CN108479323A - A kind of deacidifying device for garbage-incineration smoke purifying - Google Patents
A kind of deacidifying device for garbage-incineration smoke purifying Download PDFInfo
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- CN108479323A CN108479323A CN201810576155.8A CN201810576155A CN108479323A CN 108479323 A CN108479323 A CN 108479323A CN 201810576155 A CN201810576155 A CN 201810576155A CN 108479323 A CN108479323 A CN 108479323A
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- 239000000779 smoke Substances 0.000 title claims abstract description 11
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 74
- 239000003546 flue gas Substances 0.000 claims abstract description 74
- 239000000376 reactant Substances 0.000 claims abstract description 71
- 239000013618 particulate matter Substances 0.000 claims abstract description 5
- 239000007789 gas Substances 0.000 claims description 19
- 238000000034 method Methods 0.000 claims description 7
- 239000000463 material Substances 0.000 claims description 4
- 235000019738 Limestone Nutrition 0.000 claims 1
- 239000003795 chemical substances by application Substances 0.000 claims 1
- 235000019504 cigarettes Nutrition 0.000 claims 1
- 239000006028 limestone Substances 0.000 claims 1
- 238000004056 waste incineration Methods 0.000 abstract description 19
- 238000000746 purification Methods 0.000 abstract description 14
- 239000000428 dust Substances 0.000 abstract description 12
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical class [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 9
- 239000002253 acid Substances 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 239000000843 powder Substances 0.000 description 5
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 4
- 235000011941 Tilia x europaea Nutrition 0.000 description 4
- 239000004571 lime Substances 0.000 description 4
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 3
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 3
- 235000011116 calcium hydroxide Nutrition 0.000 description 3
- 239000000920 calcium hydroxide Substances 0.000 description 3
- 229910001385 heavy metal Inorganic materials 0.000 description 3
- 150000002013 dioxins Chemical class 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000011152 fibreglass Substances 0.000 description 2
- 239000010881 fly ash Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- -1 SO x Substances 0.000 description 1
- 238000000889 atomisation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- YEBIHIICWDDQOL-YBHNRIQQSA-N polyoxin Chemical compound O[C@@H]1[C@H](O)[C@@H](C(C=O)N)O[C@H]1N1C(=O)NC(=O)C(C(O)=O)=C1 YEBIHIICWDDQOL-YBHNRIQQSA-N 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
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- 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
- B01D53/32—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 by electrical effects other than those provided for in group B01D61/00
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/02—Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
-
- 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
- B01D53/46—Removing components of defined structure
- B01D53/68—Halogens or halogen compounds
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0283—Flue gases
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Environmental & Geological Engineering (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Treating Waste Gases (AREA)
Abstract
本发明提供一种用于垃圾焚烧烟气净化的脱酸装置,包括:烟气荷电器,配置为使进入所述烟气荷电器的烟气带电以形成荷电烟气;反应剂荷电器,配置为使进入所述反应剂荷电器内的反应剂带电以形成荷电反应剂,所述荷电反应剂的电荷与所述荷电烟气的电荷相反;混合器,所述混合器分别与所述烟气荷电器以及所述反应剂荷电器相连接,配置为使所述荷电烟气与所述荷电反应剂结合;除尘器,所述除尘器与所述混合器相连接,配置为去除所述烟气中的颗粒物。根据本发明提供的用于垃圾焚烧烟气净化的脱酸装置,通过设置烟气荷电器和反应剂荷电器以使烟气和反应剂荷上电性相反的电荷,然后在混合器中结合,提高了脱酸反应效率,节约了运行成本。
The present invention provides a deacidification device for purifying waste incineration flue gas, comprising: a flue gas charger configured to charge the flue gas entering the flue gas charger to form charged flue gas; a reactant charger, configured to charge a reactant entering the reactant charger to form a charged reactant, the charged reactant having a charge opposite to that of the charged smoke; a mixer, the mixer being respectively connected to The flue gas charger and the reactant charger are connected and configured to combine the charged flue gas with the charged reactant; the dust remover is connected to the mixer and configured To remove particulate matter in the flue gas. According to the deacidification device for waste incineration flue gas purification provided by the present invention, by setting the flue gas charger and the reactant charger so that the flue gas and the reactant are charged with opposite charges, and then combined in the mixer, The efficiency of the deacidification reaction is improved, and the operating cost is saved.
