CN205730737U - 一种超细雾预除尘高效除雾器 - Google Patents
一种超细雾预除尘高效除雾器 Download PDFInfo
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- CN205730737U CN205730737U CN201620355806.7U CN201620355806U CN205730737U CN 205730737 U CN205730737 U CN 205730737U CN 201620355806 U CN201620355806 U CN 201620355806U CN 205730737 U CN205730737 U CN 205730737U
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- 238000001556 precipitation Methods 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L sulfate Chemical compound 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[O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound 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[S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Abstract
本实用新型公开了一种超细雾预除尘高效除雾器，包括屋脊式除雾器与管式除雾器组成的除雾层和超细喷雾层，屋脊式除雾层是由折流板和固定装置搭建的“人”字型结构，并配有冲洗装置；超细喷雾层由密布的细雾层管道及支架、细雾喷嘴，配有供水系统。脱硫塔内含有粉尘的烟气首先流经装置底部的超细喷雾层，被细雾喷嘴喷射出的超细雾滴吸收除尘后，进入除雾层。利用折流板惯性分离的除雾作用，使含有粉尘的液滴得到进一步去除，从而使得该除雾器能较好的解决烟囱下雨或下石膏雨的现象。
Description
所属技术领域
[0001]本实用新型涉及烟气除雾器技术领域，具体涉及一种超细雾预除尘高效除雾器，主要适用于脱硫塔除雾器的固定应用。
背景技术
[0002] 脱硫塔是对工业烟气和废气进行脱硫处理的设备，湿法烟气脱硫工艺使用的脱硫塔在脱硫处理过程中，将产生一定粒径的“雾”，“雾”包括水分，以及硫酸盐等粉尘颗粒物，如果直接从烟囱排出，将产生石膏雨，污染工厂周围环境。因此，湿法脱硫工艺上提出除雾除尘的要求，脱硫后的烟气必须经过除雾除尘后方可排放。现阶段，脱硫塔内主要采用除雾器进行除雾处理。除雾器能够除掉烟气中大部分的水分，但对粉尘颗粒物的处理作用比较小。除雾器未能除掉的粉尘则需要在脱硫塔出口管道上设置湿式或者干式电除尘器进行除尘，方能达到国家规定的排放标准，电除尘器投资额巨大。
[0003]目前国内外采用的除雾器主要包括平板式除雾器、菱形除雾器、屋脊式除雾器和管式除雾器等几种形式，使用中这几种除雾器或单独使用，或若干种组合使用。虽然能起到很好的除雾效果，但除尘效果不好，仍需要设置电除尘器处理后方能排放。
实用新型内容
[0004]本实用新型针对上述问题，提供一种超细雾预除尘高效除雾器，能够提高现有除雾器的除尘效果，由这种超细雾预除尘高效除雾器处理过的烟气中的粉尘含量大大降低，从而在后续管道上无需设置其他除尘设备。
[0005]超细雾预除尘高效除雾器位于脱硫塔内，包括除雾层和超细喷雾层，超细喷雾层位于除雾层下方；
[0006]除雾层由一层或多层屋脊式除雾器组成，或者由一层或多层屋脊式除雾器与管式除雾器共同组成；
