CN206054015U - A kind of system for improving thermoelectricity pure condensate unit motility - Google Patents

A kind of system for improving thermoelectricity pure condensate unit motility Download PDF

Info

Publication number
CN206054015U
CN206054015U CN201620957697.6U CN201620957697U CN206054015U CN 206054015 U CN206054015 U CN 206054015U CN 201620957697 U CN201620957697 U CN 201620957697U CN 206054015 U CN206054015 U CN 206054015U
Authority
CN
China
Prior art keywords
steam pipe
valve
steam
reducing
cooling plant
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.)
Withdrawn - After Issue
Application number
CN201620957697.6U
Other languages
Chinese (zh)
Inventor
孙士恩
彭桂云
田亚
常浩
庄荣
高新勇
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.)
Huadian Electric Power Research Institute Co Ltd
Original Assignee
Huadian Electric Power Research Institute 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 Huadian Electric Power Research Institute Co Ltd filed Critical Huadian Electric Power Research Institute Co Ltd
Priority to CN201620957697.6U priority Critical patent/CN206054015U/en
Application granted granted Critical
Publication of CN206054015U publication Critical patent/CN206054015U/en
Withdrawn - After Issue legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Engine Equipment That Uses Special Cycles (AREA)

Abstract

This utility model is related to a kind of system for improving thermoelectricity pure condensate unit motility.For thermoelectricity pure condensate unit, it is most important to excavate its peak load regulation potentiality, at present also without such technology.This utility model includes boiler, steam turbine, condenser, condensate pump, oxygen-eliminating device, feed pump, main steam pipe, cold reheated steam pipe and reheat heat steam pipe, is characterized in:Also including reducing-and-cooling plant A, reducing-and-cooling plant B, main steam bypass, reheat heat steam by-pass, steam pipe branch road A and steam pipe branch road B, the two ends of main steam bypass are connected on main steam pipe and cold reheated steam pipe, reducing-and-cooling plant A is arranged in main steam bypass, reducing-and-cooling plant B is connected with oxygen-eliminating device by steam pipe branch road A, reducing-and-cooling plant B passes through steam pipe branch road B and condenser connects, and reducing-and-cooling plant B passes through reheat heat steam by-pass and reheat heat steam pipe connects.This utility model is reasonable in design, can realize pure condensate unit load peak regulation.