Description
技术领域technical field
本发明涉及焚烧发电领域,具体地,涉及一种用于垃圾焚烧烟气净化的脱酸装置。The invention relates to the field of incineration power generation, in particular to a deacidification device for purifying waste incineration flue gas.
背景技术Background technique
在垃圾焚烧烟气净化技术领域,控制酸性气体排放是重要的烟气净化项目。目前垃圾焚烧电厂常常将干法脱酸设备布置在半干法脱酸设备后,二者同时使用,控制酸性气体达标排放。干法脱酸多采用管道喷射法,即将消石灰粉通过气力输送方式直接送入半干式脱酸反应塔和布袋除尘器之间的烟道里,在布袋除尘器里面,消石灰和酸性气体反应,产物变成飞灰被布袋除尘器捕集,达到脱酸目的。另外,脱除重金属和二噁英也是采用类似的方式,将活性炭粉末通过气力输送的方式送入半干式脱酸反应塔和布袋除尘器之间的烟道里,活性炭吸附重金属和二噁英后被除尘器捕集下来。In the field of waste incineration flue gas purification technology, the control of acid gas emissions is an important flue gas purification project. At present, waste incineration power plants often arrange dry deacidification equipment after semi-dry deacidification equipment, and use both at the same time to control acid gas emissions. The dry deacidification mostly adopts the pipeline injection method, that is, the slaked lime powder is directly sent into the flue between the semi-dry deacidification reaction tower and the bag filter through pneumatic conveying. In the bag filter, the slaked lime and acid gas react to produce It turns into fly ash and is collected by the bag filter to achieve the purpose of deacidification. In addition, a similar method is used to remove heavy metals and dioxins. The activated carbon powder is sent into the flue between the semi-dry deacidification reaction tower and the bag filter by pneumatic conveying. After the activated carbon absorbs heavy metals and dioxins Trapped by the dust collector.
但由于干法脱酸设备脱酸效率较低、运行成本高等原因,常常处于停运的状态,许多垃圾焚烧电厂的做法是在半干法脱酸设备上加大给料投入,停运干法脱酸设备,虽然这样做也能控制酸性气体达标排放,但也会给半干法脱酸设备带来很多问题,如雾化器雾化效果变差、雾化器更换频繁、反应塔出口温度过低等。However, due to the low deacidification efficiency and high operating cost of the dry deacidification equipment, it is often in a state of outage. The practice of many waste incineration power plants is to increase the input of materials on the semi-dry deacidification equipment, and shut down the dry deacidification equipment. Deacidification equipment, although this can also control the emission of acid gas up to the standard, it will also bring many problems to the semi-dry deacidification equipment, such as poor atomization effect of the atomizer, frequent replacement of the atomizer, and the outlet temperature of the reaction tower. Too low etc.
因此,有必要提出一种新的用于垃圾焚烧烟气净化的脱酸装置,以解决上述问题。Therefore, it is necessary to propose a new deacidification device for waste incineration flue gas purification to solve the above problems.
发明内容Contents of the invention
在发明内容部分中引入了一系列简化形式的概念,这将在具体实施方式部分中进一步详细说明。本发明的发明内容部分并不意味着要试图限定出所要求保护的技术方案的关键特征和必要技术特征,更不意味着试图确定所要求保护的技术方案的保护范围。A series of concepts in simplified form are introduced in the Summary of the Invention, which will be further detailed in the Detailed Description. The summary of the invention in the present invention does not mean to limit the key features and essential technical features of the claimed technical solution, nor does it mean to try to determine the protection scope of the claimed technical solution.
本发明提供一种用于垃圾焚烧烟气净化的脱酸装置,包括:The invention provides a deacidification device for purifying waste incineration flue gas, comprising:
烟气荷电器,配置为使进入所述烟气荷电器的烟气带电以形成荷电烟气;A gas charger configured to charge the gas entering the gas charger to form charged gas;
反应剂荷电器,配置为使进入所述反应剂荷电器内的反应剂带电以形成荷电反应剂,所述荷电反应剂的电荷与所述荷电烟气的电荷相反;a reactant charger configured to charge a reactant entering the reactant charger to form a charged reactant having a charge opposite to that of the charged smoke;
混合器,所述混合器分别与所述烟气荷电器以及所述反应剂荷电器相连接,配置为使所述荷电烟气与所述荷电反应剂结合;a mixer, the mixer is respectively connected to the gas charger and the reactant charger, and is configured to combine the charged smoke with the charged reactant;
除尘器,所述除尘器与所述混合器相连接,配置为去除所述烟气中的颗粒物。a dust remover, the dust remover is connected to the mixer and is configured to remove particulate matter in the flue gas.
