to the liquid level gauge 18 to measure the water level in the water storage tank 4.

PFI ”Po + r+ ・HI+ r2 ・H2・
”(1)PL =pa + ro −Ho + rfi
 T Hx     −(2)DP=Pr  Pt=r
l・Hl−r、−1(、−・(3)PR:差圧式液位検
出器の高圧側圧力 PL:差圧式液位検出器の低圧側圧力 Po=貯水タンク内圧 ro:貯水タンク内水の平均比重 r、二基率圧力検出管内水の平均比重 r、:導圧管14ま念は導圧管15内水の平均比重 Ho:貯水タンク H0二基準圧力検出管水位 (3)式に示すように、基準圧力検出管内水の平均比重
r1 と貯水タンク内水の平均比重r0がほぼ同値であ
る場合、液位測定の誤差もほぼ零になる。
PFI ”Po + r+ ・HI+ r2 ・H2・
”(1) PL = pa + ro −Ho + rfi
T Hx −(2) DP=Pr Pt=r
l・Hl−r, −1(, −・(3) PR: High pressure side pressure of the differential pressure type liquid level detector PL: Low pressure side pressure of the differential pressure type liquid level detector Po = Water storage tank internal pressure ro: Water in the water storage tank The average specific gravity r of the water in the pressure sensing tube 14, the average specific gravity r of the water in the pressure sensing tube 14, the average specific gravity of the water in the impulse tube 15, Ho: the water storage tank H0, the two reference pressure sensing tube water level, as shown in equation (3). Furthermore, if the average specific gravity r1 of the water in the reference pressure detection pipe and the average specific gravity r0 of the water in the water storage tank are approximately the same value, the error in liquid level measurement will also be approximately zero.

基準圧力検出管12の直径は約50+mで高ざ約400
0m程度あるが、注水流量を約1.6 kg /分とす
れば、基準圧力検出管内流速は80crIt/分と極〈
微速となり、基準圧力検出管内での圧力損失はほとんど
零となる。貯水タンク4の圧力が急減少する場合は、一
般に、最短でも約十分間かかるのに対し、基準圧力の検
出管内の水は約5分で全量置換されるなめ、貯水タンク
4の水温よシ常時、極〈わずか低温側に保持することが
でき、基準圧力検出−#12内の水はフラッシュを発生
すルコトはない。71−を均圧器。
The diameter of the reference pressure detection tube 12 is approximately 50+m and the height is approximately 400m.
However, if the water injection flow rate is approximately 1.6 kg/min, the standard pressure detection pipe flow velocity is 80 crIt/min, which is extremely low.
The speed becomes very slow, and the pressure loss within the reference pressure detection tube becomes almost zero. If the pressure in the water storage tank 4 suddenly decreases, it generally takes about ten minutes at the shortest, but the water in the standard pressure detection tube is completely replaced in about 5 minutes. , it can be kept at a very low temperature, and there is no chance that the water in the reference pressure detection-#12 will cause a flash. 71- is a pressure equalizer.

第2図は本発明の他の実施例を示す配管系統図で、注水
管11の途中に加熱チューブ13を設け、基準圧力検出
管への注水を貯水タンク4の貯水によって加熱昇温し、
注水の温度を高くする。第1図に比べ基準圧力検出管1
2の水温と貯水タンク4の貯水の比重が、さらに設定値
に近くなるため、液位測定の精度が向上する。
FIG. 2 is a piping system diagram showing another embodiment of the present invention, in which a heating tube 13 is provided in the middle of the water injection pipe 11, and the water injected into the reference pressure detection pipe is heated and heated by water stored in the water storage tank 4.
Increase the water injection temperature. Reference pressure detection tube 1 compared to Fig. 1
Since the water temperature No. 2 and the specific gravity of the water stored in the water storage tank 4 become closer to the set values, the accuracy of liquid level measurement is improved.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、常時、貯水タンク内貯水温度と、基準
圧力検出管内水の比重をほとんど同じにすることができ
るので、貯水タンク圧力・温度変化にともない自動的に
比重補正が行なわれ脱気室及び貯水タンクがどのような
運転を行なわれた場合にも貯水タンクの液位を精度良く
測定する効果がある。
According to the present invention, the temperature of the water stored in the water storage tank and the specific gravity of the water in the reference pressure detection pipe can be kept almost the same at all times, so that the specific gravity is automatically corrected in accordance with changes in the pressure and temperature of the water storage tank, and deaeration is performed. This has the effect of accurately measuring the liquid level in the water storage tank no matter how the chamber and water storage tank are operated.