Description

A kind of system for improving thermoelectricity pure condensate unit motility
Technical field
This utility model belongs to power plant units motility and lifts field, and in particular to a kind of to improve the spirit of thermoelectricity pure condensate unit The system of activity, is particularly suited for needing thermal power plant's pure condensate unit of quick response load variations.
Background technology
At present, China's policy gradually payes attention to the popularization of new forms of energy, reduces the ratio of fired power generating unit.Ended for the end of the year 2012, I The installed capacity of wind-driven power of the existing 44.8GW of state.But wind-powered electricity generation has very strong randomness, intermittence, uncontrollability and anti-peak regulation special Property, this carries out the difficulty of peak load regulation network with regard to gradually increasing fired power generating unit.In order to be able to new forms of energy resource of effectively dissolving, country by The policy for gradually increasing fired power generating unit peak regulation requires that such as National Energy Board northeast Supervision Bureau is with regard to printing and distributing《Tohoku Electric Power peak regulation Assisted hatching supervisory method(It is tentative)》And its supplementary provisions requirement will lift clean energy resource and dissolve space, while defining " staged " compensation mechanism, according to peak regulation rate point third gear making up price, i.e., first grade:48%<Thermal power plant's peak regulation rate≤55%, compensation Valency is 0.4 yuan/kWh;Second gear:55%<Thermal power plant's peak regulation rate≤60%, compensation valency are 0.4~0.6 yuan/kWh;Third gear:Thermoelectricity Factory's peak regulation rate>60%, compensation valency is 0.6~0.8 yuan/kWh.
As can be seen here, national policy is just progressively increasing the compensation dynamics to fired power generating unit peak modulation capacity.For thermoelectricity pure condensate Unit, excavates its peak load regulation potentiality, lifts unit motility, and the new forms of energy such as wind-powered electricity generation of dissolving to electrical network play vital work With.Therefore, how to adopt an effective measure and lift the motility of fired power generating unit, become one of focus of concern.Publication date It is on 01 19th, 2011, in the Chinese patent of Publication No. CN101950964A, disclosed a kind of comprising cogeneration units With the system and dispatching method of pure condensed steam formula fired power generating unit, also really could not realize lifting the function of unit motility.
Utility model content
The purpose of this utility model is to overcome above-mentioned deficiency present in prior art, and provides a kind of reasonable in design, Dependable performance, is advantageously implemented the system of the raising thermoelectricity pure condensate unit motility of pure condensate unit load peak regulation.
The technical scheme in the invention for solving the above technical problem is:The raising thermoelectricity pure condensate unit motility is System includes boiler, steam turbine, condenser, condensate pump, low pressure heat regenerative system, oxygen-eliminating device, feed pump, high-pressure extraction system, master Steam pipe, cold reheated steam pipe and reheat heat steam pipe, the boiler pass through main steam pipe and reheat heat steam pipe and steam turbine Connection, the steam turbine are connected with boiler by cold reheated steam pipe, the steam turbine, condenser, condensate pump, low pressure backheat System, oxygen-eliminating device, feed pump, high-pressure extraction system and boiler are sequentially connected, and its construction features is:Also fill including pressure and temperature reducing Put A, reducing-and-cooling plant B, valve B, valve C, valve D, valve E, valve F, main steam bypass, reheat heat steam by-pass, steaming Steam pipe branch road A and steam pipe branch road B, the two ends of the main steam bypass are connected to main steam pipe and cold reheated steam pipe On, the valve B, reducing-and-cooling plant A and valve C are sequentially arranged in main steam bypass, and the reducing-and-cooling plant B passes through Steam pipe branch road A is connected with oxygen-eliminating device, and, on steam pipe branch road A, the reducing-and-cooling plant B is by steaming for the valve F Steam pipe branch road B and condenser connection, on steam pipe branch road B, the reducing-and-cooling plant B passes through heat again to the valve E Hot vapour by pass and the connection of reheat heat steam pipe, the valve D are arranged in reheat heat steam by-pass.
Preferably, this utility model also includes that valve A, the valve A are arranged on main steam pipe.
Preferably, this utility model also includes that valve H, the valve H are arranged on reheat heat steam pipe.
A kind of operation method of the system of described raising thermoelectricity pure condensate unit motility, its feature is:The operation The step of method, is as follows:
When pure condensate unit load is quickly reduced or raised, adjusting feed pump reduces its flow increase or flow, now Should ensure that boiler drum, oxygen-eliminating device and condenser water level allow minimum and highest limit between, recycling drum, The storage emission capacity of oxygen-eliminating device and condenser realizes the quick response of unit load;Or, adjusting condensate pump increases its flow Big or flow reduces, and now should ensure that the water level of boiler-steam dome, oxygen-eliminating device and condenser limits it in the minimum and highest for allowing Between, reuse drum, oxygen-eliminating device and condenser stores the quick response that emission capacity realizes unit load;
When pure condensate unit load long-time is raised and lowered, unit is met by increasing or decreasing the evaporation capacity of boiler The change of load;If the evaporation capacity of boiler cannot continue to reduce, main steam bypass is opened, main steam passes through reducing-and-cooling plant A enters cold reheated steam pipe after carrying out pressure and temperature reducing, Jing after boiler reheating, by reheat heat steam by-pass Jing reducing-and-cooling plant B After carrying out pressure and temperature reducing, condenser is entered by steam pipe branch road B, unit load is realized using the external heat dissipation capacity of condenser Response;And/or, oxygen-eliminating device is entered by steam pipe branch road A, the sound of unit load is realized using the heat storage capacity of oxygen-eliminating device Should.
Preferably, this utility model is when pure condensate unit load is quickly reduced or raised, adjusting feed pump makes its flow Increase or flow reduce, and flow therein reduces to be included closing flow.