进一步,所述脱酸装置还包括:Further, the deacidification device also includes:
半干法脱酸反应塔,配置为对烟气进行脱酸,经过所述半干法脱酸反应塔处理后的烟气排至所述烟气荷电器中。The semi-dry deacidification reaction tower is configured to deacidify flue gas, and the flue gas treated by the semi-dry deacidification reaction tower is discharged into the flue gas charger.
进一步,所述反应剂包括石灰粉。Further, the reactant includes lime powder.
进一步,所述烟气荷电器和所述反应剂荷电器包括导流板、电晕线和接地极板。Further, the gas charger and the reactant charger include a deflector, a corona wire and a grounding plate.
进一步,所述电晕线垂直于烟气或反应剂流动方向布置,合并后接入高压直流电源,所述接地极板设置于所述电晕线的两侧。Further, the corona wires are arranged perpendicular to the flow direction of the flue gas or the reactant, and connected to a high-voltage DC power supply after being combined, and the grounding plates are arranged on both sides of the corona wires.
进一步,所述电晕线包括芒刺线或鱼骨线。Further, the corona wire includes prickly wire or herringbone wire.
进一步,所述高压直流电源提供8KV-10KV直流高压输出的高频电源。Further, the high-voltage DC power supply provides a high-frequency power supply with a DC high-voltage output of 8KV-10KV.
进一步,所述接地极板形成多个放电通道。Further, the ground plate forms a plurality of discharge channels.
进一步,所述接地极板的材料包括导电玻璃钢。Further, the material of the ground plate includes conductive glass fiber reinforced plastic.
进一步,所述荷电烟气带正电荷,所述荷电反应剂带负电荷。Further, the charged smoke is positively charged, and the charged reactant is negatively charged.
根据本发明提供的用于垃圾焚烧烟气净化的脱酸装置,通过设置烟气荷电器和反应剂荷电器以使烟气和反应剂荷上电性相反的电荷,然后在混合器中结合,提高了脱酸反应效率,节约了运行成本。According to the deacidification device for waste incineration flue gas purification provided by the present invention, by setting the flue gas charger and the reactant charger so that the flue gas and the reactant are charged with opposite charges, and then combined in the mixer, The efficiency of the deacidification reaction is improved, and the operating cost is saved.
附图说明Description of drawings
本发明的下列附图在此作为本发明的一部分用于理解本发明。附图中示出了本发明的实施例及其描述,用来解释本发明的装置及原理。在附图中,The following drawings of the invention are hereby included as part of the invention for understanding the invention. Embodiments of the present invention and their descriptions are shown in the drawings to explain the device and principle of the present invention. In the attached picture,
图1为本发明的一种用于垃圾焚烧烟气净化的脱酸装置的示意图;Fig. 1 is a kind of schematic diagram of the deacidification device that is used for waste incineration flue gas purification of the present invention;
图2为本发明的烟气荷电器的示意图;Fig. 2 is the schematic diagram of the flue gas charger of the present invention;
图3为本发明的反应剂荷电器的示意图;Fig. 3 is the schematic diagram of reactant charger of the present invention;
图4为本发明的反应剂管道布置示意图;Fig. 4 is a schematic diagram of reactant pipeline layout of the present invention;
图5为本发明的反应剂管道布置示意图。Fig. 5 is a schematic diagram of the arrangement of reactant pipelines in the present invention.
附图标识Reference sign
1、半干法脱酸反应塔 2、烟气荷电器 3、反应剂荷电器1. Semi-dry deacidification reaction tower 2. Flue gas charger 3. Reactant charger
4、混合器 5、反应剂管道 6、除尘器4. Mixer 5. Reactant pipeline 6. Dust collector
7、烟气导流板 8、正极电晕线 9、接地极板7. Smoke deflector 8. Positive corona wire 9. Grounding plate
10、反应剂气流导流板 11、负极电晕线10. Reactant air deflector 11. Negative electrode corona wire
具体实施方式Detailed ways
在下文的描述中,给出了大量具体的细节以便提供对本发明更为彻底的理解。然而,对于本领域技术人员而言显而易见的是,本发明可以无需一个或多个这些细节而得以实施。在其他的例子中,为了避免与本发明发生混淆,对于本领域公知的一些技术特征未进行描述。In the following description, numerous specific details are given in order to provide a more thorough understanding of the present invention. It will be apparent, however, to one skilled in the art that the present invention may be practiced without one or more of these details. In other examples, some technical features known in the art are not described in order to avoid confusion with the present invention.
