JP3977960B2 - Condensate pump control system - Google Patents

Condensate pump control system Download PDF

Info

Publication number
JP3977960B2
JP3977960B2 JP17777399A JP17777399A JP3977960B2 JP 3977960 B2 JP3977960 B2 JP 3977960B2 JP 17777399 A JP17777399 A JP 17777399A JP 17777399 A JP17777399 A JP 17777399A JP 3977960 B2 JP3977960 B2 JP 3977960B2
Authority
JP
Japan
Prior art keywords
condenser
condensate pump
water level
condensate
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 - Lifetime
Application number
JP17777399A
Other languages
Japanese (ja)
Other versions
JP2001004102A (en
Inventor
正典 菊池
祐司 大塚
高歩 赤津
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 Engineering and Services Co Ltd
Hitachi Ltd
Original Assignee
Hitachi Engineering and Services Co Ltd
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 Engineering and Services Co Ltd, Hitachi Ltd filed Critical Hitachi Engineering and Services Co Ltd
Priority to JP17777399A priority Critical patent/JP3977960B2/en
Publication of JP2001004102A publication Critical patent/JP2001004102A/en
Application granted granted Critical
Publication of JP3977960B2 publication Critical patent/JP3977960B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Landscapes

  • Control Of Steam Boilers And Waste-Gas Boilers (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、火力発電プラントにおいて復水ポンプ出口から系外に排出する復水器高水位制御装置を有し、復水ポンプ2台運転中1台トリップした場合の復水器高水位制御装置作動による運転継続復水ポンプの過流量防止制御方式に関する。
【0002】
【従来の技術】
従来の技術を図1の火力発電プラントの復水給水系統について説明する。蒸気タービン2にて発電に寄与した蒸気は、復水器7にて海水20と熱交換され、その後凝縮し復水器7に一時貯蔵される。
【0003】
復水器7に一時貯蔵された凝縮水(復水)は、復水ポンプ8にて抽出され、給水加熱器9で加熱された後、脱気器水位調節弁10を介して脱気器11へ流入する。
【0004】
脱気器11に流入した復水は、ボイラ給水ポンプ12にて抽出され給水加熱器13にて加熱された後にボイラ1へ給水される。
【0005】
復水器7は、貯蔵水の水位上昇により海水20と蒸気タービン排気蒸気5の熱交換が低下する事を防止するために、復水器7水位が一定値以上に上がると復水器スピルオーバー弁31を開に制御する事により復水器水位を低下させる復水器高水位制御装置30を設置している。
【0006】
【発明が解決しようとする課題】
通常のプラント運転は、図1の復水ポンプ8が2台運転をしており1台トリップすると、復水器7からの抽出量が減少するため復水器7の水位が上昇する。
【0007】
復水器7の水位が規定水位より上昇すると、復水ポンプ8の出口から系外に復水を排出する復水器高水位制御装置30の復水器スピルオーバ弁31が開する。
【0008】
復水器スピルオーバ弁31が開すると、復水ポンプ8の流出量が増加するため、復水ポンプ8が過大流量状態になる。
【0009】
過大流量状態となった復水ポンプ8は、オーバーロードにより運転の継続ができなくなるためトリップする。
【0010】
2台目の復水ポンプ8がトリップすると、ボイラ1に給水する事ができなくなるため、プラント停止に至る問題があった。
【0011】
本発明の目的は、復水ポンプが過大流量となる事を防止するものである。
【0012】
【課題を解決するための手段】
上記目的を達成するために発明は、復水ポンプが2台運転中1台トリップして一時的に復水器の水位が上昇しても一定時間は、復水器高水位制御装置を作動させず、復水器スピルオーバ弁31を開させない制御装置を設置したものである。
【0013】
【発明の実施の形態】
火力発電プラントの復水系統に本発明を適用した一実例を図2を用いて説明する。
【0014】
復水器40に貯蔵された復水は、復水ポンプ41および復水ポンプ42にて抽出され、給水加熱器43にて加熱された後、脱気器水位調節弁44を介して脱気器45に供給される。
【0015】
脱気器45内の復水は、ボイラ給水ポンプ46にて抽出され、給水加熱器47にて加熱された後、給水調節弁48を介してボイラ49に給水される。
【0016】
図3は、復水ポンプ42トリップ時おける、復水器水位、タービン負荷、復水ポンプ41通水量および復水ポンプ42通水量を示すものである。
【0017】
タービン負荷60は、100%負荷にて運転しており、2台の復水ポンプは復水ポンプ41通常通水量64および復水ポンプ42通常通水量65であり、それぞれ140t/hである。
【0018】
この状態において、復水ポンプ41がトリップする。
【0019】
2台運転中の復水ポンプが1台トリップした事により、2台分の通水量を復水ポンプ421台で賄う事になるため運転を継続している復水ポンプ42の通水量は、復水ポンプ過流量制限流量67の210t/hを越え232t/hにまで増加し過流量状態になる。
【0020】
本プラントは、その防止策としてタービン負荷60を50%負荷まで降下させ、運転を継続している復水ポンプの通水量を減少させる制御を行っている。
【0021】
しかし、100%負荷から50%負荷までに負荷を降下させる間に運転を継続している復水ポンプ42は、過流量となるため脱気器水位調節弁開度を復水ポンプ過流量制限流量67以下の193t/h相当の開度まで、復水ポンプ41トリップと同時に絞り込むものとしている。
【0022】
その場合、復水ポンプが2台運転中に1台トリップするとため一時的に復水器からの抽出水量が減少するので、復水器の水位が上昇する。
【0023】
復水器水位が復水器高水位制御装置作動設定水位63まで上昇するため、復水器高水位制御装置が作動し、復水器スピルオーバ弁51を開し系外に復水を排出する。
【0024】
