WO2017185564A1 - 自适应沸腾式泡沫脱硫除尘装置 - Google Patents

自适应沸腾式泡沫脱硫除尘装置 Download PDF

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WO2017185564A1
WO2017185564A1 PCT/CN2016/095407 CN2016095407W WO2017185564A1 WO 2017185564 A1 WO2017185564 A1 WO 2017185564A1 CN 2016095407 W CN2016095407 W CN 2016095407W WO 2017185564 A1 WO2017185564 A1 WO 2017185564A1
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desulfurization
adaptive
mass transfer
hole
type foam
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PCT/CN2016/095407
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English (en)
French (fr)
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吴其荣
喻江涛
范振兴
李紫龙
王进
王琴
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中电投远达环保工程有限公司重庆科技分公司
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Publication of WO2017185564A1 publication Critical patent/WO2017185564A1/zh

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/04—Separating dispersed particles from gases, air or vapours by liquid as separating agent by passing the gas or air or vapour through foam
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/46—Removing components of defined structure
    • B01D53/48—Sulfur compounds
    • B01D53/50—Sulfur oxides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/80—Semi-solid phase processes, i.e. by using slurries

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  • the invention relates to the field of flue gas purification, in particular to an adaptive boiling type foam desulfurization and dust removal device.
  • the existing desulfurization and dust removal equipment mainly has the following types:
  • Chinese Patent No. 200710093042.4 discloses a two-phase rectification flue gas desulfurization process which utilizes the non-uniformity of the flow field in the spray tower, and the design of the rectifying plate and the spray layer is not intentionally directed to the liquid phase and The gas phase is uniformly rectified, the resistance of the flue gas is relatively small, the flow velocity of the flue gas is not reduced, and the gas phase and the liquid phase are relatively uneven, so that the liquid phase and the gas phase are always maintained in a turbulent state for countercurrent reaction, and optimized.
  • the flow field reduces the pressure drop of the system, achieves the purpose of energy saving and reducing equipment cost and maintenance cost;
  • Chinese Patent No. 201110447122.1 discloses a desulfurization absorption tower with a bias flow type two-phase rectification device, which is provided with a bias flow two-phase rectification device between the spray layer and the flue gas inlet, the bidirectional flow biphasic
  • the rectifying device comprises a horizontally arranged rectifying plate, the rectifying plate flows perpendicularly to the flue gas inlet to the divided area, the rectifying plate of each area is provided with a mesh hole and the mesh hole density near the flue gas inlet area is larger than the sieve far away from the flue gas inlet area
  • the density of the pores according to the uneven distribution of the flue gas when the flue gas enters the desulfurization absorption tower, the sieve density of the region where the flue gas concentration is low and the flow velocity is low is larger than the sieve density of the region where the flue gas concentration is high and the flow velocity is high, so the rectification plate
  • the flue gas resistance of each area is different, and the flue gas
  • Chinese Patent No. 201520212632.4 discloses a coal-fired power plant flue gas multi-pollutant deep purification control coupling system, including economizer system, double-mixed rectification and efficiency-enhancing SCR flue gas denitration system, high-efficiency electrostatic precipitator system, and wet
  • the method is divided into a desulfurization system, a two-phase rectification phase transformation coagulation system and a wet electrostatic depth control system.
  • the above systems are sequentially connected, and the double-mix rectification and efficiency-enhancing SCR flue gas denitration system includes an ammonia injection device, a denitration catalyst and a rectification regulating device, and a wet method.
  • the zone-efficiency desulfurization system adopts a tower partition system or a two-column double-loop coupling system, and the two-phase rectifier phase-change condensation system is installed at the inlet of the wet electrostatic depth control system.
  • the prior art is a rectification system based on the design of a conventional perforated plate structure, and the mass transfer effect of the flue gas and the slurry is improved by providing a perforated plate structure.
  • the pore diameters of the holes on the conventional perforated plate are the same, It is a straight hole, which can not effectively achieve the efficient removal of dust, and has poor adaptability to the flow field, low mass transfer efficiency, no load adjustment function, and reduced removal effect.
  • the object of the present invention is to provide an adaptive boiling type foam desulfurization and dust removal device, which can not only improve the uniformity of the flue gas, but also enhance the gas-liquid mass transfer efficiency, and has high adaptability to the slurry circulation amount and the unit load. Improve the deep removal effect of sulfur dioxide and dust.
