CN113568443A - Method for controlling pressure behind valve of low-pressure bypass control system - Google Patents

Method for controlling pressure behind valve of low-pressure bypass control system Download PDF

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Publication number
CN113568443A
CN113568443A CN202110857600.XA CN202110857600A CN113568443A CN 113568443 A CN113568443 A CN 113568443A CN 202110857600 A CN202110857600 A CN 202110857600A CN 113568443 A CN113568443 A CN 113568443A
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Prior art keywords
pressure
low
reducing valve
bypass
pressure reducing
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CN202110857600.XA
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Chinese (zh)
Inventor
孙建国
程江南
范双双
马全乐
康君
戴云飞
于海东
李越男
赵新宇
马志国
郭峃峄
马巍
姚坤
刘东旭
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Inner Mongolia Mengda Power Generation Co ltd
Harbin Wohua Intelligent Power Generation Equipment Co ltd
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Inner Mongolia Mengda Power Generation Co ltd
Harbin Wohua Intelligent Power Generation Equipment Co ltd
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Priority to CN202110857600.XA priority Critical patent/CN113568443A/en
Publication of CN113568443A publication Critical patent/CN113568443A/en
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    • GPHYSICS
    • G05CONTROLLING; REGULATING
    • G05DSYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
    • G05D16/00Control of fluid pressure
    • G05D16/20Control of fluid pressure characterised by the use of electric means
    • G05D16/2006Control of fluid pressure characterised by the use of electric means with direct action of electric energy on controlling means
    • G05D16/2013Control of fluid pressure characterised by the use of electric means with direct action of electric energy on controlling means using throttling means as controlling means
    • G05D16/2026Control of fluid pressure characterised by the use of electric means with direct action of electric energy on controlling means using throttling means as controlling means with a plurality of throttling means
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F16ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
    • F16KVALVES; TAPS; COCKS; ACTUATING-FLOATS; DEVICES FOR VENTING OR AERATING
    • F16K31/00Actuating devices; Operating means; Releasing devices

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • General Engineering & Computer Science (AREA)
  • Fluid Mechanics (AREA)
  • Mechanical Engineering (AREA)
  • General Physics & Mathematics (AREA)
  • Automation & Control Theory (AREA)
  • Control Of Turbines (AREA)

Abstract

A method for controlling the pressure behind a valve of a low-pressure bypass control system relates to the technical field of power plant unit control. The invention aims to solve the problems that the temperature behind the pressure reducing valve is easily overhigh due to overlarge pressure behind the pressure reducing valve, so that the pressure of a low-side pressure reducing valve is quickly closed, the pressure of a reheater is quickly increased, and the action of a safety door of the reheater is caused; secondly, the vacuum degree of the condenser is easily reduced, and the low-vacuum protection action of the unit is stopped. When the low-pressure bypass control system is in an automatic control state, a PI (proportional integral) regulation result of the difference between the maximum pressure behind the low-bypass pressure reducing valve and the actual pressure behind the low-bypass pressure reducing valve is used as a low-bypass pressure reducing valve instruction, and when the low-pressure bypass control system is in a manual control state, the opening degree of the maximum low-bypass pressure reducing valve is used as a low-bypass pressure reducing valve instruction; and selecting the minimum value of the low bypass pressure reducing valve instruction and the reheater instruction as a final instruction of the low bypass pressure reducing valve, and controlling the opening of the low bypass pressure reducing valve by using the final instruction.