復水器スピルオーバー弁51が開し復水を系外へ排出すると、その排出水の分復水ポンプ42の通水量が復水器高水位制御装置作動時の復水ポンプ通水量66の232t/hまで増加する。
【0025】
そこで、復水ポンプ2台運転中1台がトリップし負荷降下を行う場合は、復水器水位が規定水位以上になっても復水器高水位制御装置を一定時間作動させない事により復水器スピルオーバ弁を開しない事としている。
【0026】
図4は、復水ポンプが2台運転中1台トリップした場合に復水器高水位制御装置を作動させないためのインターロックを示したものである。
【0027】
復水ポンプ41停止信号80または、復水ポンプ42停止信号81が発生すると、タイマ84が働く45分間復水器スピルオーバー弁83を強制的に閉に制御を行っている。
【0028】
【発明の効果】
本発明によれば、復水器高水位制御装置は、復水ポンプが2台運転時1台トリップした場合に復水器の水位が上昇し規定値になった場合でも、復水器高水位制御装置を一定時間作動させない事により、復水器スピルオーバ弁が開して運転継続している復水ポンプが過負荷になる事を防止することができる。
【図面の簡単な説明】
【図1】従来技術を説明する図である。
【図2】本発明を説明する図である。
【図3】本発明を説明する図である。
【図4】本発明を説明する図である。
【符号の説明】
1…ボイラ、2…蒸気タービン、5…蒸気タービン排気蒸気、6…発電機、7…復水器、8…復水ポンプ、9…給水加熱器、10…脱気器水位調節弁、11…脱気器、12…ボイラ給水ポンプ、13…給水加熱器、14…給水調節弁、20…海水、30…復水器水位制御系、31…復水器スピルオーバ弁、40…復水器、41…復水ポンプ、42…復水ポンプ、43…給水加熱器、44…脱気器水位調節弁、45…脱気器、46…ボイラ給水ポンプ、47…給水加熱器、48…給水調節弁、49…ボイラ、50…復水器高水位制御装置、51…復水器スピルオーバ弁、52…復水ポンプ停止信号、53…復水器水位信号、54…脱気器水位調節弁開度制限信号、55…復水器スピルオーバ弁開度制限信号、56…演算部、60…タービン負荷、61…復水器通常水位、62…復水器最高水位、63…復水器高水位制御装置作動設定値、64…復水ポンプ41通常通水量、65…復水ポンプ42通常通水量、66…復水器高水位制御装置作動時の復水ポンプ通水量、67…復水ポンプ過流量制限流量、68…復水器高水位制御装置不動作時の復水ポンプ通水量、80…復水ポンプ41停止信号、81…復水ポンプ42停止信号、82…復水器スピルオーバ弁、83…タイマ。
[0001]
BACKGROUND OF THE INVENTION
The present invention has a condenser high water level control device that discharges out of the system from the outlet of the condensate pump in a thermal power plant, and operates the condenser high water level control device when one of the condensate pumps trips during operation. The present invention relates to an overflow prevention control system for a continuous operation condensate pump.
[0002]
[Prior art]
The conventional technology will be described for the condensate water supply system of the thermal power plant shown in FIG. The steam that contributes to power generation in the steam turbine 2 is heat-exchanged with the seawater 20 in the condenser 7, and then condensed and temporarily stored in the condenser 7.
[0003]
The condensed water (condensate) temporarily stored in the condenser 7 is extracted by the condensate pump 8 and heated by the feed water heater 9, and then the deaerator 11 through the deaerator water level control valve 10. Flow into.
[0004]
The condensed water flowing into the deaerator 11 is extracted by the boiler feed water pump 12 and heated by the feed water heater 13 and then supplied to the boiler 1.
[0005]
The condenser 7 prevents the heat exchange between the seawater 20 and the steam turbine exhaust steam 5 from being lowered due to the rise in the stored water level. When the condenser 7 water level rises above a certain value, the condenser spillover valve A condenser high water level control device 30 that lowers the condenser water level by controlling 31 to open is installed.
[0006]
[Problems to be solved by the invention]
In normal plant operation, when two condensate pumps 8 in FIG. 1 are operating and one of them is tripped, the amount of extraction from the condenser 7 decreases, so the water level of the condenser 7 rises.
[0007]
When the water level of the condenser 7 rises above the specified water level, the condenser spillover valve 31 of the condenser high water level control device 30 that discharges the condensed water from the outlet of the condensing pump 8 to the outside of the system is opened.
[0008]
