CN204563780U - Barb demister optimized by a kind of streamlined two passage bands - Google Patents

Barb demister optimized by a kind of streamlined two passage bands Download PDF

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Publication number
CN204563780U
CN204563780U CN201520171555.2U CN201520171555U CN204563780U CN 204563780 U CN204563780 U CN 204563780U CN 201520171555 U CN201520171555 U CN 201520171555U CN 204563780 U CN204563780 U CN 204563780U
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demister
barb
streamlined
optimized
blade
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Expired - Fee Related
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CN201520171555.2U
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Chinese (zh)
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张翼
王通
卢权
彰金宝
吕玉坤
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Sanhe Power Generation Co Ltd
North China Electric Power University Baoding
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Sanhe Power Generation Co Ltd
North China Electric Power University Baoding
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Abstract

Barb demister optimized by the streamlined two passage bands of one that the utility model discloses the demister scope belonging to wet method fume desulfurizing system.It is made up of multiple demister blade assembly, demister blade assembly is made up of the adjacent demister blade be fixedly connected with by jig between two again, every two demister blades form fluid passage, demister barb is placed in and demister import department, demister barb is made up of straightway and arc, and arc and straightway are tangential on 1/4 circular arc.The utility model structure is simple, be easy to realize, in-site installation is convenient, while guarantee demisting efficiency pressure drop minimum.

Description

一种流线型两通道带优化倒钩除雾器A streamlined two-channel demister with optimized barbs

技术领域technical field

本实用新型属于湿法烟气脱硫系统的除雾装置范围,特别涉及一种流线型两通道带优化倒钩除雾器。The utility model belongs to the scope of a demister of a wet flue gas desulfurization system, in particular to a streamlined two-channel demister with optimized barbs.

背景技术Background technique

湿法脱硫工艺中,经吸收塔处理的烟气夹带了大量的浆体液滴,且烟气流速越高,其携带的液滴量越多。如果不除去这些液滴,它不但会因沉积在吸收塔下游设备表面形成石膏垢而加速设备的腐蚀,还会影响烟气加热器的换热效率。如果采用烟气湿排法,则会造成因烟囱“降雨”(排放液体、固体或浆体)而污染电厂周围环境。除雾器是燃煤或燃油锅炉烟气脱硫系统中的关键设备,其性能直接影响到湿法烟气脱硫系统(WFGD)能否连续可靠运行。WFGD的工作原理是:当含有雾沫的气体以一定速度流经除雾器时,由于惯性作用,雾沫与除雾器叶片相碰撞而附着在除雾器叶片表面上;除雾器叶片表面附近雾沫的扩散和重力沉降使雾沫形成较大的液滴并随气流向上运动至除雾器叶片转弯处,由于转向离心力及其与除雾器叶片的摩擦和吸附作用以及液体的表面张力使得液滴越来越大,直至积聚的液滴大到其自身产生的重力超过烟气的浮力与液体表面张力的合力时,液滴就从除雾器叶片表面上被分离下来。除雾器叶片的多折向结构增加了雾沫被捕集的机会,未被除去的雾沫在下一个转弯处经过相同的作用而被捕集,这样反复作用,从而除去烟气中所携带的液滴。In the wet desulfurization process, the flue gas treated by the absorption tower entrains a large number of slurry droplets, and the higher the flue gas flow rate, the more droplets it carries. If these droplets are not removed, it will not only accelerate the corrosion of the equipment due to the formation of gypsum scale deposited on the surface of the equipment downstream of the absorption tower, but also affect the heat exchange efficiency of the flue gas heater. If the flue gas wet discharge method is used, it will cause pollution of the surrounding environment of the power plant due to "rainfall" (discharge of liquid, solid or slurry) in the chimney. The mist eliminator is the key equipment in the flue gas desulfurization system of coal-fired or oil-fired boilers, and its performance directly affects whether the wet flue gas desulfurization system (WFGD) can operate continuously and reliably. The working principle of WFGD is: when the gas containing mist flows through the demister at a certain speed, due to inertia, the mist collides with the demister blade and adheres to the surface of the demister blade; The diffusion and gravity settlement of the nearby mist make the mist form larger droplets and move upward with the airflow to the corner of the demister blade. The droplets become larger and larger until the accumulated droplets are so large that the gravity generated by themselves exceeds the resultant force of the buoyancy of the smoke and the surface tension of the liquid, and the droplets are separated from the surface of the demister blades. The multi-folding structure of the mist eliminator blades increases the chance of the mist being captured, and the unremoved mist is captured through the same action at the next turning, so that the action is repeated, thereby removing the mist carried in the flue gas. droplet.

