CN111810926A - A device for adjusting the temperature of a final stage reheater and its operation method - Google Patents
A device for adjusting the temperature of a final stage reheater and its operation method Download PDFInfo
- Publication number
- CN111810926A CN111810926A CN202010784624.2A CN202010784624A CN111810926A CN 111810926 A CN111810926 A CN 111810926A CN 202010784624 A CN202010784624 A CN 202010784624A CN 111810926 A CN111810926 A CN 111810926A
- Authority
- CN
- China
- Prior art keywords
- hydraulic cylinder
- final
- reheater
- temperature
- piston rod
- 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.)
- Granted
Links
- 238000000034 method Methods 0.000 title claims abstract description 14
- 239000000779 smoke Substances 0.000 claims abstract description 48
- 238000010438 heat treatment Methods 0.000 claims abstract description 21
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 26
- 239000003546 flue gas Substances 0.000 claims description 26
- 229910052783 alkali metal Inorganic materials 0.000 claims description 4
- 150000001340 alkali metals Chemical class 0.000 claims description 4
- 239000010881 fly ash Substances 0.000 claims description 4
- 239000002245 particle Substances 0.000 claims description 4
- 239000012774 insulation material Substances 0.000 claims description 3
- 230000001105 regulatory effect Effects 0.000 claims description 3
- 230000033228 biological regulation Effects 0.000 claims description 2
- 230000003750 conditioning effect Effects 0.000 claims 4
- 230000004888 barrier function Effects 0.000 claims 2
- 239000002893 slag Substances 0.000 claims 2
- 230000007774 longterm Effects 0.000 abstract description 6
- 238000011109 contamination Methods 0.000 abstract description 3
- 238000010977 unit operation Methods 0.000 abstract description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- 238000011017 operating method Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000010248 power generation Methods 0.000 description 2
- 230000008646 thermal stress Effects 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 206010022000 influenza Diseases 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 238000003303 reheating Methods 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
- F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
- F22B1/18—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22D—PREHEATING, OR ACCUMULATING PREHEATED, FEED-WATER FOR STEAM GENERATION; FEED-WATER SUPPLY FOR STEAM GENERATION; CONTROLLING WATER LEVEL FOR STEAM GENERATION; AUXILIARY DEVICES FOR PROMOTING WATER CIRCULATION WITHIN STEAM BOILERS
- F22D1/00—Feed-water heaters, i.e. economisers or like preheaters
- F22D1/02—Feed-water heaters, i.e. economisers or like preheaters with water tubes arranged in the boiler furnace, fire tubes or flue ways
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22G—SUPERHEATING OF STEAM
- F22G1/00—Steam superheating characterised by heating method
- F22G1/02—Steam superheating characterised by heating method with heat supply by hot flue gases from the furnace of the steam boiler
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J13/00—Fittings for chimneys or flues
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/06—Arrangements of devices for treating smoke or fumes of coolers
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chimneys And Flues (AREA)
- Control Of Steam Boilers And Waste-Gas Boilers (AREA)
Abstract
本发明公开了一种末级再热器温度调节的装置及其运行方法,包括控制器、旋转电机、主动轮、从动轮、液压缸、液压缸活塞杆、遮烟挡板以及用于提供电能的电源箱,其中,遮烟挡板位于锅炉水平烟道内高温过热器与末级再热器之间,旋转电机的输出轴与主动轮相连接,主动轮与从动轮相配合,从动轮与遮烟挡板的上端相连接,液压缸活塞杆的一端与液压缸相配合,液压缸活塞杆的另一端插入于锅炉水平烟道内后与遮烟挡板相连接,控制器与活塞缸的控制端及旋转电机的控制端相连接,该装置及其运行方法能够有效缓解锅炉长期高负荷运行状态下末级再热器受热面沾污结渣现象,提高机组运行安全可靠性。
The invention discloses a device for adjusting the temperature of a final-stage reheater and an operation method thereof, comprising a controller, a rotating motor, a driving wheel, a driven wheel, a hydraulic cylinder, a piston rod of the hydraulic cylinder, a smoke shielding baffle, and a device for supplying electric energy. The power box of the power supply box, in which the smoke shielding baffle is located between the high temperature superheater and the final stage reheater in the horizontal flue of the boiler, the output shaft of the rotating motor is connected with the driving wheel, the driving wheel is matched with the driven wheel, and the driven wheel is connected with the shielding wheel. The upper end of the smoke baffle is connected, one end of the piston rod of the hydraulic cylinder is matched with the hydraulic cylinder, the other end of the piston rod of the hydraulic cylinder is inserted into the horizontal flue of the boiler and connected to the smoke shielding baffle, and the controller is connected to the control end of the piston cylinder. The device and its operation method can effectively alleviate the contamination and slagging phenomenon of the heating surface of the final stage reheater under the long-term high-load operation state of the boiler, and improve the safety and reliability of the unit operation.