  • the adaptive boiling type foam desulfurization and dust removal device of the present invention comprises a mass transfer member for mass transfer of a fluid in a desulfurization absorption tower, wherein the mass transfer member is a plate-like structure, and the mass transfer member comprises at least three longitudinally side by side
  • the partitions are arranged, and each of the partitions is provided with at least two sets of holes for fluid passage along the longitudinal direction, each set of holes being composed of two holes of different apertures, and two holes of different apertures in each set of holes are arranged at a lateral interval.
  • the cross section of the hole is trapezoidal.
  • the cross section of the hole is an isosceles trapezoid, and the diameter of the upper hole is larger than the diameter of the lower hole, and the angle ⁇ between the hole wall and the end surface of the lower hole is 90-165°.
  • the porosity of the pores distributed on each of the zones is unequal porosity.
  • the diameters of the upper and lower holes of the hole are determined by the porosity, ie Where K is the porosity, d 1 is the upper pore diameter, d 2 is the lower pore diameter, ⁇ is a constant, ⁇ is in the range of 0.8 to 1.0, and L is between the upper pore edges of two adjacent pores. spacing.
  • the holes on the respective partitions are arranged in a polygonal shape.
  • each of the partitions is a separate plate body, and the mass transfer members are composed of splicing of the plates.
  • the thickness of the plate body is 3 to 20 mm.
  • the mass transfer member is disposed in the desulfurization absorption tower between the flue gas inlet of the desulfurization absorption tower and the slurry spray layer disposed in the desulfurization absorption tower.
  • the distance between the mass transfer member and the flue gas inlet of the desulfurization absorption tower is 500 to 2000 mm.
  • the slurry of the slurry spray layer is sprayed onto the mass transfer member to form a boiling foam layer for load regulation of the fluid, the boiling foam layer having a height of 100 to 500 mm.
  • the adaptive boiling type foam desulfurization and dust removing device of the present invention by providing a mass transfer member of a plate-like structure, the mass transfer member includes at least three partitions arranged side by side in the longitudinal direction, each of which is arranged side by side in the longitudinal direction There are at least two sets of holes for the passage of fluids, each set consisting of two holes of different pore sizes, in which holes of two different pore sizes are arranged laterally, and the cross section of the holes is trapezoidal, so that it can not only Improve the uniformity of flue gas, enhance the gas-liquid mass transfer efficiency, and at the same time have higher adaptability to the slurry circulation volume and unit load, and improve the deep removal effect of sulfur dioxide and dust.
  • Figure 1 is a schematic view of the structure of the present invention
  • Figure 2 is a schematic structural view of a mass transfer member of the present invention
  • Figure 3 is a cross-sectional view taken along line A-A of Figure 2;
  • Figure 4 is a schematic view showing the state of use of the present invention.
  • FIG. 1 is a schematic structural view of the present invention
  • FIG. 2 is a schematic structural view of a mass transfer member of the present invention
  • FIG. 3 is a cross-sectional view taken along line AA of FIG. 2
  • FIG. 4 is a schematic view showing the state of use of the present invention, and the direction indicated by the arrow is a fluid flow direction.
  • the adaptive boiling type foam desulfurization and dust removal device of the embodiment includes the fluid used in the desulfurization absorption tower 4 a mass transfer mass transfer member 1, the mass transfer member 1 being a plate-like structure, the mass transfer member comprising at least three partitions (first partition 21, second partition 22, third partition 23) arranged side by side in the longitudinal direction, At least two sets of holes for fluid passage are arranged side by side in each longitudinal direction, and each set of holes is composed of two holes of different diameters (hole I31, hole II32), and two holes of different diameters in each set of holes (holes) I31, the hole II32) is disposed at a lateral interval, and the mass transfer member 1 of the embodiment is provided with six partitions (a first partition 21, a second partition 22, a third partition 23, a fourth partition 24, and a fifth partition 25, The sixth partition 26), each partition is provided with two sets of holes, and the holes of the two
  • the hole (hole I31 or hole II32) has a trapezoidal cross section, so that the slurry can flow down the hole wall of the hole, and the trapezoid is adopted through the hole.