为了彻底理解本发明,将在下列的描述中提出详细的步骤,以便阐释本发明提出的一种用于垃圾焚烧烟气净化的脱酸装置。显然,本发明的施行并不限定于本领域的技术人员所熟习的特殊细节。本发明的较佳实施例详细描述如下,然而除了这些详细描述外,本发明还可以具有其他实施方式。In order to thoroughly understand the present invention, detailed steps will be provided in the following description to illustrate a deacidification device for waste incineration flue gas purification proposed by the present invention. It is evident that the practice of the invention is not limited to specific details familiar to those skilled in the art. Preferred embodiments of the present invention are described in detail below, however, the present invention may have other embodiments besides these detailed descriptions.
应当理解的是,当在本说明书中使用术语“包含”和/或“包括”时,其指明存在所述特征、整体、步骤、操作、元件和/或组件,但不排除存在或附加一个或多个其他特征、整体、步骤、操作、元件、组件和/或它们的组合。It should be understood that when the terms "comprising" and/or "comprising" are used in this specification, they indicate the presence of the features, integers, steps, operations, elements and/or components, but do not exclude the presence or addition of one or Multiple other features, integers, steps, operations, elements, components and/or combinations thereof.
本发明提供了一种用于垃圾焚烧烟气净化的脱酸装置,如图1所示,包括:烟气荷电器2,反应剂荷电器3,混合器4和除尘器6。The present invention provides a deacidification device for purifying waste incineration flue gas. As shown in FIG.
本发明提供的用于垃圾焚烧烟气净化的脱酸装置还包括半干法脱酸反应塔1。示例性地,所述半干法脱酸反应塔1内设置有雾化器,将消石灰浆液喷入所述半干法脱酸反应塔1内与烟气中的酸性气体(如SOx、HCl等)发生反应,以实现脱酸的目的。The deacidification device used for purification of waste incineration flue gas provided by the present invention also includes a semi-dry deacidification reaction tower 1 . Exemplarily, the semi-dry deacidification reaction tower 1 is provided with an atomizer, and the slaked lime slurry is sprayed into the semi-dry deacidification reaction tower 1 and acid gases (such as SO x , HCl etc.) to react to achieve the purpose of deacidification.
经半干法脱酸反应塔1排出的烟气进入烟气荷电器2中,所述烟气荷电器2配置为使进入所述烟气荷电器内的烟气带电以形成荷电烟气。The flue gas discharged from the semi-dry deacidification reaction tower 1 enters the flue gas charger 2, and the flue gas charger 2 is configured to charge the flue gas entering the flue gas charger to form charged flue gas.
参照图2,所述烟气荷电器2包括烟气导流板7、正极电晕线8和接地极板9。进一步,正极电晕线8垂直于烟气流动方向布置,合并后接入正高压直流电源,所述正高压直流电源可提供8KV-10KV的直流高压输出,电压和电流可调,实时数值可通过电源自带数字面板显示。进一步,所述接地极板9设置于所述正极电晕线8的两侧,以形成放电通道。烟气荷电器2中设置有至少2个接地极板9,以形成至少一个放电通道,烟气荷电器2中还可以设置有多个接地极板9,以形成多个放电通道。从半干法脱酸反应塔1排出的烟气经过烟气导流板7被均匀分散于烟气荷电器2内,在放电通道被荷上正电荷。Referring to FIG. 2 , the gas charger 2 includes a gas deflector 7 , a positive corona wire 8 and a ground plate 9 . Further, the positive corona wire 8 is arranged perpendicular to the flow direction of the flue gas, and after being combined, it is connected to a positive high-voltage DC power supply. The positive high-voltage DC power supply can provide a DC high-voltage output of 8KV-10KV. The voltage and current are adjustable, and the real-time value can be passed through The power supply comes with a digital panel display. Further, the ground plate 9 is arranged on both sides of the positive corona wire 8 to form a discharge channel. At least two grounding plates 9 are arranged in the gas charger 2 to form at least one discharge channel, and a plurality of grounding plates 9 may also be arranged in the gas charger 2 to form multiple discharge channels. The flue gas discharged from the semi-dry deacidification reaction tower 1 is evenly dispersed in the flue gas charger 2 through the flue gas deflector 7, and is positively charged in the discharge channel.