Preferably, this utility model is when pure condensate unit load is quickly reduced or raised, adjusting condensate pump flows which Amount increase or flow reduce, and flow therein reduces to be included closing flow.
This utility model compared with prior art, with advantages below and effect:Simple structure, reasonable in design, performance can Lean on, realize that the motility of thermoelectricity pure condensate unit is lifted by rational design;After having used this utility model, it is possible to achieve thermoelectricity The depth peak modulation capacity of unit, meets demand of the electrical network to peak load regulation conscientiously, is worth with higher practice.
Description of the drawings
Fig. 1 is the structural representation of the system of raising thermoelectricity pure condensate unit motility in this utility model embodiment.
In figure:1-boiler, 2-steam turbine, 3-condenser, 4-condensate pump, 5-low pressure heat regenerative system, 6-deoxygenation Device, 7-feed pump, 8-high-pressure extraction system, 9-reducing-and-cooling plant A, 10-reducing-and-cooling plant B, 11-valve A, By 12-valve B, 13-valve C, 14-valve D, 15-valve E, 16-valve F, 17-main steam pipe, 18-main steam Road, 19-cold reheated steam pipe, 20-reheat heat steam pipe, 21-reheat heat steam by-pass, 22-valve H, 23-steam pipe Branch road A, 24-steam pipe branch road B.
Specific embodiment
The utility model is described in further detail below in conjunction with the accompanying drawings and by embodiment, and following examples are right It is of the present utility model explanation and this utility model is not limited to following examples.
Embodiment.
Referring to Fig. 1, the system of the raising thermoelectricity pure condensate unit motility in the present embodiment includes boiler 1, steam turbine 2, coagulates Vapour device 3, condensate pump 4, low pressure heat regenerative system 5, oxygen-eliminating device 6, feed pump 7, high-pressure extraction system 8, reducing-and-cooling plant A9, subtract Warm decompressor B10, valve A11, valve B12, valve C13, valve D14, valve E15, valve F16, main steam pipe 17, main steaming Vapour bypass 18, cold reheated steam pipe 19, reheat heat steam pipe 20, reheat heat steam by-pass 21, valve H22, steam pipe branch road A23 With steam pipe branch road B24.
Boiler 1 in the present embodiment passes through main steam pipe 17 and reheat heat steam pipe 20 is connected with steam turbine 2, valve A11 On main steam pipe 17, valve H22 is arranged on reheat heat steam pipe 20, steam turbine 2 by cold reheated steam pipe 19 and Boiler 1 connects.Steam turbine 2, condenser 3, condensate pump 4, low pressure heat regenerative system 5, oxygen-eliminating device 6, feed pump 7, high-pressure extraction system System 8 and boiler 1 are sequentially connected.
The two ends of the main steam bypass 18 in the present embodiment are connected on main steam pipe 17 and cold reheated steam pipe 19, Valve B12, reducing-and-cooling plant A9 and valve C13 are sequentially arranged in main steam bypass 18, and reducing-and-cooling plant B10 is by steaming Steam pipe branch road A23 is connected with oxygen-eliminating device 6, and on steam pipe branch road A23, reducing-and-cooling plant B10 passes through steam to valve F16 Pipe branch road B24 and condenser 3 connect, and on steam pipe branch road B24, reducing-and-cooling plant B10 passes through reheat heat to valve E15 Steam by-pass 21 and reheat heat steam pipe 20 connect, and valve D14 is arranged in reheat heat steam by-pass 21.
The step of operation method of the system of the raising thermoelectricity pure condensate unit motility in the present embodiment, is as follows.
When pure condensate unit load is quickly reduced or raised, adjusting feed pump 7 reduces its flow increase or flow(Until Close flow), now should ensure that the water level of the drum, oxygen-eliminating device 6 and condenser 3 of boiler 1 is limited in the minimum and highest for allowing Between, reuse drum, oxygen-eliminating device 6 and condenser 3 stores the quick response that emission capacity realizes unit load;Or, adjust Section condensate pump 4 makes its flow increase or flow reduction(Until closing flow), now should ensure that 1 drum of boiler, 6 and of oxygen-eliminating device The water level of condenser 3 reuses the storage heat release of drum, oxygen-eliminating device 6 and condenser 3 between the minimum and highest for allowing is limited Ability realizes the quick response of unit load.
When pure condensate unit load long-time is raised and lowered, machine is met by increasing or decreasing the evaporation capacity of boiler 1 The change of group load;If the evaporation capacity of boiler 1 cannot continue to reduce, main steam bypass 18 is opened, main steam is subtracted by desuperheat Pressure device A9 enters cold reheated steam pipe 19 after carrying out pressure and temperature reducing, Jing after 1 reheating of boiler, is subtracted by 21 Jing of reheat heat steam by-pass Warm decompressor B10 carries out pressure and temperature reducing.Then, condenser 3 is entered by steam pipe branch road B24, using the external of condenser 3 Heat dissipation capacity is realizing the response of unit load;And/or, oxygen-eliminating device 6 is entered by steam pipe branch road A23, using the storage of oxygen-eliminating device 6 Heat energy power is realizing the response of unit load.
This utility model appropriate design lifts the system and operational approach of thermoelectricity pure condensate unit motility, with this practicality After new, can give full play to the peak modulation capacity of pure condensate unit, strengthen response of the unit to network load, be that electrical network is dissolved wind-powered electricity generation In the wide space that new forms of energy are provided, therefore, it is worth with higher practice.
Furthermore, it is necessary to explanation, the specific embodiment described in this specification, is named the shape of its parts and components Claiming etc. can be with difference, and above the content described in this specification is only to this utility model structure example explanation. Equivalence changes or simple change that construction, feature and principle described in all foundation this utility model inventional ideas is done, wrap Include in the protection domain of this utility model patent.This utility model person of ordinary skill in the field can be to described Specific embodiment is made various modifications or supplements or substituted using similar mode, without departing from knot of the present utility model Structure surmounts scope defined in the claims, all should belong to protection domain of the present utility model.