  • the structure can buffer and load the fluid, which not only improves the uniformity of the flue gas, but also enhances the gas-liquid mass transfer efficiency. At the same time, it has high adaptability to the slurry circulation volume and unit load, and greatly improves the depth of sulfur dioxide and dust. Remove the effect.
  • the cross section of the hole (the hole I31 or the hole II32) is an isosceles trapezoid, and the diameter of the upper hole (the upper hole 31a of the hole I or the upper hole of the hole II) is larger than that of the lower hole (the lower hole I)
  • the diameter of the hole 31b or the lower hole of the hole II enables the flow rate of the fluid to be controlled, and the load is adjusted.
  • the angle ⁇ between the hole wall and the end face of the lower hole is 90 to 165°, so that the slurry can be along the hole.
  • the wall flows downward and buffers the slurry, which is more conducive to enhancing the gas-liquid mass transfer efficiency, ensuring better integration of the flue gas and the slurry, and further improving the load regulation capability and improving the adaptability.
  • the porosity of the holes distributed in each partition is unequal porosity, so as to improve the adaptability to the flow field and further enhance the adaptability.
  • the upper hole of the hole (the hole I31 or the hole II32) (the upper hole 31a of the hole I or the upper hole of the hole II) and the lower hole (the lower hole 31b of the hole I or the lower hole of the hole II)
  • the diameter is determined by the porosity, ie Where K is the porosity, d 1 is the upper pore diameter, d 2 is the lower pore diameter, ⁇ is a constant, ⁇ is in the range of 0.8 to 1.0, and L is between the upper pore edges of two adjacent pores.
  • the spacing is such that the arrangement and distribution of the holes are more reasonable, the load adjustment capability is further improved, the mass transfer efficiency is high, the self-adaptive ability is good, and the removal effect is improved.
  • the holes on the respective partitions are arranged in a polygonal shape, and the holes on the respective partitions of the embodiment may be arranged in a triangle or a square or a rectangle or a parallelogram or other polygonal manner to improve the adaptive capability.
  • each of the partitions is a separate plate body, and the mass transfer member 1 is composed of splicing of the plates, which is convenient for processing and manufacturing; of course, each partition can also be disposed on one plate.
  • the thickness of the plate body is 3-20 mm to ensure the strength of the plate body and to facilitate manufacturing.
  • the mass transfer member 1 is disposed in the desulfurization absorption tower 4, between the flue gas inlet 5 of the desulfurization absorption tower 4 and the slurry spray layer 6 disposed in the desulfurization absorption tower 4, and the slurry spray layer 6
  • the slurry is sprayed downward, the slurry flows from top to bottom, and the flue gas entering the flue gas inlet 5 flows upward, and the slurry and the flue gas flow pass through the holes in the mass transfer member 1 for mass transfer.
  • the distance between the mass transfer member 1 and the flue gas inlet 5 of the desulfurization absorption tower 4 is 500 to 2000 mm, so that the flue gas can flow completely through the mass transfer member to maximize the mass transfer efficiency. ,Economical and practical.
  • the slurry 7 of the slurry spray layer 6 is sprayed on the mass transfer member 1 to form a boiling foam layer 8 for load regulation of the fluid.
  • the height of the boiling foam layer 8 is 100 ⁇ . 500mm, part of the foam passing through the boiling foam layer 8 falls into the hole of the mass transfer member 1, so that the slurry can flow down the hole wall of the hole, further adjusting the load of the slurry 7 and the flue gas to improve the mass transfer efficiency.