[0007]屋脊式除雾器包括折流板、固定装置和冲洗装置，固定装置包括上端板、下端板、卡条、方形梁、连接件;冲洗装置包括冲洗管道、冲洗喷嘴、冲洗管道支架；
[0008]超细除雾层为一层或者多层，各层均由细雾层管道、细雾喷嘴、细雾层支架组成，各层的细雾层管道均包括主管道与支管道，细雾喷嘴均安装在支管道上，
[0009]各层的细雾层管道通过细雾层支架连接为一体，并通过细雾层支架将超细除雾层安装在除雾层底部，或者通过细雾层支架与脱硫塔固定；
[0010]细雾层管道材质为金属或PPH，细雾层管道的主管道与支管道直径均为5〜300mm，细雾喷嘴材质为金属或塑料，细雾层支架材质为金属或PPH;
[0011 ]超细喷雾层的细雾喷嘴，是根据烟气粉尘的粒径进行选择，具体要求如下:细雾喷嘴工作压力为0.1〜5.0MPa，喷射角度为10°〜180°，喷射流量为0.2〜100升每立方米，喷射雾滴的粒径为10〜5000微米，所有细雾喷嘴喷射出的水雾，能够覆盖脱硫塔截面积的50%〜100%，以实现雾滴吸收烟气中大量的粉尘后，由于重量增加，一部分直接下降到脱硫塔底部，被集中回收，另一部分随烟气上升进入除雾层，经屋脊式除雾器折流板的惯性分离作用，与烟气中原有的水分一同与烟气脱离，吸附于折流板表面，在屋脊式除雾器的冲洗装置冲洗下，下落到脱硫塔底部被集中回收；
[0012]超细雾预除尘高效除雾器的供水系统位于脱硫塔外，包括水栗、自清洗过滤器、供水管道及法兰，供水系统与超细喷雾层连接;供水系统提供的水，经过超细喷雾层中各层的细雾层管道分配到各细雾喷嘴处，经细雾喷嘴喷射对烟气进行除尘处理。
[0013]这种超细雾预除尘高效除雾器由超细喷雾层和除雾层组合而成。除雾层主要起除雾作用，由一层或多层屋脊式除雾器及冲洗装置组成;或者采用一层或多层屋脊式除雾器与管式除雾器的组合，并设置冲洗装置组成。超细喷雾层起除尘作用，由细雾层管道、细雾喷嘴、细雾层支架组成，安装在除雾层下方，通过细雾层支架与除雾器连接成一体;或者将超细雾层单独安装在除雾层下方，通过细雾层支架与脱硫塔连接。
[0014]本实用新型的技术效果在于，某一粒径的粉尘容易被特定粒径的雾滴吸收，形成包裹着粉尘颗粒物的雾滴。超细喷雾层能够从细雾喷嘴喷射出带有一定粒径范围的液体雾滴，雾滴吸收烟气中大量的粉尘后，由于重量增加，一部分直接下降到脱硫塔底部，被集中回收。另一部分随烟气上升进入除雾层，经屋脊式除雾器折流板的惯性分离作用，与烟气中原有的水分一同与烟气脱离，吸附于折流板表面。在屋脊式除雾器的冲洗装置冲洗下，下落到脱硫塔底部被集中回收。从而实现了对进入除雾器前的烟气预先进行除尘处理，提高了除雾器的除尘效果。
附图说明
[0015]图1是超细雾预除尘高效除雾器结构示意图；
[0016]图2是超细雾预除尘高效除雾器的除雾层俯视图；
[0017]图3是超细雾预除尘高效除雾器供水系统图；
[0018]图中:1、屋脊式除雾器;2、管式除雾器;3、超细喷雾层;4、上端板;5、冲洗管道;6、冲洗喷嘴;7、冲洗管道支架;8、卡条;9、折流板;10、下端板;11、连接件；12、方形梁；13、脱硫塔;14、细雾层支架；15、细雾层管道;16、细雾喷嘴；17、超细雾预除尘高效除雾器;18、水栗；
19、自清洗过滤器;20、供水管道。
具体实施方式
[0019]下面结合附图和实例对本实用新型进一步说明。
[0020]本实用新型实例提供的脱硫塔超细雾预除尘高效除雾器安装于示意图3所示的脱硫塔系统内。
[0021]超细雾预除尘高效除雾器位于脱硫塔内，包括除雾层和超细喷雾层，超细喷雾层位于除雾层下方；
[0022]除雾层由一层或多层屋脊式除雾器组成，或者由一层或多层屋脊式除雾器与管式除雾器共同组成；
[0023]屋脊式除雾器包括折流板、固定装置和冲洗装置，固定装置包括上端板、下端板、卡条、方形梁、连接件;冲洗装置包括冲洗管道、冲洗喷嘴、冲洗管道支架；