衡量除雾器性能的两个重要指标是除雾器进出口压降和除雾效率。除雾器进出口压降越大表明系统需要补充的动力越大,能耗就越高,一般两级除雾器压降应控制在120-200Pa以内。除雾效率越低烟气含水量就越高,液滴沉积在吸收塔下游设备表面的量则会越大,给设备安全运行带来的隐患也会越大。因此,干态下烟气出口端含水量应控制在75mg/Nm3以内。Two important indicators to measure the performance of the mist eliminator are the pressure drop at the inlet and outlet of the mist eliminator and the mist removal efficiency. The greater the pressure drop at the inlet and outlet of the demister, the greater the power that the system needs to supplement, and the higher the energy consumption. Generally, the pressure drop of the two-stage demister should be controlled within 120-200Pa. The lower the demisting efficiency, the higher the water content of the flue gas, the greater the amount of droplets deposited on the surface of the equipment downstream of the absorption tower, and the greater the hidden danger to the safe operation of the equipment. Therefore, the moisture content at the outlet end of the flue gas should be controlled within 75mg/Nm 3 in a dry state.

传统的流线型两通道带钩叶片临界流速较高、易清洗,目前在大型脱硫设备中被广泛应用,但是大都存在除雾效率低或压降较大的问题。The traditional streamlined two-channel hooked blade has a high critical flow rate and is easy to clean. It is widely used in large-scale desulfurization equipment at present, but most of them have the problems of low demisting efficiency or large pressure drop.

实用新型内容Utility model content

本实用新型的目的是针对现有技术中传统的流线型两通道带钩叶片临界流速较高、易清洗,且目前在大型脱硫设备中被广泛应用,但大都存在除雾效率低或压降较大的问题,而提供一种流线型两通道带优化倒钩除雾器,其特征在于,倒钩除雾器由多个除雾器叶片组件组成,除雾器叶片组件又由两两相邻通过卡具固定连接的除雾器叶片组成,每两个除雾器叶片构成流体通道,除雾器的倒钩置于流体通道内。The purpose of this utility model is to aim at the traditional streamlined two-channel hook blades in the prior art with high critical flow velocity and easy cleaning, and are widely used in large-scale desulfurization equipment at present, but most of them have low demisting efficiency or large pressure drop To solve the problem, a streamlined two-channel demister with optimized barbs is provided. It consists of fixedly connected mist eliminator blades, every two mist eliminator blades form a fluid passage, and the barbs of the mist eliminator are placed in the fluid passage.

所述置于流体通道内的除雾器倒钩与除雾器进口垂直高度为69.5mm处,倒钩与竖直方向的夹角为36°;除雾器倒钩由直线段和弧线段组成,其直线段长6.5mm,弧线段是半径为6.5mm且与直线段相切的1/4圆弧。The vertical height between the barb of the demister placed in the fluid channel and the inlet of the demister is 69.5mm, and the angle between the barb and the vertical direction is 36°; the barb of the demister is composed of a straight line segment and an arc segment Composition, the length of the straight line is 6.5mm, and the arc is a 1/4 arc with a radius of 6.5mm and tangent to the straight line.

所述倒钩置于除雾器叶片构成的流体通道中,倒钩是顺应叶片构成的流体通道中的流线方向,因而控制了系统产生的压降。The barb is placed in the fluid channel formed by the blades of the mist eliminator, and the barb follows the direction of the flow line in the fluid channel formed by the blades, thus controlling the pressure drop generated by the system.

本实用新型的有益效果是结构简单、易于实现、现场安装方便、在保证除雾效率的同时压降最低;为了克服目前湿法脱硫除雾器除雾效率低、压降高的问题,达到既保证湿法烟气脱硫系统的正常运行,又节省能源的双重目的。The utility model has the beneficial effects of simple structure, easy realization, convenient on-site installation, and the lowest pressure drop while ensuring the demisting efficiency; The dual purpose of ensuring the normal operation of the wet flue gas desulfurization system and saving energy.

附图说明Description of drawings

图1是湿法脱硫塔内FLAT MEV25/40型除雾器系统整体示意图。Figure 1 is the overall schematic diagram of the FLAT MEV25/40 demister system in the wet desulfurization tower.

图2是倒钩优化的除雾器叶片组示意图。Figure 2 is a schematic diagram of a barb-optimized demister blade set.

图1中,1.除雾器叶片组件;2.除雾器叶片支撑结构;3.除雾器支撑梁;4.冲洗管路;5.冲洗管路支撑系统;图2中,6.除雾器叶片;7.除雾器倒钩。In Fig. 1, 1. Demister blade assembly; 2. Demister blade support structure; 3. Demister support beam; 4. Flush pipeline; 5. Flush pipeline support system; Fig. 2, 6. Demister 7. Demister barbs.