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Abstract

一种自适应沸腾式泡沫脱硫除尘装置，包括用于对脱硫吸收塔（4）内流体进行传质的传质构件（1），所述传质构件（1）为板状结构，该传质构件（1）包括至少三个沿纵向并排设置的分区（第一分区21、第二分区22、第三分区23），每个分区（第一分区21、第二分区22、第三分区23）上沿纵向并排设有至少两组用于流体通过的孔（孔Ⅰ31、孔Ⅱ32），每组孔（孔Ⅰ31、孔Ⅱ32）由两种不同孔径的孔（孔Ⅰ31、孔Ⅱ32）组成，每组孔（孔Ⅰ31、孔Ⅱ32）中两种不同孔径的孔（孔Ⅰ31、孔Ⅱ32）沿横向间隔设置，孔（孔Ⅰ31、孔Ⅱ32）的横截面为梯形。

Description

自适应沸腾式泡沫脱硫除尘装置 技术领域
本发明涉及烟气净化领域，特别涉及一种自适应沸腾式泡沫脱硫除尘装置。
背景技术
随着国家针对燃煤超低排放政策的提出，传统的脱硫和除尘技术已很难满足超低排放要求下的严格排放指标，通过对现有装置的优化和改进，提升现有装置的脱硫和协同除尘效率成为目前最为有效和经济的一种方式。现有的脱硫除尘设备主要有以下几种：
1.专利号为200710093042.4的中国专利公开了一种双相整流烟气脱硫工艺，其利用了喷淋塔内流场的不均匀性，整流板和喷淋层的设计不会刻意对液相及气相进行均匀的整流，烟气的阻力相对变小，不会造成烟气的流速降低，气相和液相相对不均匀，使得液相和气相始终保持在紊流的状态下进行逆流反应，优化了流场，使系统压降降低，达到节能降耗和降低装置成本和维修成本的目的；
2.专利号为201110447122.1的中国专利公开了一种带偏流式双相整流装置的脱硫吸收塔，通过在喷淋层与烟气入口之间设有偏流式双相整流装置，该偏流式双相整流装置包括水平设置的整流板，整流板垂直于烟气入口流向划分区域，每个区域的整流板上均开有筛孔并且靠近烟气入口区域的筛孔密度大于远离烟气入口区域的筛孔密度，根据烟气进入脱硫吸收塔时烟气分布的不均匀性，烟气浓度低、流速低的区域的筛孔密度大于烟气浓度高、流速高的区域的筛孔密度，因此整流板各个区域的烟气阻力不同，烟气通过整流板时被整流均布，从而使烟气分布均匀，以提高脱硫效率；
3.专利号为201520212632.4的中国专利公开了一种燃煤电厂烟气多污染物深度净化控制耦合系统，包括省煤器系统、双混整流提效SCR烟气脱硝系统、高效静电除尘系统、湿法分区提效脱硫系统、双相整流相变凝聚系统和湿式静电深度控制系统，以上系统依次连接，双混整流提效SCR烟气脱硝系统包括喷氨装置、脱硝催化剂和整流调节装置，湿法分区提效脱硫系统采用一塔分区系统或两塔双回路耦合系统，双相整流相变凝聚系统设置在湿式静电深度控制系统入口处。
可见，现有技术均是基于传统多孔板结构设计的整流系统，通过设置多孔板结构来提高烟气和浆液的传质效果，然而，由于传统的多孔板上各孔的孔径均相同，且均为直孔，使其不能有效实现粉尘的高效脱除，且对流场自适应性差，传质效率低，不具备负荷调节功能，降低了脱除效果。
因此，急需开发一种不仅能够提高烟气的均匀性，加强气液传质效率，同时对浆液循环量和机组负荷具有较高适应性，提高对二氧化硫和粉尘的深度脱除效果的自适应沸腾式泡沫脱硫除尘装置。
发明内容
有鉴于此，本发明的目的在于提供一种自适应沸腾式泡沫脱硫除尘装置，不仅能够提高烟气的均匀性，加强气液传质效率，同时对浆液循环量和机组负荷具有较高适应性，提高对二氧化硫和粉尘的深度脱除效果。
本发明的自适应沸腾式泡沫脱硫除尘装置，包括用于对脱硫吸收塔内流体进行传质的传质构件，所述传质构件为板状结构，该传质构件包括至少三个沿纵向并排设置的分区，每个分区上沿纵向并排设有至少两组用于流体通过的孔，每组孔由两种不同孔径的孔组成，每组孔中两种不同孔径的孔沿横向间隔设置，所述孔的横截面为梯形。
