CN107138036A - 卡尔多炉焚烧电/线路板烟气净化方法 - Google Patents
卡尔多炉焚烧电/线路板烟气净化方法 Download PDFInfo
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- 230000005611 electricity Effects 0.000 title claims abstract description 23
- 238000000034 method Methods 0.000 title claims abstract description 13
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 18
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- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 claims abstract description 5
- 229910052794 bromium Inorganic materials 0.000 claims abstract description 5
- 150000002013 dioxins Chemical class 0.000 claims abstract description 5
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- 238000001816 cooling Methods 0.000 claims abstract description 4
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- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 36
- 239000002918 waste heat Substances 0.000 claims description 6
- KVGZZAHHUNAVKZ-UHFFFAOYSA-N 1,4-Dioxin Chemical compound O1C=COC=C1 KVGZZAHHUNAVKZ-UHFFFAOYSA-N 0.000 abstract description 3
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- 239000007789 gas Substances 0.000 description 3
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- 238000004140 cleaning Methods 0.000 description 1
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- 239000003517 fume Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
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Abstract
本发明涉及一种卡尔多炉焚烧电/线路板烟气净化方法,该方法包括以下步骤:⑴卡尔多炉焚烧电/线路板产生的烟气进入卡尔多炉焚烧电/线路板烟气净化烟道,然后经余热锅炉换热后,此时烟气温度降低至150℃~250℃;⑵所述步骤⑴所得的降温后的烟气依次进入动力波洗涤器Ⅰ、动力波洗涤器Ⅱ,并分别用碱液进行两级酸性气体吸收除尘,得到除尘后的烟气;⑶所述除尘后的烟气经干燥塔干燥后,进入活性炭吸附塔除去二噁英类物质及残留溴,然后经烟囱排空即可。本发明不但效率高,而且有效净化烟气,使排除的气体中二噁英含量100%达到国家规定标准。
Description
技术领域
本发明涉及卡尔多炉生产技术领域,尤其涉及卡尔多炉焚烧电/线路板烟气净化方法。
背景技术
目前,电/线路板的焚烧及绝大部分冶金企业烟气因条件所限制,并未进行特殊净化、处理,有个别良好企业仅是通过二噁英二次焚烧等方式做简单处理。故排出的烟气中酸性气体的含量严重超标,特别是二噁英含量超出国家规定达标含量的数倍、甚至数百倍,造成了严重的大气污染。因此,很多企业因烟气排放不达标而受到政府罚款,有严重者甚至导致被迫停产。
发明内容
本发明所要解决的技术问题是提供一种高效率的卡尔多炉焚烧电/线路板烟气净化方法。
为解决上述问题,本发明所述的卡尔多炉焚烧电/线路板烟气净化方法,包括以下步骤:
⑴卡尔多炉焚烧电/线路板产生的烟气进入卡尔多炉焚烧电/线路板烟气净化烟道,然后经余热锅炉换热后,此时烟气温度降低至150℃~250℃;
⑵所述步骤⑴所得的降温后的烟气依次进入动力波洗涤器Ⅰ、动力波洗涤器Ⅱ,并分别用碱液进行两级酸性气体吸收除尘,得到除尘后的烟气;
⑶所述除尘后的烟气经干燥塔干燥后,进入活性炭吸附塔除去二噁英类物质及残留溴,然后经烟囱排空即可。
所述步骤⑴中的卡尔多炉焚烧电/线路板烟气净化烟道,包括与卡尔多炉相连的烟道;所述烟道末端连有烟囱;所述烟道上按先后顺序依次连有余热锅炉、动力波洗涤器Ⅰ、动力波洗涤器Ⅱ、干燥塔、活性炭吸附塔。
