CN110813514B - A non-automatic self-adjusting gas-solid two-phase distributor - Google Patents
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- 239000007787 solid Substances 0.000 title claims abstract description 16
- 239000000843 powder Substances 0.000 claims abstract description 50
- 239000003245 coal Substances 0.000 claims abstract description 26
- 238000000576 coating method Methods 0.000 claims description 6
- 238000013461 design Methods 0.000 claims description 5
- 230000008859 change Effects 0.000 abstract description 4
- 230000004044 response Effects 0.000 abstract description 2
- 238000002485 combustion reaction Methods 0.000 description 11
- 238000010586 diagram Methods 0.000 description 6
- 239000011248 coating agent Substances 0.000 description 5
- 230000007423 decrease Effects 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Substances N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 5
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 239000000446 fuel Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 206010021143 Hypoxia Diseases 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000003044 adaptive effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000011017 operating method Methods 0.000 description 1
- 125000000864 peroxy group Chemical group O(O*)* 0.000 description 1
- 230000008569 process Effects 0.000 description 1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/18—Adding fluid, other than for crushing or disintegrating by fluid energy
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Abstract
一种非能动自调节的气固两相分配器,包括分配器本体,分配器本体包括在出口风粉替代管顶部焊接支撑顶座,支撑顶座包括内圈与外圈,外圈直径与原磨煤机出口风粉管直径相等,位于内圈下方设置有阻力元件,阻力元件底端设置限位装置,位于出口风粉替代管上设置有导向滑道,导向滑道用于使阻力元件按固定路线发生形变。本发明在调节风粉流速上,可根绝磨煤机实际运行工况,实时动态调节各个出口风粉管流通阻力,响应速度快,工作量小,设备异动小,且方便更换。
A non-automatic self-adjusting gas-solid two-phase distributor, comprising a distributor body, the distributor body including a support top seat welded on the top of an outlet air powder substitute pipe, the support top seat including an inner ring and an outer ring, the diameter of the outer ring is the same as the original diameter. The diameter of the outlet air powder pipe of the coal mill is equal, a resistance element is arranged under the inner ring, the bottom end of the resistance element is provided with a limiting device, and a guide slide is arranged on the outlet air powder substitute pipe, and the guide slide is used to make the resistance element press The fixed route is deformed. In adjusting the air-powder flow rate, the invention can eliminate the actual operating conditions of the coal mill, dynamically adjust the flow resistance of each outlet air-powder pipe in real time, has fast response speed, small workload, small equipment change and convenient replacement.
Description
技术领域technical field
本发明涉及燃煤电站磨煤机系统技术领域,特别涉及一种非能动自调节的气固两相分配器。The invention relates to the technical field of coal mill systems in coal-fired power stations, in particular to a non-automatic self-adjusting gas-solid two-phase distributor.
背景技术Background technique
为实现氮氧化物超低排放,燃煤电站普遍使用炉内低氮燃烧技术,即浓淡分离燃烧器、空气分级燃烧、燃料分级燃烧等。上述技术的共同核心就是通过对煤粉和一/二次风的精确控制实现主燃烧区域成还原性气氛(空气过量系数小于1)。In order to achieve ultra-low emission of nitrogen oxides, coal-fired power plants generally use low-nitrogen combustion technologies in the furnace, namely, concentration-lean separation burners, air staged combustion, and fuel staged combustion. The common core of the above technologies is to achieve a reducing atmosphere in the main combustion area (the excess air factor is less than 1) through precise control of pulverized coal and primary/secondary air.