本发明提供的用于垃圾焚烧烟气净化的脱酸装置还包括反应剂荷电器3,配置为使进入所述反应剂荷电器3内的反应剂带电以形成荷电反应剂,所述荷电反应剂的电荷与所述荷电烟气的电荷相反。The deacidification device for waste incineration flue gas purification provided by the present invention also includes a reactant charger 3 configured to charge the reactant entering the reactant charger 3 to form a charged reactant, the charged reactant The charge of the reactant is opposite to that of the charged smoke.
参照图3,所述反应剂荷电器3包括反应剂气流导流板10、负极电晕线11和接地极板9。进一步,负极电晕线11垂直于反应剂气流流动方向布置,合并后接入负高压直流电源,所述负高压直流电源可提供8KV-10KV的直流高压输出,电压和电流可调,实时数值可通过电源自带数字面板显示。进一步,所述接地极板9设置于所述负极电晕线11的两侧,以形成放电通道。反应剂荷电器3中设置有至少2个接地极板9,以形成至少一个放电通道,反应剂荷电器3中还可以设置有多个接地极板9,以形成多个放电通道。所述反应剂包括石灰粉。细小的石灰粉经过反应剂气流导流板10被均匀分散于反应剂荷电器3内,在放电通道被荷上负电荷。Referring to FIG. 3 , the reactant charger 3 includes a reactant air flow deflector 10 , a negative corona wire 11 and a grounding plate 9 . Further, the negative corona wire 11 is arranged perpendicular to the flow direction of the reactant gas flow, and connected to a negative high-voltage DC power supply after being combined. The negative high-voltage DC power supply can provide a DC high-voltage output of 8KV-10KV, the voltage and current are adjustable, and the real-time value can be adjusted. Through the power supply comes with a digital panel display. Further, the ground plate 9 is arranged on both sides of the negative corona wire 11 to form a discharge channel. The reactant charger 3 is provided with at least two grounded plates 9 to form at least one discharge channel, and the reactant charger 3 may also be provided with multiple grounded plates 9 to form multiple discharge channels. The reactant includes lime powder. The fine lime powder is uniformly dispersed in the reactant charger 3 through the reactant airflow deflector 10, and is charged with a negative charge in the discharge channel.
示例性地,所述正极电晕线8和负极电晕线11包括芒刺线或鱼骨线;所述接地极板9的材料包括导电玻璃钢。Exemplarily, the positive corona wire 8 and the negative corona wire 11 include prickly wire or herringbone wire; the material of the ground plate 9 includes conductive glass fiber reinforced plastic.
本发明提供的用于垃圾焚烧烟气净化的脱酸装置还包括混合器4,所述混合器4分别与所述烟气荷电器2以及所述反应剂荷电器3相连接,配置为使所述荷电烟气与所述荷电反应剂结合。The deacidification device for waste incineration flue gas purification provided by the present invention also includes a mixer 4, which is connected to the flue gas charger 2 and the reactant charger 3 respectively, and is configured to make the The charged smoke is combined with the charged reactant.
在一个实施例中,烟气荷电器2排出的荷电烟气进入混合器4中,反应剂荷电器3排出的荷电反应剂经反应剂管道5进入混合器4中,带正电的荷电烟气和带负电的荷电反应剂在混合器内充分混合,二者在库仑力的作用下相互吸引并结合。相比烟气和反应剂不带电荷的情况,石灰粉颗粒能与更多的酸性气体分子结合,提高了反应效率。In one embodiment, the charged flue gas discharged from the gas charger 2 enters the mixer 4, the charged reactant discharged from the reactant charger 3 enters the mixer 4 through the reactant pipeline 5, and the positively charged The electric smoke and the negatively charged reactants are fully mixed in the mixer, and the two attract and combine with each other under the action of Coulomb force. Compared with the case where the flue gas and the reactants are not charged, the lime powder particles can combine with more acid gas molecules, which improves the reaction efficiency.
进一步,反应剂管道5有多种布置方式。可以是多路进反应剂,如图4所示的三种,也可以是更多路进反应剂,这取决于反应剂量及管径等因素。也可以是多个进反应剂的方向,图5列出了两种布置方式,每一种布置方式都有不同的混合效果,可根据实际选用最优的方式。Further, there are various arrangements of the reactant pipeline 5 . It can be multi-path reactant, three kinds shown in Fig. 4, also can be more path-feed reactant, and this depends on factors such as reactant dose and tube diameter. There can also be multiple directions for entering the reactants. Figure 5 lists two arrangements, each arrangement has a different mixing effect, and the optimal method can be selected according to the actual situation.