进一步，所述孔的横截面为等腰梯形，其上孔的直径大于下孔的直径，孔壁与下孔端面之间的夹角α为90～165°。
进一步，各分区上分布的孔的孔隙率为不均等孔隙率。
进一步，所述孔的上孔和下孔的直径通过孔隙率确定，即
Figure PCTCN2016095407-appb-000001
式中，K为孔隙率，d1为上孔直径，d2为下孔直径，ε为常数，ε的取值范围为0.8～1.0，L为相邻两个孔的上孔边缘之间的间距。
进一步，各个分区上的孔呈多边形布置。
进一步，各个分区分别为单独的板体，传质构件由各板体拼接组成。
进一步，所述板体的厚度为3～20mm。
进一步，所述传质构件设置在脱硫吸收塔内，位于脱硫吸收塔的烟气入口与脱硫吸收塔内设置的浆液喷淋层之间。
进一步，所述传质构件与脱硫吸收塔的烟气入口之间的距离为500～2000mm。
进一步，使用时，浆液喷淋层的浆液喷淋在传质构件上形成用于对流体进行负荷调节的沸腾式泡沫层，该沸腾式泡沫层的高度为100～500mm。
本发明的有益效果：本发明的自适应沸腾式泡沫脱硫除尘装置，通过设置板状结构的传质构件，传质构件包括至少三个沿纵向并排设置的分区，每个分区上沿纵向并排设有至少两组用于流体通过的孔，每组孔由两种不同孔径的孔组成，每组孔中两种不同孔径的孔沿横向间隔设置，且孔的横截面为梯形，使其不仅能够提高烟气的均匀性，加强气液传质效率，同时对浆液循环量和机组负荷具有较高适应性，提高对二氧化硫和粉尘的深度脱除效果。
附图说明
下面结合附图和实施例对本发明作进一步描述：
图1为本发明的结构示意图；
图2为本发明传质构件的结构简图；
图3为图2的A-A向剖视图；
图4为本发明使用状态示意图。
具体实施方式
图1为本发明的结构示意图，图2为本发明传质构件的结构简图，图3为图2的A-A向剖视图，图4为本发明使用状态示意图，图中箭头所示方向为流体流向，其中烟气的流向为自下而上，浆液的流向为自上而下，如图所示：本实施例的自适应沸腾式泡沫脱硫除尘装置，包括用于对脱硫吸收塔4内流体进行传质的传质构件1，所述传质构件1为板状结构，该传质构件包括至少三个沿纵向并排设置的分区(第一分区21、第二分区22、第三分区23)，每个分区上沿纵向并排设有至少两组用于流体通过的孔，每组孔由两种不同孔径的孔(孔I31、孔II32)组成，每组孔中两种不同孔径的孔(孔I31、孔II32)沿横向间隔设置，本实施例的传质构件1上设置有六个分区(第一分区21、第二分区22、第三分区23、第四分区24、第五分区25、第六分区26)，每个分区上设有两组孔，每组孔中两种孔的孔径以及各孔的孔隙率根据烟气的流场分布状况确定，所述孔(孔I31或孔II32)的横截面为梯形，使浆液能够沿着孔的孔壁向下流动，通过孔采用梯形结构能够对流体进行缓冲和负荷调节，这样不仅能够提高烟气的均匀性，加强气液传质效率，同时对浆液循环量和机组负荷具有较高适应性，极大地提高对二氧化硫和粉尘的深度脱除效果。
本实施例中，所述孔(孔I31或孔II32)的横截面为等腰梯形，其上孔(孔I的上孔31a或孔II的上孔)的直径大于下孔(孔I的下孔31b或孔II的下孔)的直径，使其能够对流体的流量进行控制，实现负荷调节，孔壁与下孔端面之间的夹角α为90～165°，使浆液能够沿着孔壁向下流动，对浆液形成缓冲，这样更加有利于加强气液传质效率，保证烟气与浆液能够更好的结合，并进一步提高负荷调节能力，提高适应性。
本实施例中，各分区上分布的孔的孔隙率为不均等孔隙率，以提高对流场的适应能力，进一步增强自适应性。
本实施例中，所述孔(孔I31或孔II32)的上孔(孔I的上孔31a或孔II的上孔)和下孔(孔I的下孔31b或孔II的下孔)的直径通过孔隙率确定，即
Figure PCTCN2016095407-appb-000002