When the condenser spillover valve 31 is opened, the outflow amount of the condensate pump 8 is increased, so that the condensate pump 8 enters an excessive flow rate state.
[0009]
The condensate pump 8 that has reached an excessive flow rate is tripped because operation cannot be continued due to overload.
[0010]
When the second condensate pump 8 trips, it becomes impossible to supply water to the boiler 1, which causes a problem of stopping the plant.
[0011]
The object of the present invention is to prevent the condensate pump from having an excessive flow rate.
[0012]
[Means for Solving the Problems]
In order to achieve the above object, the present invention operates the condenser high water level control device for a certain period of time even if two condenser pumps trip and one of the condenser pumps trips and the condenser water level temporarily rises. In other words, a control device that does not open the condenser spillover valve 31 is installed.
[0013]
DETAILED DESCRIPTION OF THE INVENTION
An example in which the present invention is applied to a condensate system of a thermal power plant will be described with reference to FIG.
[0014]
The condensate stored in the condenser 40 is extracted by the condensate pump 41 and the condensate pump 42, heated by the feed water heater 43, and then deaerator through the deaerator water level control valve 44. 45.
[0015]
Condensate in the deaerator 45 is extracted by the boiler feed water pump 46, heated by the feed water heater 47, and then fed to the boiler 49 via the feed water adjustment valve 48.
[0016]
FIG. 3 shows the condenser water level, turbine load, condensate pump 41 flow rate, and condensate pump 42 flow rate when the condensate pump 42 trips.
[0017]
The turbine load 60 is operated at a load of 100%, and the two condensate pumps are a condensate pump 41 normal flow rate 64 and a condensate pump 42 normal flow rate 65, which are 140 t / h, respectively.
[0018]
In this state, the condensate pump 41 trips.
[0019]
When one of the condensate pumps in operation is tripped, the condensate pump 42 that has been in operation since the condensate pump 421 covers the amount of water passing through the two condensate pumps. The water pump overflow limit flow rate 67 exceeds 210 t / h and increases to 232 t / h, resulting in an overflow state.
[0020]
As a preventive measure, this plant performs control to lower the turbine load 60 to 50% load and reduce the water flow rate of the condensate pump that continues to operate.
[0021]
However, since the condensate pump 42 that continues to operate while lowering the load from 100% load to 50% load becomes overflow, the deaerator water level control valve opening is set to the condensate pump overflow limit flow rate. At the same time as the condensate pump 41 trip, it is narrowed down to an opening degree equivalent to 193 t / h below 67.
[0022]
In that case, since one of the condensate pumps trips during operation, the amount of water extracted from the condenser temporarily decreases, and the water level of the condenser rises.
[0023]
Since the condenser water level rises to the condenser high water level control device operation setting water level 63, the condenser high water level control device operates, opens the condenser spillover valve 51, and discharges the condensate outside the system.
[0024]