Description

Method for controlling pressure behind valve of low-pressure bypass control system
Technical Field
The invention belongs to the technical field of power plant unit control, and particularly relates to pressure behind a valve.
Background
The existing generating sets of I and II stages of power plants adopt thermal power generating sets with the rated power of 330 MW. The low-pressure bypass control system is mainly used for recovering working quality and ensuring smooth running of the unit impact rotation and the unit reverse cutting cylinder in a unit starting or accident state. The low-pressure bypass control system comprises a low bypass pressure reducing valve and a low bypass temperature reducing valve, and relates to a reheater pressure control system and a temperature control system behind the low bypass pressure reducing valve. In the reheater pressure control loop, a pressure set value is generated by the primary pressure of the steam turbine, and a reheater pressure measured value is output through a PI regulator after being deviated from the set value so as to control the opening of the low-bypass pressure reducing valve. The low side temperature reducing valve is a two-position control valve of a linked switch, and when the opening degree of the low side pressure reducing valve is more than 2%, the first-stage temperature reducing valve is linked; when the opening degree of the low by-pass reducing valve is more than 2% and the pressure behind the valve is more than 3.7bar, the two-stage temperature reducing valve is connected.
If the pressure behind the pressure reducing valve is continuously increased, the temperature behind the pressure reducing valve is easily overhigh, and when the temperature is higher than a certain value, the low bypass pressure reducing valve is quickly closed, so that the pressure of a reheater is quickly increased, and the action of a safety door of the reheater is caused. Moreover, the continuous increase of the pressure behind the pressure reducing valve can also cause the reduction of the vacuum degree of the condenser, thereby causing the shutdown of the low-vacuum protection action of the unit.
Disclosure of Invention
The invention aims to solve the problems that the temperature behind the pressure reducing valve is easily overhigh due to overlarge pressure behind the pressure reducing valve, so that the pressure of a low-side pressure reducing valve is quickly closed, the pressure of a reheater is quickly increased, and the action of a safety door of the reheater is caused; secondly, the vacuum degree of the condenser is easily reduced, and further the low vacuum protection action of the unit is stopped, and a method for controlling the pressure behind the valve of the low-pressure bypass control system is provided.
A method for controlling the pressure behind a valve of a low-pressure bypass control system specifically comprises the following steps:
when the low-pressure bypass control system is in an automatic control state, a PI (proportional integral) regulation result of the difference between the maximum pressure behind the low-bypass pressure reducing valve and the actual pressure behind the low-bypass pressure reducing valve is used as a low-bypass pressure reducing valve instruction, and when the low-pressure bypass control system is in a manual control state, the opening degree of the maximum low-bypass pressure reducing valve is used as a low-bypass pressure reducing valve instruction;
and selecting the minimum value of the low bypass pressure reducing valve instruction and the reheater instruction as a final instruction of the low bypass pressure reducing valve, and controlling the opening of the low bypass pressure reducing valve by using the final instruction.
Further, the reheater instructions are: PI regulation result of difference between reheater actual pressure and reheater set pressure.
Further, the maximum pressure X after the low-side pressure reducing valve1And actual pressure X after low side pressure reducing valve2PI regulation result Q of the difference1The expression is as follows:
Figure BDA0003184665320000021
wherein k ispFor proportional coefficient of PI regulation, kiFor the integral coefficient of the PI regulation,
Figure BDA0003184665320000022
the integral is represented.
Further, the reheater actual pressure Y1And reheater set pressure Y2PI regulation result Q of the difference2The expression is as follows:
Figure BDA0003184665320000023
wherein k ispFor proportional coefficient of PI regulation, kiFor the integral coefficient of the PI regulation,
Figure BDA0003184665320000024
the integral is represented.
Further, the maximum pressure behind the low-side pressure reducing valve is the maximum pressure allowed by the unit design.
The invention has the beneficial effects that:
1. in the production operation process, if the pressure behind the pressure reducing valve is continuously increased, the temperature behind the pressure reducing valve is easily overhigh, and when the temperature is higher than a certain value, the low-side pressure reducing valve is quickly closed, so that the pressure of a reheater is quickly increased, and the action of a reheater safety door is caused. The invention automatically controls the actual pressure after the low side pressure reducing valve, and can avoid the actual pressure after the low side pressure reducing valve from exceeding the maximum pressure after the low side pressure reducing valve, thereby avoiding the occurrence of the action of the safety door.
2. In the production operation process, the continuous increase of the pressure behind the pressure reducing valve can also cause the reduction of the vacuum degree of the condenser, thereby causing the shutdown of the low-vacuum protection action of the unit. The invention can avoid the problem of unit tripping caused by the reduction of the vacuum degree of the condenser due to overhigh pressure after the low-side pressure reducing valve.
3. The invention can effectively and automatically control the back pressure of the pressure reducing valve, reduce the labor intensity of operators in the starting or accident state of the unit and avoid the misoperation of the operators.
Drawings
Fig. 1 is a schematic diagram illustrating a method for controlling a post-valve pressure of a low-pressure bypass control system according to the present invention.
Detailed Description
The first embodiment is as follows: specifically describing the present embodiment with reference to fig. 1, the method for controlling the pressure after the valve in the low-pressure bypass control system according to the present embodiment includes:
when the low-pressure bypass control system is in an automatic control state, the maximum pressure X after the low-pressure bypass reducing valve allowed by the unit design is used1And actual pressure X after low side pressure reducing valve2PI regulation result Q of the difference1As the low side pressure reducing valve command, the expression is as follows:
Figure BDA0003184665320000025
and when the low-pressure bypass control system is in a manual control state, taking the opening degree of the maximum low bypass reducing valve as a command of the low bypass reducing valve.
The actual pressure Y of the reheater1And reheater set pressure Y2PI regulation result Q of the difference2As a reheater instruction, the expression is:
Figure BDA0003184665320000031
and selecting the minimum value of the low bypass pressure reducing valve instruction and the reheater instruction as a final instruction of the low bypass pressure reducing valve, and controlling the opening of the low bypass pressure reducing valve by using the final instruction.
In the above formula, kpFor proportional coefficient of PI regulation, kiFor the integral coefficient of the PI regulation,
Figure BDA0003184665320000032
the integral is represented.
In the production operation process, if the pressure behind the pressure reducing valve is continuously increased, the temperature behind the pressure reducing valve is easily overhigh, and when the temperature is higher than a certain value, the low-side pressure reducing valve is quickly closed, so that the pressure of a reheater is quickly increased, and the action of a reheater safety door is caused. The embodiment automatically controls the actual pressure behind the low-side pressure reducing valve, and can avoid the actual pressure behind the low-side pressure reducing valve from exceeding the maximum pressure behind the low-side pressure reducing valve, thereby avoiding the action of the safety door.
In addition, in the production operation process, the continuous increase of the pressure behind the pressure reducing valve can also cause the reduction of the vacuum degree of the condenser, thereby causing the shutdown of the low-vacuum protection action of the unit. This embodiment can avoid the condenser vacuum that the low side relief valve back pressure is too high to lead to reduce, and the unit tripping operation problem that arouses.
Moreover, the pressure behind the pressure reducing valve can be effectively and automatically controlled, the labor intensity of operators is reduced when the unit is started or in an accident state, and misoperation of the operators is avoided.