由于煤质差异大、磨煤机入口一次风量测量存在误差等原因,磨煤机实际运行工况偏离设计工况,必然导致磨煤机各根出粉管的风粉浓度及流速产生较大偏差。低氮燃烧背景要求下,这种偏差直接造成炉膛内存在不完全燃烧或火焰偏斜,局部区域高温腐蚀,过/再热器壁温超温等问题。目前,降低磨煤机风粉管流速偏差的主要方式是开展一次风调整试验,通过手动调节磨煤机出口风粉管可调缩孔开度,增加/减小相应管路阻力。而该方法存在以下不足:工作量大,需要在线反复测量风粉管动压和调整可调缩孔开度;精度低,无法实现风粉管全截面测量,且恶劣煤质条件下测量仪器容易发生堵塞,测试数据可靠性不足;运行工况与试验工况存在较大偏差时,改善效果有限,需要定期测试和维护。Due to the large difference in coal quality and the error in the measurement of the primary air volume at the inlet of the coal mill, the actual operating conditions of the coal mill deviate from the design conditions, which will inevitably lead to large deviations in the air powder concentration and flow rate of each powder outlet pipe of the coal mill . Under the background of low nitrogen combustion, this deviation directly causes problems such as incomplete combustion or flame deflection in the furnace, high temperature corrosion in local areas, and overtemperature of the over/reheater wall temperature. At present, the main way to reduce the flow rate deviation of the coal mill air powder pipe is to carry out a primary air adjustment test, and manually adjust the outlet air powder pipe of the coal mill to adjust the opening of the shrinkage hole to increase/decrease the corresponding pipeline resistance. However, this method has the following shortcomings: the workload is large, and it is necessary to repeatedly measure the dynamic pressure of the air-powder pipe online and adjust the opening of the adjustable shrinkage hole; the accuracy is low, and the full-section measurement of the air-powder pipe cannot be realized, and the measuring instrument is easy to measure under poor coal quality conditions. Blockage occurs, and the reliability of the test data is insufficient; when there is a large deviation between the operating conditions and the test conditions, the improvement effect is limited, and regular testing and maintenance are required.
发明内容SUMMARY OF THE INVENTION
为了克服上述现有技术的不足,本发明的目的在于提供一种非能动自调节的气固两相分配器,以保证磨煤机出口各根风粉管流量实时一致,尽量降低一次风量的同时二次风门开度不需设置同层偏置,配合浓淡分离燃烧器、空气分级燃烧、燃料分级燃烧等低氮燃烧技术,促进煤粉的高效低氮燃烧。In order to overcome the above-mentioned deficiencies of the prior art, the purpose of the present invention is to provide a non-automatic self-adjusting gas-solid two-phase distributor, so as to ensure that the flow of each air-powder pipe at the outlet of the coal mill is consistent in real time, and while reducing the primary air volume as much as possible The opening of the secondary air valve does not need to be offset on the same layer, and it cooperates with low-nitrogen combustion technologies such as concentration separation burners, air staged combustion, and fuel staged combustion to promote high-efficiency and low-nitrogen combustion of pulverized coal.
为了实现上述目的,本发明采用的技术方案是:In order to achieve the above object, the technical scheme adopted in the present invention is:
一种非能动自调节的气固两相分配器,包括分配器本体,所述分配器本体包括在出口风粉管顶部焊接的支撑顶座1,所述支撑顶座1包括内圈与外圈,外圈直径与原磨煤机出口风粉管直径相等,位于内圈下方设置有阻力元件2,所述阻力元件2底端设置限位装置3,位于出口风粉管上设置有导向滑道4,导向滑道4用于使阻力元件2按固定路线发生形变。A non-automatic self-adjusting gas-solid two-phase distributor includes a distributor body, the distributor body includes a
所述阻力元件2顶端与支撑顶座1内圈焊接,自上而下逐级增加直径延伸至出口风粉管壁面。The top end of the
所述阻力元件2为流线型设计、具有一定弹性及刚度。The
所述分配器本体外侧均涂有防磨防静电涂层。The outside of the dispenser body is coated with an anti-wear and anti-static coating.