式中，K为孔隙率，d1为上孔直径，d2为下孔直径，ε为常数，ε的取值范围为0.8～1.0，L为相邻两个孔的上孔边缘之间的间距，这样使孔的设置和分布更加合理，进一步提高负荷调节能力，传质效率高，自适应能力好，提高脱除效果。
本实施例中，各个分区上的孔呈多边形布置，本实施例的各个分区上的孔可采用三角形或正方形或长方形或平行四边形或其它多边形方式布置，以提高自适应能力。
本实施例中，各个分区分别为单独的板体，传质构件1由各板体拼接组成，便于加工制造；当然，各个分区也可设置在一个板体上。
本实施例中，所述板体的厚度为3～20mm，以保证板体的强度，且便于制造。
本实施例中，所述传质构件1设置在脱硫吸收塔4内，位于脱硫吸收塔4的烟气入口5与脱硫吸收塔4内设置的浆液喷淋层6之间，浆液喷淋层6向下喷淋浆液，浆液自上向下流动，烟气入口5进入的烟气向上流动，浆液和烟气流经传质构件1上的孔进行传质。
本实施例中，所述传质构件1与脱硫吸收塔4的烟气入口5之间的距离为500～2000mm，保证烟气能够充分完全的流经传质构件，以最大化提高传质效率，经济实用。
本实施例中，使用时，浆液喷淋层6的浆液7喷淋在传质构件1上形成用于对流体进行负荷调节的沸腾式泡沫层8，该沸腾式泡沫层8的高度为100～500mm，通过沸腾式泡沫层8的部分泡沫落入传质构件1的孔内，使浆液能够沿着孔的孔壁向下流动，进一步对浆液7和烟气进行负荷调节，以提高传质效率。
最后说明的是，以上实施例仅用以说明本发明的技术方案而非限制，尽管参照较佳实施例对本发明进行了详细说明，本领域的普通技术人员应当理解， 可以对本发明的技术方案进行修改或者等同替换，而不脱离本发明技术方案的宗旨和范围，其均应涵盖在本发明的权利要求范围当中。

Claims (10)

  1. 一种自适应沸腾式泡沫脱硫除尘装置，其特征在于：包括用于对脱硫吸收塔内流体进行传质的传质构件，所述传质构件为板状结构，该传质构件包括至少三个沿纵向并排设置的分区，每个分区上沿纵向并排设有至少两组用于流体通过的孔，每组孔由两种不同孔径的孔组成，每组孔中两种不同孔径的孔沿横向间隔设置，所述孔的横截面为梯形。
  2. 根据权利要求1所述的自适应沸腾式泡沫脱硫除尘装置，其特征在于：所述孔的横截面为等腰梯形，其上孔的直径大于下孔的直径，孔壁与下孔端面之间的夹角α为90～165°。
  3. 根据权利要求2所述的自适应沸腾式泡沫脱硫除尘装置，其特征在于：各分区上分布的孔的孔隙率为不均等孔隙率。
  4. 根据权利要求3所述的自适应沸腾式泡沫脱硫除尘装置，其特征在于：所述孔的上孔和下孔的直径通过孔隙率确定，即
    Figure PCTCN2016095407-appb-100001
    式中，K为孔隙率，d1为上孔直径，d2为下孔直径，ε为常数，ε的取值范围为0.8～1.0，L为相邻两个孔的上孔边缘之间的间距。
  5. 根据权利要求4所述的自适应沸腾式泡沫脱硫除尘装置，其特征在于：各个分区上的孔呈多边形布置。
  6. 根据权利要求1所述的自适应沸腾式泡沫脱硫除尘装置，其特征在于：各个分区分别为单独的板体，传质构件由各板体拼接组成。
  7. 根据权利要求6所述的自适应沸腾式泡沫脱硫除尘装置，其特征在于：所述板体的厚度为3～20mm。
  8. 根据权利要求1所述的自适应沸腾式泡沫脱硫除尘装置，其特征在于：所述传质构件设置在脱硫吸收塔内，位于脱硫吸收塔的烟气入口与脱硫吸收塔内设置的浆液喷淋层之间。
  9. 根据权利要求8所述的自适应沸腾式泡沫脱硫除尘装置，其特征在于：所述传质构件与脱硫吸收塔的烟气入口之间的距离为500～2000mm。
  10. 根据权利要求8所述的自适应沸腾式泡沫脱硫除尘装置，其特征在于：使用时，浆液喷淋层的浆液喷淋在传质构件上形成用于对流体进行负荷调节的沸腾式泡沫层，该沸腾式泡沫层的高度为100～500mm。
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