具体实施方式Detailed ways

本实用新型提供一种流线型两通道带优化倒钩除雾器,下面结合附图对本实用新型做进一步的说明。The utility model provides a streamlined two-channel demister with optimized barbs. The utility model will be further described below in conjunction with the accompanying drawings.

图1中,除雾器系统由除雾器叶片组件1、除雾器叶片支撑结构2、除雾器支撑梁3、冲洗管路4和冲洗管路支撑系统5组成,其基本结构与FLAT MEV25/40型除雾器一致,除雾器叶片组件1是由多个除雾器叶片6通过卡具两两拼接而成,每两个除雾器叶片6构成流体通道(如图2所示)。所述的除雾器叶片6由流线型叶片和除雾器倒钩7组成,除雾器倒钩7置于与除雾器进口垂直高度为69.5mm处,倒钩与竖直方向的夹角为36°。除雾器倒钩7由直线段和弧线段组成,其直线段长6.5mm,弧线段是半径为6.5mm且与直线段相切的1/4圆弧。In Fig. 1, the mist eliminator system consists of the mist eliminator blade assembly 1, the mist eliminator blade support structure 2, the mist eliminator support beam 3, the flushing pipeline 4 and the flushing pipeline support system 5, and its basic structure is the same as that of the FLAT MEV25 /40 type mist eliminator, the mist eliminator blade assembly 1 is made up of a plurality of mist eliminator blades 6 spliced in pairs by clamps, and every two mist eliminator blades 6 form a fluid channel (as shown in Figure 2) . The demister blade 6 is composed of a streamlined blade and a demister barb 7. The demister barb 7 is placed at a vertical height of 69.5 mm from the inlet of the demister, and the angle between the barb and the vertical direction is 36°. The demister barb 7 is composed of a straight line segment and an arc line segment, the length of the straight line segment is 6.5 mm, and the arc line segment is a 1/4 circular arc with a radius of 6.5 mm and tangent to the straight line segment.

通过数值模拟试验可以验证,经过改进优化后的除雾器叶片6对液滴有很好的捕集效果。当带有液滴的气流经过除雾器流体通道时,由于倒钩是顺应叶片流体通道中的流线,因而控制了系统产生的压降。倒钩置于除雾器叶片6构成的流体通道中,使得流体通道变窄,增加了液滴与除雾器叶片6碰撞的几率,从而增大了液滴被捕集的几率,起到了提高除雾效率的作用。Numerical simulation tests can be used to verify that the improved and optimized demister blade 6 has a good trapping effect on droplets. Since the barbs follow the streamlines in the vane fluid passages, the pressure drop generated by the system is controlled when the airflow with liquid droplets passes through the demister fluid passages. The barb is placed in the fluid channel formed by the demister blade 6, which narrows the fluid channel and increases the probability of the droplet colliding with the demister blade 6, thereby increasing the probability of the droplet being trapped and improving The effect of defogging efficiency.

Claims (3)

1. barb demister optimized by streamlined two passage bands, it is characterized in that, barb demister is made up of multiple demister blade assembly, demister blade assembly is made up of the adjacent demister blade be fixedly connected with by jig between two again, every two demister blades form fluid passage, and the barb of demister is placed in fluid passage.
2. barb demisters optimized by a kind of streamlined two passage bands according to claim 1, it is characterized in that, described in be placed in demister barb in fluid passage and demister import vertical height is 69.5mm place, the angle of barb and vertical direction is 36 °; Demister barb is made up of straightway and arc, its straight line segment length 6.5mm, and arc is that radius is 6.5mm and 1/4 circular arc tangent with straightway.
3. barb demister optimized by a kind of streamlined two passage bands according to claim 1, it is characterized in that, described barb is placed in the fluid passage that demister blade is formed, and the grain direction in the fluid passage of blade formation complied with by barb, thus controls the pressure drop that system produces.
CN201520171555.2U 2015-03-25 2015-03-25 Barb demister optimized by a kind of streamlined two passage bands Expired - Fee Related CN204563780U (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104740935A (en) * 2015-03-25 2015-07-01 三河发电有限责任公司 Streamline-type two-passage demister with optimized barb
CN107281819A (en) * 2017-07-03 2017-10-24 合肥天翔环境工程有限公司 A kind of High efficiency baffle plate formula demister

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104740935A (en) * 2015-03-25 2015-07-01 三河发电有限责任公司 Streamline-type two-passage demister with optimized barb
CN107281819A (en) * 2017-07-03 2017-10-24 合肥天翔环境工程有限公司 A kind of High efficiency baffle plate formula demister

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Granted publication date: 20150819

Termination date: 20160325