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

第1図、第2図は本発明の一実施例の配管系統図である
。 1・・・復水管、2・・・脱気室、3・・・加熱蒸気管
、4・・・貯水タンク、5・・・スプレー弁、6・・・
連絡管、7・・・均圧管、8・・・降水管、11・・・
注水配管、12・・・基準圧力検出管、13・・・加熱
チューブ、14・・・導圧管、15・・・導圧管、16
・・・差圧式液位検出器。
1 and 2 are piping system diagrams of an embodiment of the present invention. 1... Condensate pipe, 2... Deaeration chamber, 3... Heating steam pipe, 4... Water storage tank, 5... Spray valve, 6...
Communication pipe, 7... pressure equalization pipe, 8... downcomer pipe, 11...
Water injection pipe, 12... Reference pressure detection tube, 13... Heating tube, 14... Impulse tube, 15... Impulse tube, 16
...Differential pressure type liquid level detector.

Claims (1)

【特許請求の範囲】[Claims] 1、熱交換器に貯えられた飽和水を収容する容器内に配
設され、前記容器の低部の圧力検出配管と基準液位を保
持する開口部をもつ基準圧力検出管と前記熱交換器に復
水を供給する復水管から分岐して前記基準圧力検出管の
下端に、前記復水を冷却水として導く配管を配設したこ
とを特徴とする液位検出装置。
1. A reference pressure detection pipe disposed in a container containing saturated water stored in a heat exchanger, and having a pressure detection pipe in the lower part of the container, an opening for maintaining a reference liquid level, and the heat exchanger. A liquid level detecting device characterized in that a pipe branching from a condensate pipe that supplies condensate to a lower end of the reference pressure detecting pipe is arranged to guide the condensate as cooling water.
JP17107385A 1985-08-05 1985-08-05 Detector for liquid level Pending JPS6232319A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17107385A JPS6232319A (en) 1985-08-05 1985-08-05 Detector for liquid level

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17107385A JPS6232319A (en) 1985-08-05 1985-08-05 Detector for liquid level

Publications (1)

Publication Number Publication Date
JPS6232319A true JPS6232319A (en) 1987-02-12

Family

ID=15916520

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17107385A Pending JPS6232319A (en) 1985-08-05 1985-08-05 Detector for liquid level

Country Status (1)

Country Link
JP (1) JPS6232319A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0296090A (en) * 1988-09-30 1990-04-06 Kawasaki Heavy Ind Ltd Tunnel excavator
JPH03202590A (en) * 1989-12-29 1991-09-04 Penta Ocean Constr Co Ltd Shield excavator
JPH0667594U (en) * 1993-03-04 1994-09-22 川崎重工業株式会社 Tunnel excavator

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0296090A (en) * 1988-09-30 1990-04-06 Kawasaki Heavy Ind Ltd Tunnel excavator
JPH03202590A (en) * 1989-12-29 1991-09-04 Penta Ocean Constr Co Ltd Shield excavator
JPH0667594U (en) * 1993-03-04 1994-09-22 川崎重工業株式会社 Tunnel excavator

Similar Documents

Publication Publication Date Title
US2105127A (en) Fluid meter
US4393705A (en) Specific gravity level gauge and method
US7845223B2 (en) Condensing chamber design
JPS6232319A (en) Detector for liquid level
CN104330331B (en) A kind of device of test liquid material saturated vapour pressure under the high temperature conditions
CN104330328B (en) A kind of using method of test liquid material saturated vapor pressure device under the high temperature conditions
US3422682A (en) Hydrostatic densitometer
JP2000056064A (en) Liquid tank facility equipped with liquid level measuring device
JP2008267931A (en) Liquid level measuring device for liquid tank
US1314249A (en) Calobimetric method of and apparatus for measuring- steam-flow
CN108168764B (en) Hydraulic measuring device and water heater
CN108225476B (en) Hydraulic measuring device
US1161279A (en) Liquid-flow meter.
CN110763300A (en) System and method for measuring dynamic liquid level in pipe under steam water working condition
CN210123298U (en) Improved built-in type balance container steam drum liquid level measurement system
US3161052A (en) Measurement of interfacial levels
JPS56133613A (en) Liquid level gauge system
CN201094065Y (en) Evacuation type pressure difference water gauge
JPH09133566A (en) Liquid level measuring apparatus
JP3609722B2 (en) Liquid level detector
SU576527A1 (en) Hydrostatic densitometer
US2458783A (en) Constant reference point manometer
CN214502602U (en) Liquid level meter
JPH0634421A (en) Level gauge for evaporating and concentrating device
JP2010255530A (en) Liquid flow rate measuring device