When the condenser spillover valve 51 is opened and the condensate is discharged out of the system, the flow rate of the drainage condensate pump 42 is 232 t / of the condensate pump flow rate 66 when the condenser high water level controller is activated. Increase to h.
[0025]
Therefore, when one of the condensate pumps trips and the load drops, even if the condenser water level exceeds the specified water level, the condenser high water level controller is not operated for a certain period of time. The spillover valve is not opened.
[0026]
FIG. 4 shows an interlock for preventing the condenser high water level control device from operating when one condenser pump trips during operation.
[0027]
When the condensate pump 41 stop signal 80 or the condensate pump 42 stop signal 81 is generated, the condenser spillover valve 83 is forcibly closed for 45 minutes when the timer 84 operates.
[0028]
【The invention's effect】
According to the present invention, the condenser high water level control device is configured so that when one condenser pump trips when one unit is operated, the condenser high water level rises to the specified value even when the condenser water level rises to a specified value. By not operating the control device for a certain period of time, it is possible to prevent the condenser spillover valve from being opened and the condensate pump that is operating continuously being overloaded.
[Brief description of the drawings]
FIG. 1 is a diagram illustrating a conventional technique.
FIG. 2 is a diagram illustrating the present invention.
FIG. 3 is a diagram illustrating the present invention.
FIG. 4 is a diagram illustrating the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 ... Boiler, 2 ... Steam turbine, 5 ... Steam turbine exhaust steam, 6 ... Generator, 7 ... Condenser, 8 ... Condensate pump, 9 ... Feed water heater, 10 ... Deaerator water level control valve, 11 ... Deaerator, 12 ... Boiler feed pump, 13 ... Feed water heater, 14 ... Feed water control valve, 20 ... Sea water, 30 ... Condenser water level control system, 31 ... Condenser spillover valve, 40 ... Condenser, 41 ... Condensate pump, 42 ... Condensate pump, 43 ... Feed water heater, 44 ... Deaerator water level control valve, 45 ... Deaerator, 46 ... Boiler feed pump, 47 ... Feed water heater, 48 ... Feed water control valve, 49 ... Boiler, 50 ... Condenser high water level control device, 51 ... Condenser spillover valve, 52 ... Condensate pump stop signal, 53 ... Condenser water level signal, 54 ... Deaerator water level control valve opening limit signal 55 ... Condenser spillover valve opening limit signal, 56 ... Calculation unit, 60 ... Turbine load 61: Condenser normal water level, 62: Condenser maximum water level, 63: Condenser high water level control device operation set value, 64: Condensate pump 41 normal water flow, 65 ... Condensate pump 42 normal water flow, 66 ... Condensate pump flow rate when the condenser high water level control device is operating, 67 ... Condensate pump overflow limit flow rate, 68 ... Condensate pump water flow rate when the condenser high water level control device is not operating, 80 ... Condensate Pump 41 stop signal, 81 ... condensate pump 42 stop signal, 82 ... condenser spillover valve, 83 ... timer.