Description
技术领域technical field
本发明属于燃煤锅炉受热面温度调节技术领域,涉及一种末级再热器温度调节的装置及其运行方法。The invention belongs to the technical field of temperature regulation of the heating surface of a coal-fired boiler, and relates to a device for regulating the temperature of a final stage reheater and an operation method thereof.
背景技术Background technique
近年来,电力行业发展迅速,超临界及超超临界火电机组已成为我国现役主力机组。随着电站锅炉向高参数、大容量的方向发展,炉内燃烧不均衡所导致的汽温偏差及受热面超温问题日益严重,已成为影响机组安全稳定运行的主要问题之一。同时,由于用电结构的变化,民用电量不断增加,电网峰谷差日趋增大,火电机组在带基本负荷的同时将参与更多的调峰任务,频繁的升降负荷给汽温的调节带来不利影响。In recent years, the power industry has developed rapidly, and supercritical and ultra-supercritical thermal power units have become the main units in active service in my country. With the development of high-parameter and large-capacity power plant boilers, the problems of steam temperature deviation and heating surface overtemperature caused by unbalanced combustion in the furnace have become increasingly serious, which has become one of the main problems affecting the safe and stable operation of the unit. At the same time, due to the changes in the power consumption structure, the civil power consumption is increasing, and the peak-to-valley difference of the power grid is increasing. Negative Effects.
锅炉受热面区域烟气流速与烟温分布不均匀会导致屏式过热器、高温过热器、末级再热器等受热面吸热不均,汽温过高会加快换热器金属材料蠕变,使过热器、再热器管壁产生额外热应力,缩短了设备使用寿命,长期运行会引起受热面超温甚至爆管;汽温过低会造成汽轮机末级蒸汽湿度增大,汽轮机叶片侵蚀加剧,严重时发生水击现象,此外,汽温下降影响汽轮机发电效率,机组发电煤耗上升。为控制管壁温度在合理范围,通常需降低主汽温度及再热汽温运行,同时,当锅炉两侧烟温偏差较大时,无法合理控制减温水量,导致机组整体运行经济性下降。The uneven distribution of flue gas flow rate and flue temperature in the heating surface area of the boiler will lead to uneven heat absorption of the heating surfaces such as the screen superheater, high temperature superheater, and final reheater, and excessive steam temperature will accelerate the creep of the metal material of the heat exchanger. , causing extra thermal stress on the tube wall of the superheater and reheater, shortening the service life of the equipment, and long-term operation will cause the heating surface to overheat or even burst the tube; if the steam temperature is too low, the humidity of the steam in the final stage of the steam turbine will increase, and the steam turbine blades will be eroded. In addition, the drop in steam temperature affects the power generation efficiency of the steam turbine, and the coal consumption of the power generation unit increases. In order to control the tube wall temperature within a reasonable range, it is usually necessary to reduce the main steam temperature and reheat steam temperature. At the same time, when the flue gas temperature deviation on both sides of the boiler is large, the amount of desuperheating water cannot be reasonably controlled, resulting in a decline in the overall operating economy of the unit.