所述步骤⑵动力波洗涤器Ⅰ中的碱液是指浓度为0.05g/L~0.15 g/L的氢氧化钠溶液。
所述步骤⑵动力波洗涤器Ⅱ中的碱液是指浓度为0.5g/L~1.5g/L的氢氧化钠溶液。
本发明与现有技术相比具有以下优点:
本发明将烟气通入余热锅炉换热,将温度从1100℃~1250℃极速降低到150℃~250℃,从源头减少了二噁英的产生量(塑料焚烧中二噁英产生的温度一般为400℃~600℃);后又通过动力波洗涤器将烟气进行两级酸性气体吸收、除尘;最后经干燥塔干燥后,进入活性炭吸附塔,除去剩余二噁英类物质及残留溴,不但效率高,而且有效净化烟气,使排除的气体中二噁英含量100%达到国家规定标准(国家标准0.1ng TEQ/Nm3即欧盟标准)。
附图说明
下面结合附图对本发明的具体实施方式作进一步详细的说明。
图1为本发明的结构示意图。
图中:1—烟道 2—余热锅炉 3—动力波洗涤器Ⅰ 4—动力波洗涤器Ⅱ 5—干燥塔 6—活性炭吸附塔 7—烟囱。
具体实施方式
卡尔多炉焚烧电/线路板烟气净化方法,包括以下步骤:
⑴卡尔多炉焚烧电/线路板产生的烟气进入卡尔多炉焚烧电/线路板烟气净化烟道,然后经余热锅炉2换热后,此时烟气温度降低至150℃~250℃。
其中:卡尔多炉焚烧电/线路板烟气净化烟道包括与卡尔多炉相连的烟道1(参见图1)。烟道1末端连有烟囱7,烟道1上按先后顺序依次连有余热锅炉2、动力波洗涤器Ⅰ3、动力波洗涤器Ⅱ4、干燥塔5、活性炭吸附塔6。
⑵步骤⑴所得的降温后的烟气依次进入动力波洗涤器Ⅰ3、动力波洗涤器Ⅱ4,并分别用碱液进行两级酸性气体吸收除尘,得到除尘后的烟气。
其中:动力波洗涤器Ⅰ3中的碱液是指浓度为0.05g/L~0.15 g/L的氢氧化钠溶液。
动力波洗涤器Ⅱ4中的碱液是指浓度为0.5 g/L~1.5g/L的氢氧化钠溶液。
⑶除尘后的烟气经干燥塔5干燥后,进入活性炭吸附塔6除去二噁英类物质及残留溴,然后经烟囱7排空即可。
Claims (4)
1.卡尔多炉焚烧电/线路板烟气净化方法,包括以下步骤:
⑴卡尔多炉焚烧电/线路板产生的烟气进入卡尔多炉焚烧电/线路板烟气净化烟道,然后经余热锅炉(2)换热后,此时烟气温度降低至150℃~250℃;
⑵所述步骤⑴所得的降温后的烟气依次进入动力波洗涤器Ⅰ(3)、动力波洗涤器Ⅱ(4),并分别用碱液进行两级酸性气体吸收除尘,得到除尘后的烟气;
⑶所述除尘后的烟气经干燥塔(5)干燥后,进入活性炭吸附塔(6)除去二噁英类物质及残留溴,然后经烟囱(7)排空即可。
2.如权利要求1所述的卡尔多炉焚烧电/线路板烟气净化方法,其特征在于:所述步骤⑴中的卡尔多炉焚烧电/线路板烟气净化烟道,包括与卡尔多炉相连的烟道(1);所述烟道(1)末端连有烟囱(7);所述烟道(1)上按先后顺序依次连有余热锅炉(2)、动力波洗涤器Ⅰ(3)、动力波洗涤器Ⅱ(4)、干燥塔(5)、活性炭吸附塔(6)。
3.如权利要求1所述的卡尔多炉焚烧电/线路板烟气净化方法,其特征在于:所述步骤⑵动力波洗涤器Ⅰ(3)中的碱液是指浓度为0.05g/L~0.15 g/L的氢氧化钠溶液。
4.如权利要求1所述的卡尔多炉焚烧电/线路板烟气净化方法,其特征在于:所述步骤⑵动力波洗涤器Ⅱ(4)中的碱液是指浓度为0.5 g/L~1.5g/L的氢氧化钠溶液。
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US20050013757A1 (en) * | 2003-07-16 | 2005-01-20 | Franz Windschmitt | Method and system for removing sulfur and dust from waste gases, particularly refinery waste gases |
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CN102728194A (zh) * | 2012-07-11 | 2012-10-17 | 光大环保科技发展(北京)有限公司 | 一种用于垃圾焚烧的烟气净化处理方法及装置 |
CN103623670A (zh) * | 2013-11-13 | 2014-03-12 | 江苏和顺环保股份有限公司 | 一种烟气净化处理系统 |
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Patent Citations (6)
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US20050013757A1 (en) * | 2003-07-16 | 2005-01-20 | Franz Windschmitt | Method and system for removing sulfur and dust from waste gases, particularly refinery waste gases |
CN101476730A (zh) * | 2009-01-13 | 2009-07-08 | 王惠生 | 一种节能经济型垃圾及危废物焚烧处理方法 |
CN101822942A (zh) * | 2010-05-26 | 2010-09-08 | 刘阳生 | 一种固体废物焚烧烟气中二噁英、重金属湿法净化方法 |
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