本发明提供的用于垃圾焚烧烟气净化的脱酸装置还包括除尘器6,所述除尘器6与所述混合器4相连接,配置为去除所述烟气中的颗粒物。进一步,从混合器4中排出的烟气在混合器4除尘器6之间的管道中混合活性炭后进入除尘器6中,作为一个实例,除尘器6包括布袋除尘器,布袋将烟气中的粉尘、脱酸产物、吸附有有害物质的活性炭等颗粒物收集下来,送至飞灰储存仓(未示出)。The deacidification device for purification of waste incineration flue gas provided by the present invention further includes a dust collector 6 connected to the mixer 4 and configured to remove particulate matter in the flue gas. Further, the flue gas discharged from the mixer 4 enters the dust collector 6 after being mixed with activated carbon in the pipeline between the mixer 4 and the dust collector 6. As an example, the dust collector 6 includes a bag filter, and the bag removes the dust in the flue gas. Particles such as dust, deacidification products, and activated carbon adsorbed with harmful substances are collected and sent to a fly ash storage bin (not shown).
在一个实施例中,本发明提供的用于垃圾焚烧烟气净化的脱酸装置还包括第二反应剂荷电器,以使活性炭荷上与荷电烟气电性相反的电荷,提高重金属和二噁英的吸附效率。In one embodiment, the deacidification device used for waste incineration flue gas purification provided by the present invention also includes a second reactant charger, so that the activated carbon is charged with a charge opposite to that of the charged flue gas, and the concentration of heavy metals and secondary The adsorption efficiency of oxins.
本发明提供的用于垃圾焚烧烟气净化的脱酸装置的工作过程为:烟气首先经过半干法脱酸反应塔1脱酸后进入烟气荷电器2,在烟气荷电器2中荷上正电荷形成荷电烟气,然后进入混合器4中;反应剂进入反应剂荷电器3中荷上负电荷形成荷电反应剂,然后经由反应剂管道5也进入混合器4中;荷电烟气和荷电反应剂在混合器4中相互吸引并结合,然后进入除尘器6以去除烟气中的颗粒物。The working process of the deacidification device used for waste incineration flue gas purification provided by the present invention is as follows: the flue gas first passes through the semi-dry deacidification reaction tower 1 to deacidify and then enters the flue gas charger 2, and the flue gas is charged in the flue gas charger 2 The positive charge forms the charged smoke, and then enters the mixer 4; the reactant enters the reactant charger 3 and is charged with a negative charge to form a charged reactant, and then also enters the mixer 4 through the reactant pipeline 5; The flue gas and charged reactants are attracted and combined in the mixer 4, and then enter the dust collector 6 to remove particulate matter in the flue gas.
根据本发明提供的用于垃圾焚烧烟气净化的脱酸装置,通过设置烟气荷电器和反应剂荷电器以使烟气和反应剂荷上电性相反的电荷,然后在混合器中结合,提高了脱酸反应效率,节约了运行成本。According to the deacidification device for waste incineration flue gas purification provided by the present invention, by setting the flue gas charger and the reactant charger so that the flue gas and the reactant are charged with opposite charges, and then combined in the mixer, The efficiency of the deacidification reaction is improved, and the operating cost is saved.
本发明已经通过上述实施例进行了说明,但应当理解的是,上述实施例只是用于举例和说明的目的,而非意在将本发明限制于所描述的实施例范围内。此外本领域技术人员可以理解的是,本发明并不局限于上述实施例,根据本发明的教导还可以做出更多种的变型和修改,这些变型和修改均落在本发明所要求保护的范围以内。本发明的保护范围由附属的权利要求书及其等效范围所界定。The present invention has been described through the above-mentioned embodiments, but it should be understood that the above-mentioned embodiments are only for the purpose of illustration and description, and are not intended to limit the present invention to the scope of the described embodiments. In addition, those skilled in the art can understand that the present invention is not limited to the above-mentioned embodiments, and more variations and modifications can be made according to the teachings of the present invention, and these variations and modifications all fall within the claimed scope of the present invention. within the range. The protection scope of the present invention is defined by the appended claims and their equivalent scope.
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