汽温调节的方法主要分为蒸汽侧调节和烟气侧调节两大类,对于末级再热器汽温的调节方式,通常以烟气侧调调节为主,常见方法有烟气再循环,分隔烟道挡板及改变火焰中心位置,同时还会设置有再热器事故喷水减温器以用于紧急事故工况、快速变负荷工况或其它非稳定工况。上述调节方法在目前机组运行过程中均存在不同程度的问题:如采用分隔烟道挡板法汽温调节时滞性过大,挡板开度与气温非线性关系,挡板只在一定开度范围内有良好的调节效果;改变火焰中心的调节方法灵敏度高、时滞性小,但精度不高,种种不利因素给机组快速变负荷过程中的末级再热汽温的调节造成困难。The methods of steam temperature adjustment are mainly divided into two categories: steam side adjustment and flue gas side adjustment. For the adjustment method of the steam temperature of the final reheater, the flue gas side adjustment is usually the main method. The common methods include flue gas recirculation, Separate the flue baffle and change the position of the center of the flame. At the same time, a reheater accident water spray desuperheater is also provided for emergency conditions, rapid load changes or other unstable conditions. The above adjustment methods all have different degrees of problems in the current operation of the unit: if the time lag of the steam temperature adjustment is too large by using the baffle method of separating the flue, the baffle opening has a nonlinear relationship with the air temperature, and the baffle only has a certain opening. It has a good adjustment effect within the range; the adjustment method of changing the flame center has high sensitivity and small time lag, but the accuracy is not high.
发明内容SUMMARY OF THE INVENTION
本发明的目的在于克服上述现有技术的缺点,提供了一种末级再热器温度调节的装置及其运行方法,该装置及其运行方法能够有效缓解锅炉长期高负荷运行状态下末级再热器受热面沾污结渣现象,提高机组运行安全可靠性。The purpose of the present invention is to overcome the above-mentioned shortcomings of the prior art, and to provide a device for adjusting the temperature of the final stage reheater and an operating method thereof, which can effectively alleviate the long-term high-load operation of the boiler under the condition of long-term high-load operation. The heating surface of the heater is contaminated with slagging, which improves the safety and reliability of the unit operation.
为达到上述目的,本发明所述的末级再热器温度调节的装置包括控制器、旋转电机、主动轮、从动轮、液压缸、液压缸活塞杆、遮烟挡板以及用于提供电能的电源箱,其中,遮烟挡板位于锅炉水平烟道内高温过热器与末级再热器之间,旋转电机的输出轴与主动轮相连接,主动轮与从动轮相配合,从动轮与遮烟挡板的上端相连接,液压缸活塞杆的一端与液压缸相配合,液压缸活塞杆的另一端插入于锅炉水平烟道内后与遮烟挡板相连接,控制器与活塞缸的控制端及旋转电机的控制端相连接。In order to achieve the above purpose, the device for adjusting the temperature of the final stage reheater according to the present invention includes a controller, a rotating motor, a driving wheel, a driven wheel, a hydraulic cylinder, a piston rod of a hydraulic cylinder, a smoke shielding baffle, and a device for providing electrical energy. The power box, wherein the smoke shielding baffle is located between the high temperature superheater and the final stage reheater in the horizontal flue of the boiler, the output shaft of the rotating motor is connected with the driving wheel, the driving wheel is matched with the driven wheel, and the driven wheel is connected with the smoke shielding The upper end of the baffle is connected, one end of the piston rod of the hydraulic cylinder is matched with the hydraulic cylinder, and the other end of the piston rod of the hydraulic cylinder is inserted into the horizontal flue of the boiler and connected to the smoke shielding baffle. The control terminal of the rotating motor is connected.
旋转电机的输出轴通过第一连杆与主动轮相连接。The output shaft of the rotary electric machine is connected with the driving wheel through the first connecting rod.
从动轮通过第二连杆与遮烟挡板的上端相连接。The driven wheel is connected with the upper end of the smoke shielding baffle through the second connecting rod.
遮烟挡板上以及液压缸活塞杆与锅炉水平烟道的连接位置处均包裹有保温材料层。The smoke shielding baffle plate and the connecting position of the piston rod of the hydraulic cylinder and the horizontal flue of the boiler are wrapped with a layer of thermal insulation material.
主动轮与从动轮之间通过螺纹相配合。The driving wheel and the driven wheel are matched by threads.
液压缸活塞杆的端部设置有耳座,耳座与遮烟挡板的上端相连接。The end of the piston rod of the hydraulic cylinder is provided with an ear seat, and the ear seat is connected with the upper end of the smoke shielding baffle.