[0024]超细除雾层为一层或者多层，各层均由细雾层管道、细雾喷嘴、细雾层支架组成，各层的细雾层管道均包括主管道与支管道，细雾喷嘴均安装在支管道上，
[0025]各层的细雾层管道通过细雾层支架连接为一体，并通过细雾层支架将超细除雾层安装在除雾层底部，或者通过细雾层支架与脱硫塔固定；
[0026]细雾层管道材质为金属或PPH，细雾层管道的主管道与支管道直径均为5〜300mm，细雾喷嘴材质为金属或塑料，细雾层支架材质为金属或PPH;
[0027]超细喷雾层的细雾喷嘴，是根据烟气粉尘的粒径进行选择，具体要求如下:细雾喷嘴工作压力为0.1〜5.0MPa，喷射角度为10°〜180°，喷射流量为0.2〜100升每立方米，喷射雾滴的粒径为10〜5000微米，所有细雾喷嘴喷射出的水雾，能够覆盖脱硫塔截面积的50%〜100%，以实现雾滴吸收烟气中大量的粉尘后，由于重量增加，一部分直接下降到脱硫塔底部，被集中回收，另一部分随烟气上升进入除雾层，经屋脊式除雾器折流板的惯性分离作用，与烟气中原有的水分一同与烟气脱离，吸附于折流板表面，在屋脊式除雾器的冲洗装置冲洗下，下落到脱硫塔底部被集中回收；
[0028]超细雾预除尘高效除雾器的供水系统位于脱硫塔外，包括水栗、自清洗过滤器、供水管道及法兰，供水系统与超细喷雾层连接;供水系统提供的水，经过超细喷雾层中各层的细雾层管道分配到各细雾喷嘴处，经细雾喷嘴喷射对烟气进行除尘处理。
[0029] 锅炉排出的烟气进入脱硫塔，经过脱硫设备的脱硫处理后，烟气上升到超细雾预除尘高效除雾器。超细喷雾所用的水经自清洗过滤器水处理后，由水栗加压进入脱硫塔内超细雾预除尘高效除雾器的细雾层管道中，通过安装在管道上的细雾喷嘴喷射，对烟气的粉尘进行吸收除尘，在经过除雾层处理后从脱硫塔顶部排出。当进入脱硫塔内的烟气粉尘含量较高时，超细喷雾层的管道和喷嘴排列较密集，喷嘴喷射流量较大，喷嘴尺寸也较大；而粉尘含量较低时，超细喷雾层的管道和喷嘴排列较稀疏，喷嘴喷射流量较小，喷嘴尺寸也较小。细雾层管道包括主管道和支管道，布置方式由脱硫塔直径和烟尘含量决定。
[0030]上述实例仅供说明本实用新型之用，而非是对本实用新型的限制，有关技术领域的普通技术人员，在不脱离本实用新型的精神和范围的前提下，还可以作出各种变化和变形，因此所用等同的技术方案也应属于本实用新型的专利保护范畴，本实用新型的专利保护范围应该由各权利要求限定。
Claims (1)
1.一种超细雾预除尘高效除雾器，其特征在于: 超细雾预除尘高效除雾器位于脱硫塔内，包括除雾层和超细喷雾层，超细喷雾层位于除雾层下方； 除雾层由一层或多层屋脊式除雾器组成，或者由一层或多层屋脊式除雾器与管式除雾器共同组成； 屋脊式除雾器包括折流板、固定装置和冲洗装置，固定装置包括上端板、下端板、卡条、方形梁、连接件;冲洗装置包括冲洗管道、冲洗喷嘴、冲洗管道支架； 超细除雾层为一层或者多层，各层均由细雾层管道、细雾喷嘴、细雾层支架组成，各层的细雾层管道均包括主管道与支管道，细雾喷嘴均安装在支管道上， 各层的细雾层管道通过细雾层支架连接为一体，并通过细雾层支架将超细除雾层安装在除雾层底部，或者通过细雾层支架与脱硫塔固定； 细雾层管道材质为金属或PPH，细雾层管道的主管道与支管道直径均为5〜300mm，细雾喷嘴材质为金属或塑料，细雾层支架材质为金属或PPH; 超细喷雾层的细雾喷嘴，是根据烟气粉尘的粒径进行选择，具体要求如下:细雾喷嘴工作压力为0.1〜5.0MPa，喷射角度为10°〜180°，喷射流量为0.2〜100升每立方米，喷射雾滴的粒径为10〜5000微米； 超细雾预除尘高效除雾器的供水系统位于脱硫塔外，包括水栗、自清洗过滤器、供水管道及法兰，供水系统与超细喷雾层连接。
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