Claims (5)

1. A method for controlling the pressure behind the valve of a low-pressure bypass control system is characterized in that,
when the low-pressure bypass control system is in an automatic control state, a PI (proportional integral) regulation result of the difference between the maximum pressure behind the low-bypass pressure reducing valve and the actual pressure behind the low-bypass pressure reducing valve is used as a low-bypass pressure reducing valve instruction, and when the low-pressure bypass control system is in a manual control state, the opening degree of the maximum low-bypass pressure reducing valve is used as a low-bypass pressure reducing valve instruction;
and selecting the minimum value of the low bypass pressure reducing valve instruction and the reheater instruction as a final instruction of the low bypass pressure reducing valve, and controlling the opening of the low bypass pressure reducing valve by using the final instruction.
2. The method of claim 1, wherein the reheater instructions are: PI regulation result of difference between reheater actual pressure and reheater set pressure.
3. The method of claim 1, wherein the maximum post-low-pressure-bypass-relief-valve pressure X is a maximum post-low-pressure-bypass-relief-valve pressure X1And actual pressure X after low side pressure reducing valve2PI regulation result Q of the difference1The expression is as follows:
Figure FDA0003184665310000011
wherein k ispFor proportional coefficient of PI regulation, kiFor the integral coefficient of the PI regulation,
Figure FDA0003184665310000012
the integral is represented.
4. The method of claim 2, wherein the reheater actual pressure Y is set to be equal to or greater than the reheater actual pressure Y1And reheater set pressure Y2PI regulation result Q of the difference2The expression is as follows:
Figure FDA0003184665310000013
wherein k ispFor proportional coefficient of PI regulation, kiFor the integral coefficient of the PI regulation,
Figure FDA0003184665310000014
the integral is represented.
5. The method for controlling the pressure after the valve of the low-pressure bypass control system according to the claim 1, 2, 3 or 4, wherein the maximum pressure after the low-pressure bypass reducing valve is the maximum pressure allowed by the unit design.
CN202110857600.XA 2021-07-28 2021-07-28 Method for controlling pressure behind valve of low-pressure bypass control system Pending CN113568443A (en)

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA1138657A (en) * 1978-06-08 1983-01-04 Mitsuhisa Yokota Control system for steam turbine plants including turbine bypass systems
CN109442368A (en) * 2018-09-21 2019-03-08 国网辽宁省电力有限公司电力科学研究院 A kind of bypath system integrated control method promoting thermal power plant unit regulating power
CN111828110A (en) * 2020-07-22 2020-10-27 西安热工研究院有限公司 Control method for automatic steam retention of MFT (post-MFT) auxiliary steam of boiler of double reheating unit
CN111853906A (en) * 2020-08-11 2020-10-30 西安热工研究院有限公司 Automatic adjusting method and system for heat supply high-low pressure bypass valve of thermal power generating unit

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA1138657A (en) * 1978-06-08 1983-01-04 Mitsuhisa Yokota Control system for steam turbine plants including turbine bypass systems
CN109442368A (en) * 2018-09-21 2019-03-08 国网辽宁省电力有限公司电力科学研究院 A kind of bypath system integrated control method promoting thermal power plant unit regulating power
CN111828110A (en) * 2020-07-22 2020-10-27 西安热工研究院有限公司 Control method for automatic steam retention of MFT (post-MFT) auxiliary steam of boiler of double reheating unit
CN111853906A (en) * 2020-08-11 2020-10-30 西安热工研究院有限公司 Automatic adjusting method and system for heat supply high-low pressure bypass valve of thermal power generating unit

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
付兴;费阳阳;: "火力发电厂简易高、低压旁路系统控制及改进", 科技创新导报, no. 05 *
凌晓定: "旁路系统控制策略的应用分析", 华东电力, no. 07 *
戴连波;: "北仑电厂1号机组旁路控制系统改造设计", 机电信息, no. 06 *

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