旋转电机通过电源箱固定于锅炉水平烟道的外壁上。The rotating motor is fixed on the outer wall of the horizontal flue of the boiler through the power box.
本发明所述末级再热器温度调节的装置的运行方法包括以下步骤:The operating method of the device for adjusting the temperature of the final stage reheater according to the present invention comprises the following steps:
当末级再热器结渣严重时,控制器控制液压缸工作,液压缸驱动液压缸活塞杆伸出,液压缸活塞杆带动遮烟挡板下落至末级再热器的前迎风侧,通过遮烟挡板遮挡高温烟气,减少末级再热器与高温烟气的对流换热,阻挡烟气中的飞灰颗粒及熔融态碱金属附着在末级再热器的受热面管壁处,减轻末级再热器受热面的沾污结渣;When the slagging of the final reheater is serious, the controller controls the hydraulic cylinder to work, the hydraulic cylinder drives the piston rod of the hydraulic cylinder to extend, and the piston rod of the hydraulic cylinder drives the smoke shielding baffle to fall to the front windward side of the final reheater. The smoke shielding baffle shields the high temperature flue gas, reduces the convection heat exchange between the final reheater and the high temperature flue gas, and prevents the fly ash particles and molten alkali metals in the flue gas from adhering to the heating surface tube wall of the final reheater , to reduce the contamination and slagging of the heating surface of the final reheater;
当末级再热器两侧汽温偏差大于预设值时,则控制器控制液压缸工作,液压缸驱动液压缸活塞杆伸出,液压缸活塞杆带动遮烟挡板下落至末级再热器的前迎风侧,然后控制旋转电机工作,旋转电机带动主动轮旋转,主动轮带动从动轮旋转,从动轮带动遮烟挡板在水平烟道内旋转,改变遮烟挡板与烟气来流方向的夹角,以调节末级再热器与高温烟气的对流换热量,继而调节末级再热器的出口温度,减小末级再热器事故减温水的喷水量,提高锅炉经济性。When the steam temperature deviation on both sides of the final stage reheater is greater than the preset value, the controller controls the hydraulic cylinder to work, the hydraulic cylinder drives the hydraulic cylinder piston rod to extend, and the hydraulic cylinder piston rod drives the smoke shielding baffle to fall to the final stage reheating The front windward side of the device, and then control the rotating motor to work, the rotating motor drives the driving wheel to rotate, the driving wheel drives the driven wheel to rotate, and the driven wheel drives the smoke shielding baffle to rotate in the horizontal flue, changing the direction of the smoke shielding baffle and the flow of smoke. In order to adjust the convective heat exchange between the last-stage reheater and the high-temperature flue gas, and then adjust the outlet temperature of the last-stage reheater, reduce the amount of water sprayed by the accidental desuperheating water of the last-stage reheater, and improve the boiler economy. sex.
本发明具有以下有益效果:The present invention has the following beneficial effects:
本发明所述的末级再热器温度调节的装置及其运行方法在具体操作时,当末级再热器结渣严重时,液压缸推动液压缸活塞杆伸出,将遮烟挡板下落至末级再热器的前迎风侧,通过遮烟挡板遮挡高温烟气,减少末级再热器与高温烟气的对流换热,阻挡烟气中的飞灰颗粒及熔融态碱金属附着在末级再热器的受热面管壁处,减轻末级再热器受热面的沾污结渣,有效缓解锅炉长期高负荷运行状态下末级再热器受热面沾污结渣现象。另外,当末级再热器两侧汽温偏差过大时,通过旋转电机带动遮烟挡板在水平烟道内旋转,改变遮烟挡板与烟气来流方向的夹角,以调节末级再热器与高温烟气的对流换热量,继而调节末级再热器的出口温度,减小末级再热器事故减温水的喷水量,提高锅炉经济性,同时减小炉膛两侧烟温偏差及流场不均,避免末级再热器局部金属过热超温导致的爆管频发现象,提高机组运行安全可靠性。During the specific operation of the device for adjusting the temperature of the final stage reheater and the operation method thereof, when the slagging of the final stage reheater is serious, the hydraulic cylinder pushes the piston rod of the hydraulic cylinder to extend, and the smoke shielding baffle falls down. To the front windward side of the last stage reheater, the high temperature flue gas is blocked by the smoke shielding baffle, which reduces the convection heat exchange between the last stage reheater and the high temperature flue gas, and prevents the adhesion of fly ash particles and molten alkali metals in the flue gas. At the tube wall of the heating surface of the last stage reheater, the fouling and slagging of the heating surface of the last stage reheater is reduced, and the phenomenon of fouling and slagging on the heating surface of the last stage reheater under the long-term high-load operation of the boiler is effectively alleviated. In addition, when the steam temperature deviation on both sides of the final stage reheater is too large, the rotating motor drives the smoke shielding baffle to rotate in the horizontal flue to change the angle between the smoke shielding baffle and the inflow direction of the flue gas to adjust the final stage. The convective heat exchange between the reheater and the high temperature flue gas, and then adjust the outlet temperature of the last stage reheater, reduce the amount of water sprayed by the accident desuperheating water of the last stage reheater, improve the boiler economy, and reduce the temperature on both sides of the furnace. The flue gas temperature deviation and the uneven flow field can avoid the frequent occurrence of pipe bursts caused by the overheating and overtemperature of the metal in the final stage reheater, and improve the safety and reliability of the unit operation.