Claims (1)

復水系ポンプが複数台で構成され、復水器内の水位が高くなった時、復水を系外へ排出する系外排出弁を有する発電プラントの復水ポンプ制御方式において、復水系ポンプが全台運転中1台がトリップした場合、一時的に前記系外排出弁を強制的に全閉させることを特徴とした復水ポンプ制御方式。In a condensate pump control system for a power plant that has an external discharge valve that discharges condensate outside the system when the condensate pump is composed of multiple units and the water level in the condenser becomes high, the condensate pump is A condensate pump control system characterized in that when one unit trips during operation of all units, the outside discharge valve is forcibly fully closed temporarily.
JP17777399A 1999-06-24 1999-06-24 Condensate pump control system Expired - Lifetime JP3977960B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17777399A JP3977960B2 (en) 1999-06-24 1999-06-24 Condensate pump control system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17777399A JP3977960B2 (en) 1999-06-24 1999-06-24 Condensate pump control system

Publications (2)

Publication Number Publication Date
JP2001004102A JP2001004102A (en) 2001-01-12
JP3977960B2 true JP3977960B2 (en) 2007-09-19

Family

ID=16036875

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17777399A Expired - Lifetime JP3977960B2 (en) 1999-06-24 1999-06-24 Condensate pump control system

Country Status (1)

Country Link
JP (1) JP3977960B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104728827B (en) * 2015-03-24 2016-06-29 中国电力工程顾问集团中南电力设计院有限公司 Join the condensate system of weep gland steam heater
JP6928691B2 (en) * 2016-08-26 2021-09-01 三菱パワー株式会社 Pump system and its operation method and power plant
JP6771338B2 (en) * 2016-08-26 2020-10-21 三菱パワー株式会社 Pump system and its operation method and power plant
CN111120021B (en) * 2019-12-20 2022-06-24 东方电气集团东方汽轮机有限公司 Water charging system for condenser of heat supply unit

Also Published As

Publication number Publication date
JP2001004102A (en) 2001-01-12

Similar Documents

Publication Publication Date Title
JP3977960B2 (en) Condensate pump control system
JPS6211164B2 (en)
JP4393593B2 (en) Heating method and apparatus for valve device
JP2016156527A (en) Flash steam generation device
JP4551168B2 (en) Steam turbine power generation facility and operation method thereof
JP4031872B2 (en) Water supply control method in a power plant using a drum boiler
JP3462235B2 (en) Steam generator
JP3664759B2 (en) Flash prevention device
JP2839195B2 (en) Waste heat recovery boiler water supply control device
JP3650277B2 (en) Thermal power plant control device and thermal power plant control method
JPH0660564B2 (en) Air-fuel mixture controller
JPH11294713A (en) Water supply device for exhaust heat recovery boiler
JP2519282B2 (en) Deaerator water level control system
JPS5814909A (en) Degassing apparatus
JPH0225082B2 (en)
JP2544050B2 (en) Drain tank water level control device
JPH09210301A (en) Emergency protective apparatus for fluidized bed boiler
JP2001208890A (en) Feed water heater piping system for nuclear power plant
JPS5922241Y2 (en) Thermal power plant protection equipment
JPH01193507A (en) Pressure and wafer level controller of aerator at the time of sudden decrease of load
JP3286023B2 (en) Waste heat recovery boiler condensate water supply protection system
JPH0372886B2 (en)
JPS6218832B2 (en)
JP2004020069A (en) Control method of deaerator water level control valve and power generation plant
JPS6193209A (en) Steam turbine plant including low-pressure turbine bypass system

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20050328

RD02 Notification of acceptance of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7422

Effective date: 20060512

RD04 Notification of resignation of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7424

Effective date: 20060512

A711 Notification of change in applicant

Free format text: JAPANESE INTERMEDIATE CODE: A712

Effective date: 20070213

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20070601

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20070619

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20070622

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100629

Year of fee payment: 3

R150 Certificate of patent or registration of utility model

Ref document number: 3977960

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100629

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110629

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110629

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120629

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120629

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130629

Year of fee payment: 6

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313115

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

EXPY Cancellation because of completion of term