Claims (3)

1. a kind of system for improving thermoelectricity pure condensate unit motility, including boiler(1), steam turbine(2), condenser(3), condensate Pump(4), low pressure heat regenerative system(5), oxygen-eliminating device(6), feed pump(7), high-pressure extraction system(8), main steam pipe(17), cold reheating Steam pipe(19)With reheat heat steam pipe(20), the boiler(1)By main steam pipe(17)With reheat heat steam pipe(20)With Steam turbine(2)Connection, the steam turbine(2)By cold reheated steam pipe(19)With boiler(1)Connection, the steam turbine(2), it is solidifying Vapour device(3), condensate pump(4), low pressure heat regenerative system(5), oxygen-eliminating device(6), feed pump(7), high-pressure extraction system(8)And boiler (1)It is sequentially connected, it is characterised in that:Also include reducing-and-cooling plant A(9), reducing-and-cooling plant B(10), valve B(12), valve Door C(13), valve D(14), valve E(15), valve F(16), main steam bypass(18), reheat heat steam by-pass(21), steam Pipe branch road A(23)With steam pipe branch road B(24), the main steam bypass(18)Two ends be connected to main steam pipe(17)With Cold reheated steam pipe(19)On, the valve B(12), reducing-and-cooling plant A(9)With valve C(13)It is sequentially arranged at main steam Bypass(18)On, the reducing-and-cooling plant B(10)By steam pipe branch road A(23)With oxygen-eliminating device(6)Connection, the valve F (16)Installed in steam pipe branch road A(23)On, the reducing-and-cooling plant B(10)By steam pipe branch road B(24)And condenser (3)Connection, the valve E(15)Installed in steam pipe branch road B(24)On, the reducing-and-cooling plant B(10)By reheat heat Steam by-pass(21)With reheat heat steam pipe(20)Connection, the valve D(14)Installed in reheat heat steam by-pass(21)On.
2. it is according to claim 1 improve thermoelectricity pure condensate unit motility system, it is characterised in that:Also include valve A (11), the valve A(11)Installed in main steam pipe(17)On.
3. it is according to claim 1 improve thermoelectricity pure condensate unit motility system, it is characterised in that:Also include valve H (22), the valve H(22)Installed in reheat heat steam pipe(20)On.
CN201620957697.6U 2016-08-29 2016-08-29 A kind of system for improving thermoelectricity pure condensate unit motility Withdrawn - After Issue CN206054015U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620957697.6U CN206054015U (en) 2016-08-29 2016-08-29 A kind of system for improving thermoelectricity pure condensate unit motility

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620957697.6U CN206054015U (en) 2016-08-29 2016-08-29 A kind of system for improving thermoelectricity pure condensate unit motility

Publications (1)

Publication Number Publication Date
CN206054015U true CN206054015U (en) 2017-03-29

Family

ID=58381983

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620957697.6U Withdrawn - After Issue CN206054015U (en) 2016-08-29 2016-08-29 A kind of system for improving thermoelectricity pure condensate unit motility

Country Status (1)

Country Link
CN (1) CN206054015U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106640237A (en) * 2016-08-29 2017-05-10 华电电力科学研究院 System for improving thermal power straight condensing unit flexibility and running method of system
CN109654580A (en) * 2019-01-29 2019-04-19 北京国电蓝天节能科技开发有限公司 Heating system based on low pressure (LP) cylinder optical axis

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106640237A (en) * 2016-08-29 2017-05-10 华电电力科学研究院 System for improving thermal power straight condensing unit flexibility and running method of system
CN106640237B (en) * 2016-08-29 2018-10-19 华电电力科学研究院 A kind of system and its operation method improving thermoelectricity pure condensate unit flexibility
CN109654580A (en) * 2019-01-29 2019-04-19 北京国电蓝天节能科技开发有限公司 Heating system based on low pressure (LP) cylinder optical axis

Similar Documents

Publication Publication Date Title
CN106640237B (en) A kind of system and its operation method improving thermoelectricity pure condensate unit flexibility
CN206668346U (en) The system that the high other and reheating heat of boiler promotes peak load regulation flexibility
CN208982124U (en) The heat and power system of unit fast lifting load is realized in a kind of combination heat supply
CN106401659B (en) A kind of step peak regulation system and its operation method for improving thermoelectricity unit thermoelectricity flexibility
CN103644004B (en) The cogeneration system of a kind of pair of turbine, combined cycle
CN106437876B (en) A kind of cogeneration units depth peak regulation system and its operation method
CN106979041A (en) A kind of turbine low pressure cylinder high vacuum takes off the remodeling method that cylinder runs thermoelectricity decoupled system
CN203685319U (en) Double-turbine combined-cycle combined heat and power supplying system
CN104314628B (en) A kind of coal unit and gas turbine combined power generation system
CN206035553U (en) Cogeneration system of combined cycle
CN206055732U (en) A kind of new heat-supplying unit
CN104976671B (en) Wide-load heat supply energy-saving system of back pressure type small steam turbine driven water feeding pump
CN106838865B (en) Completely thermoelectric decoupling steam extraction and heat supply power station system and working method
CN105736068A (en) High-back pressure combined heat and power generation system coupled with exhaust steam and supply heat of non-reheat steam turbine
CN206845247U (en) One kind enhancing power plant flexibility therrmodynamic system
CN206054015U (en) A kind of system for improving thermoelectricity pure condensate unit motility
CN110953571A (en) Heat supply steam residual pressure cascade utilization system applied to coal-fired heat supply unit
CN206054009U (en) A kind of cogeneration units depth peak regulation system
CN104061027B (en) The high temperature steam-extracting cooling system of Double reheat steam turbine thermodynamic system
CN102997309A (en) Classification heating system with high-temperature heat source heater bypass pipe
CN103696816A (en) Intermediate reheating small-capacity split axle type steam-turbine generator set
CN206617236U (en) A kind of gas cogeneration machine set system for being used to participate in peak load regulation network
CN206054008U (en) A kind of step peak regulation system for improving thermoelectricity unit thermoelectricity motility
CN206144612U (en) Utilize supercritical unit to realize high pressure cylinder steam extracting and heat supplying combined heat and power generation system
CN201826901U (en) Reheat type back pressure steam turbine

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
AV01 Patent right actively abandoned

Granted publication date: 20170329

Effective date of abandoning: 20181019

AV01 Patent right actively abandoned