附图说明Description of drawings
图1为本发明的设置位置图;Fig. 1 is the setting position diagram of the present invention;
图2为本发明的结构示意图;Fig. 2 is the structural representation of the present invention;
图3为本发明的运行示意图。FIG. 3 is a schematic diagram of the operation of the present invention.
其中,1为省煤器、2为炉膛水冷壁、3为低温过热器、4为屏式过热器、5为高温过热器、6为低温再热器、7为末级再热器、81为电源箱、82为旋转电机、83为主动轮、84为从动轮、85为液压缸、86为液压缸活塞杆、87为耳座、88为遮烟挡板。Among them, 1 is the economizer, 2 is the furnace water wall, 3 is the low temperature superheater, 4 is the screen superheater, 5 is the high temperature superheater, 6 is the low temperature reheater, 7 is the final stage reheater, and 81 is the Power box, 82 is a rotating motor, 83 is a driving wheel, 84 is a driven wheel, 85 is a hydraulic cylinder, 86 is a hydraulic cylinder piston rod, 87 is an ear seat, and 88 is a smoke shielding baffle.
具体实施方式Detailed ways
下面结合附图对本发明做进一步详细描述:Below in conjunction with accompanying drawing, the present invention is described in further detail:
参考图1及图2,图1中A为本发明,本发明所述的末级再热器温度调节的装置包括控制器、旋转电机82、主动轮83、从动轮84、液压缸85、液压缸活塞杆86、遮烟挡板88以及用于提供电能的电源箱81,其中,遮烟挡板88位于锅炉水平烟道内高温过热器5与末级再热器7之间,旋转电机82的输出轴与主动轮83相连接,主动轮83与从动轮84相配合,从动轮84与遮烟挡板88的上端相连接,液压缸活塞杆86的一端与液压缸85相配合,液压缸活塞杆86的另一端插入于锅炉水平烟道内后与遮烟挡板88相连接,控制器与活塞缸85的控制端及旋转电机82的控制端相连接。Referring to FIG. 1 and FIG. 2, A in FIG. 1 is the present invention, and the device for adjusting the temperature of the final stage reheater according to the present invention includes a controller, a
旋转电机82的输出轴通过第一连杆与主动轮83相连接;从动轮84通过第二连杆与遮烟挡板88的上端相连接;遮烟挡板88上以及液压缸活塞杆86与锅炉水平烟道的连接位置处均包裹有保温材料层;主动轮83与从动轮84之间通过螺纹相配合;液压缸活塞杆86的端部设置有耳座87,耳座87与遮烟挡板88的上端相连接;旋转电机82通过电源箱81固定于锅炉水平烟道的外壁上。The output shaft of the
本发明所述末级再热器温度调节的装置的运行方法包括以下步骤:The operating method of the device for adjusting the temperature of the final stage reheater according to the present invention comprises the following steps:
燃料燃烧后所产生的高温烟气首先将热量传递给炉膛水冷壁2和屏式过热器4,随后由水平烟道依次经过高温过热器5与末级再热器7后进入竖井烟道,竖井烟道中隔墙将烟道分为前、后两个平行烟道,前烟道内布置低温再热器6,后烟道内布置低温过热器3和省煤器1,本发明中的遮烟挡板8位于水平烟道内高温过热器5与末级再热器7之间;The high-temperature flue gas generated after the fuel is burned first transfers heat to the
锅炉正常运行过程中,末级再热器7管壁无超温现象,末级再热器7出口蒸汽温度偏差在设计范围内,末级再热器7的受热面无严重沾污结渣状态下,末级再热器温度调节的装置无需投入使用;During the normal operation of the boiler, there is no over-temperature phenomenon on the tube wall of the
当锅炉长期高负荷运行时,由于炉内平均热负荷大与预设热负荷值,当末级再热器7结渣严重时,则控制液压缸85工作,液压缸85驱动液压缸活塞杆86伸出,液压缸活塞杆86带动遮烟挡板88下落至末级再热器7的前迎风侧,通过遮烟挡板88遮挡高温烟气,减少末级再热器7与高温烟气的对流换热,阻挡烟气中的飞灰颗粒及熔融态碱金属附着在末级再热器7的受热面管壁处,减轻末级再热器7受热面的沾污结渣;当末级再热器7管壁超温时,通过遮烟挡板88的开度,以缓解管壁超温现象;When the boiler runs at high load for a long time, due to the large average heat load in the furnace and the preset heat load value, when the slagging of the
当锅炉处于变负荷或深度调峰运行时,炉膛内火焰充满度不高,由于热负荷分布不均两侧末级再热器7易产生热偏差、热应力不均衡等问题,长期热偏差容易使受热面管壁拉裂,严重时造成局部金属过热超温,甚至爆管。当末级再热器7两侧汽温偏差过大时,则控制液压缸85工作,液压缸85驱动液压缸活塞杆86伸出,液压缸活塞杆86带动遮烟挡板88下落至末级再热器7的前迎风侧,然后控制旋转电机82工作,旋转电机82带动主动轮83旋转,主动轮83带动从动轮84旋转,从动轮84通过带动遮烟挡板88在水平烟道内旋转,改变遮烟挡板88与烟气来流方向的夹角,以调节末级再热器7与高温烟气的对流换热量,继而调节末级再热器7的出口温度,减小末级再热器7事故减温水的喷水量,提高锅炉经济性。When the boiler is in variable load or deep peak shaving operation, the fullness of the flame in the furnace is not high. Due to the uneven distribution of heat load, the
经实践,本发明可以有效的保持受热面清洁,同时可减小受热面对流换热量,保证受热面安全,提高锅炉安全稳定运行时间,提高机组效率。Through practice, the present invention can effectively keep the heating surface clean, and at the same time can reduce the heat exchange of the heating surface, ensure the safety of the heating surface, improve the safe and stable operation time of the boiler, and improve the efficiency of the unit.