所述阻力元件2为正宝塔形阻力元件,整个阻力元件呈螺旋扩大的形状。The
所述阻力元件2呈螺旋形,最小的圆环直径等于支撑顶座1内圈外侧直径,且二者相互焊接固定,最大圆环直径等于支撑顶座1外圈内侧的直径。The
所述内圈直径应保证风粉流速大于18m/s。内外圈有四个连接点,沿圆环周长均匀分布。The diameter of the inner ring should ensure that the air flow velocity is greater than 18m/s. The inner and outer rings have four connection points, evenly distributed along the circumference of the ring.
本发明的有益效果:Beneficial effects of the present invention:
本发明在调节风粉流速上,可根绝磨煤机实际运行工况,实时动态调节各个出口风粉管流通阻力,响应速度快,工作量小,设备异动小,且方便更换。In adjusting the air-powder flow rate, the invention can eliminate the actual operating conditions of the coal mill, dynamically adjust the flow resistance of each outlet air-powder pipe in real time, has fast response speed, small workload, small equipment change and convenient replacement.
整个阻力元件采用流线型设计,具有一定的弹性及刚度,以便调节器在不靠外界动力的情况下,由风粉速度自带的冲击力驱动阻力元件的变形,改变流通面积(即流速大,冲击力大,阻力元件变形大,流通面积减小,流通阻力增加),实现自调节。其最小的圆环直径等于支撑顶座内圈外侧直径,且二者相互焊接固定,最大圆环直径等于支撑顶座外圈内侧的直径。阻力元件最外侧底端设有限位装置并与导向滑道连接,保证其按照固定路线发生不超负荷的形变。The entire resistance element adopts a streamlined design with certain elasticity and stiffness, so that the regulator can drive the deformation of the resistance element by the impact force of the wind powder speed without relying on external power, and change the flow area (that is, the flow rate is large, the impact The force is large, the resistance element is deformed greatly, the flow area is reduced, and the flow resistance is increased) to achieve self-adjustment. The smallest ring diameter is equal to the outer diameter of the inner ring of the support top seat, and the two are welded and fixed to each other, and the largest ring diameter is equal to the diameter of the inner side of the outer ring of the support top seat. The outermost bottom end of the resistance element is provided with a limiting device and is connected with the guide slideway to ensure that it deforms according to the fixed route without overloading.
限位装置设置于正宝塔形阻力元件底端,限制阻力元件的形变范围,保证阻力元件在不超负荷的情况下正常工作,提高阻力元件的使用寿命。The limiting device is arranged at the bottom end of the positive pagoda-shaped resistance element, which limits the deformation range of the resistance element, ensures the normal operation of the resistance element without overloading, and improves the service life of the resistance element.
导向滑道可保证其在固定的轨道上发生形变,提高自调节的效率并延长了阻力元件的工作寿命。The guide slide can ensure that it deforms on the fixed track, which improves the efficiency of self-adjustment and prolongs the working life of the resistance element.
防磨防静电涂层覆盖分配器所有装置表面,防止风粉撞击摩擦产生静电引火,导致事故,延长了分配器的使用寿命。The anti-wear and anti-static coating covers all the device surfaces of the dispenser to prevent the electrostatic ignition caused by the collision and friction of wind powder, which may lead to accidents and prolong the service life of the dispenser.
附图说明Description of drawings
图1为支撑顶座示意图。Figure 1 is a schematic diagram of a support top seat.
图2为正宝塔形阻力元件示意图。Figure 2 is a schematic diagram of a positive pagoda-shaped resistance element.
图3为风粉流速较低时的工作原理示意图。Figure 3 is a schematic diagram of the working principle when the air-powder flow rate is low.
图4为风粉流速较高时的工作原理示意图。Figure 4 is a schematic diagram of the working principle when the air-powder flow rate is high.
具体实施方式Detailed ways
下面结合附图对本发明作进一步详细说明。The present invention will be further described in detail below in conjunction with the accompanying drawings.
参看图1,为本发明支撑顶座1示意图,分为内圈和外圈。其中外圈直径等于原磨煤机出口风粉管的直径,内圈直径则由磨煤机运行规程及运行工况确定,即内圈直径所能通过的最低风速应保证不发生煤粉堵管,通常来说磨煤机运行规程要求风粉流速不得低于18m/s,因此内圈直径应保证风粉流速大于18m/s。内外圈有四个连接点,沿圆环周长均匀分布,用于固定内外圈位置和增加支撑顶座1稳定性。整个支撑顶座1焊接固定于风粉替代管顶部,内圈用于固定宝塔型阻力原件。Referring to FIG. 1 , it is a schematic diagram of the supporting
参看图2,为本发明装置中的正宝塔形阻力元件示意图,整个阻力元件2呈螺旋形,其最小的圆环直径等于支撑顶座1内圈外侧直径,且二者相互焊接固定,最大圆环直径等于支撑顶座1外圈内侧的直径。阻力原件2最外侧底端设有限位装置并与导向滑道4连接,保证其按照固定路线发生不超负荷的形变,延长阻力元件寿命。所述阻力元件2为正宝塔形阻力元件,是确保整个分配器实现实时自适应调整的核心元件,整个阻力元件呈螺旋扩大的形状,从设计上满足其对于弹性的需求。分配器工作过程利用一次风速作用和该阻力元件的弹性和刚度,改变风粉管流通的阻力,以达到调节风粉管流量的作用。Referring to Fig. 2, it is a schematic diagram of a positive pagoda-shaped resistance element in the device of the present invention. The
针对单台磨煤机,在每根出口风粉管上都替代安装一种非能动自调节的气固两相分配器,包括出口风粉管,支撑顶座(见图1)、正宝塔形阻力元件(见图2)、防磨防静电涂层、限位装置3、导向滑道4等。For a single coal mill, a non-automatic self-adjusting gas-solid two-phase distributor is installed on each outlet air powder pipe instead, including the outlet air powder pipe, the supporting top seat (see Figure 1), the positive tower shape Resistance element (see Figure 2), anti-wear and anti-static coating,
在所述出口风粉管顶部焊接支撑顶座1,所述支撑顶座1的外圈直径与原磨煤机出口风粉管直径相等,所述支撑顶座1的内圈直径根据磨煤机运行规程及运行工况确定,所述正宝塔形阻力元件2的顶端与支撑顶座1内圈焊接,自上而下逐级增加直径延伸至出口风粉管壁面,所述正宝塔形阻力元件2为流线型设计、具有一定弹性及刚度、且视空间条件和工况载荷进行线性或非线性阻力分配,所述正宝塔形阻力元件2底端设置限位装置3,防止阻力元件超载荷运行,提高阻力元件寿命;所述导向滑道4使正宝塔形阻力元件2按固定路线发生形变;所述非能动自调节的气固两相分配器所有装置均涂有防磨防静电涂层。Weld a
当同台磨煤机某根风粉管流速偏大时,风粉管内风粉流动产生的动量使正宝塔形阻力元件产生形变,沿流动方向向上挤压,使得该根风粉管内流通面积减小,流通阻力增大,风粉流速降低,相应地其他根风粉管流速升高,使得该台磨煤机在不借助外在动力的条件下出口各根风粉管流量实时自动调节(见图3)。When the flow velocity of a certain air-powder pipe of the same coal mill is too large, the momentum generated by the air-powder flow in the air-powder pipe causes the positive pagoda-shaped resistance element to deform and squeeze upward along the flow direction, so that the flow area in the air-powder pipe decreases. Small, the flow resistance increases, the flow rate of air powder decreases, and the flow rate of other air powder pipes increases accordingly, so that the flow rate of each air powder pipe at the outlet of the coal mill is automatically adjusted in real time without external power (see image 3).
本发明的工作原理:The working principle of the present invention:
在没有加装非能动自调节的气固两相分配器的风粉管,受物理空间影响,即各输送管道的长度、弯头和送风阻力不同,且磨煤机自身也存在风粉分配不均的问题,就导致每根风粉管的风粉流速不一致,就会导致火焰偏斜,部分区域缺氧或过氧燃烧。在加装了非能动自调节气固两相分配器(各部件均涂有防磨防静电涂层)之后,由风粉速度自带的冲击力驱动正宝塔阻力元件变形,改变流通面积(即流速大,冲击力大,则阻力元件2变形大,导致流通面积减小,流通阻力增加,风粉速度降低),实现自调节。In the air-powder pipe without the non-automatic self-adjusting gas-solid two-phase distributor, it is affected by the physical space, that is, the length, elbow and air supply resistance of each conveying pipe are different, and the coal mill itself also has air-powder distribution. The problem of unevenness will cause the air powder flow rate of each air powder pipe to be inconsistent, which will lead to flame deflection, oxygen deficiency or peroxy combustion in some areas. After installing a non-automatic self-adjusting gas-solid two-phase distributor (each part is coated with anti-wear and anti-static coating), the impact force of the wind powder speed drives the deformation of the resistance element of the pagoda, changing the flow area (ie The larger the flow rate and the larger the impact force, the larger the deformation of the
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Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63271019A (en) * | 1987-04-27 | 1988-11-08 | Hitachi Ltd | Method and device for uniformly distributing coal pulverized in mill to a plurality of burners |
CN2587513Y (en) * | 2002-11-06 | 2003-11-26 | 华东电力试验研究院 | Centrifuga adjustable coal dust distributor |
CN1548347A (en) * | 2000-03-15 | 2004-11-24 | ʥ-��������깫˾ | fluid dispenser |
CN1764498A (en) * | 2003-01-22 | 2006-04-26 | 瓦斯特能量系统有限公司 | Reactor |
CN101749724A (en) * | 2008-12-20 | 2010-06-23 | 安徽源钧生物科技有限公司 | Biomass fuel air device |
CN105485709A (en) * | 2016-01-05 | 2016-04-13 | 上海发电设备成套设计研究院 | Adjustable coal dust distributor |
CN106765275A (en) * | 2017-03-14 | 2017-05-31 | 江苏中能电力设备有限公司 | A kind of adjustable type differential pulverized coal distributor |
CN108204601A (en) * | 2017-12-21 | 2018-06-26 | 北京博奇电力科技有限公司 | Two-stage adjusts gas-particle two-phase fluidic distributor |
-
2019
- 2019-11-11 CN CN201911092410.2A patent/CN110813514B/en not_active Expired - Fee Related
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63271019A (en) * | 1987-04-27 | 1988-11-08 | Hitachi Ltd | Method and device for uniformly distributing coal pulverized in mill to a plurality of burners |
CN1548347A (en) * | 2000-03-15 | 2004-11-24 | ʥ-��������깫˾ | fluid dispenser |
CN2587513Y (en) * | 2002-11-06 | 2003-11-26 | 华东电力试验研究院 | Centrifuga adjustable coal dust distributor |
CN1764498A (en) * | 2003-01-22 | 2006-04-26 | 瓦斯特能量系统有限公司 | Reactor |
CN101749724A (en) * | 2008-12-20 | 2010-06-23 | 安徽源钧生物科技有限公司 | Biomass fuel air device |
CN105485709A (en) * | 2016-01-05 | 2016-04-13 | 上海发电设备成套设计研究院 | Adjustable coal dust distributor |
CN106765275A (en) * | 2017-03-14 | 2017-05-31 | 江苏中能电力设备有限公司 | A kind of adjustable type differential pulverized coal distributor |
CN108204601A (en) * | 2017-12-21 | 2018-06-26 | 北京博奇电力科技有限公司 | Two-stage adjusts gas-particle two-phase fluidic distributor |
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