Claims (8)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202010784624.2A CN111810926B (en) | 2020-08-06 | 2020-08-06 | A device for regulating temperature of a final stage reheater and an operating method thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202010784624.2A CN111810926B (en) | 2020-08-06 | 2020-08-06 | A device for regulating temperature of a final stage reheater and an operating method thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
CN111810926A true CN111810926A (en) | 2020-10-23 |
CN111810926B CN111810926B (en) | 2025-01-07 |
Family
ID=72863713
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202010784624.2A Active CN111810926B (en) | 2020-08-06 | 2020-08-06 | A device for regulating temperature of a final stage reheater and an operating method thereof |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN111810926B (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112944323A (en) * | 2020-12-31 | 2021-06-11 | 大唐郓城发电有限公司 | 630 ℃ double reheat boiler three-flue control method |
CN113280359A (en) * | 2021-06-25 | 2021-08-20 | 西安热工研究院有限公司 | Method for reducing contamination of convection heating surface of n-shaped high-sodium coal boiler |
CN114198737A (en) * | 2021-12-22 | 2022-03-18 | 华电新疆哈密煤电开发有限公司 | Ultra-supercritical boiler with flue gas flow field deviation eliminating device |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN208365520U (en) * | 2018-05-14 | 2019-01-11 | 华能国际电力股份有限公司海门电厂 | A kind of full load section reheating temperature intelligent controlling device |
CN208886863U (en) * | 2018-08-09 | 2019-05-21 | 宁波方太厨具有限公司 | A kind of range hood with smoke barrier |
CN212777273U (en) * | 2020-08-06 | 2021-03-23 | 华能国际电力股份有限公司 | A device for adjusting the temperature of the final stage reheater |
-
2020
- 2020-08-06 CN CN202010784624.2A patent/CN111810926B/en active Active
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN208365520U (en) * | 2018-05-14 | 2019-01-11 | 华能国际电力股份有限公司海门电厂 | A kind of full load section reheating temperature intelligent controlling device |
CN208886863U (en) * | 2018-08-09 | 2019-05-21 | 宁波方太厨具有限公司 | A kind of range hood with smoke barrier |
CN212777273U (en) * | 2020-08-06 | 2021-03-23 | 华能国际电力股份有限公司 | A device for adjusting the temperature of the final stage reheater |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112944323A (en) * | 2020-12-31 | 2021-06-11 | 大唐郓城发电有限公司 | 630 ℃ double reheat boiler three-flue control method |
CN113280359A (en) * | 2021-06-25 | 2021-08-20 | 西安热工研究院有限公司 | Method for reducing contamination of convection heating surface of n-shaped high-sodium coal boiler |
CN114198737A (en) * | 2021-12-22 | 2022-03-18 | 华电新疆哈密煤电开发有限公司 | Ultra-supercritical boiler with flue gas flow field deviation eliminating device |
Also Published As
Publication number | Publication date |
---|---|
CN111810926B (en) | 2025-01-07 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN111810926A (en) | A device for adjusting the temperature of a final stage reheater and its operation method | |
CN111256162B (en) | Slag bonding and coking prevention system and method for low ash fusion point coal blending boiler | |
CN107270274B (en) | Novel starting mode of ultra-supercritical coal-fired unit realizes unit full-load denitration input | |
CN207975627U (en) | It is suitable for using the 660MW grade ultra-supercritical boilers of high alkalinity coal | |
CN106640235A (en) | Subcritical direct air cooling unit cold starting method | |
CN109114539A (en) | A kind of boiler system and its loss protecting method | |
CN111486440A (en) | A system and method for adjusting the reheated steam temperature of a W flame boiler by adopting flue gas recirculation | |
WO2023202634A1 (en) | Flue gas circulation system for improving combustion characteristics and thermal characteristics of pulverized coal fired boiler | |
CN111603928B (en) | An efficient, clean, flexible and collaborative coal-fired power generation system and operation method | |
CN106895390A (en) | A kind of station boiler multi-element heterogeneous afterheat utilizing system | |
CN103277783A (en) | Supercritical coal-fired unit water wall metal wall temperature early-warning optimal control method | |
CN112097232A (en) | Water-cooled wall over-temperature control system and method for coal-fired units based on wall temperature prediction | |
CN205119100U (en) | Owner, reheat steam temperature and exhaust gas temperature adjustable boiler afterbody flue structure | |
CN212777273U (en) | A device for adjusting the temperature of the final stage reheater | |
CN113091046B (en) | Double reheat boiler and its outlet steam temperature control method and device | |
CN112797398A (en) | Ultra-supercritical secondary reheating unit boiler temperature regulating system | |
CN206682921U (en) | A kind of station boiler multi-element heterogeneous afterheat utilizing system | |
CN109603526A (en) | A biomass power plant flue gas treatment system | |
CN202101217U (en) | Biomass steam boiler with horizontal water and fire tubes | |
CN206737963U (en) | A kind of combustion engine coal machine coupled electricity-generation system | |
CN113719816B (en) | A temperature-adjustable supercritical carbon dioxide boiler system with multiple flue structures | |
CN205191536U (en) | Three channels power plant boiler suitable for 700 DEG C steam condition | |
CN209876904U (en) | Boiler low-temperature flue gas recirculation combustion system | |
CN209341293U (en) | A kind of boiler preheating device | |
CN113282034A (en) | Peak regulation method of ultra-supercritical thermal power generating unit |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |