CN1544127A - 二级脱硫除尘装置 - Google Patents
二级脱硫除尘装置 Download PDFInfo
- Publication number
- CN1544127A CN1544127A CNA2003101069595A CN200310106959A CN1544127A CN 1544127 A CN1544127 A CN 1544127A CN A2003101069595 A CNA2003101069595 A CN A2003101069595A CN 200310106959 A CN200310106959 A CN 200310106959A CN 1544127 A CN1544127 A CN 1544127A
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- 230000003009 desulfurizing Effects 0.000 title abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,PD94bWwgdmVyc2lvbj0nMS4wJyBlbmNvZGluZz0naXNvLTg4NTktMSc/Pgo8c3ZnIHZlcnNpb249JzEuMScgYmFzZVByb2ZpbGU9J2Z1bGwnCiAgICAgICAgICAgICAgeG1sbnM9J2h0dHA6Ly93d3cudzMub3JnLzIwMDAvc3ZnJwogICAgICAgICAgICAgICAgICAgICAgeG1sbnM6cmRraXQ9J2h0dHA6Ly93d3cucmRraXQub3JnL3htbCcKICAgICAgICAgICAgICAgICAgICAgIHhtbG5zOnhsaW5rPSdodHRwOi8vd3d3LnczLm9yZy8xOTk5L3hsaW5rJwogICAgICAgICAgICAgICAgICB4bWw6c3BhY2U9J3ByZXNlcnZlJwp3aWR0aD0nMzAwcHgnIGhlaWdodD0nMzAwcHgnIHZpZXdCb3g9JzAgMCAzMDAgMzAwJz4KPCEtLSBFTkQgT0YgSEVBREVSIC0tPgo8cmVjdCBzdHlsZT0nb3BhY2l0eToxLjA7ZmlsbDojRkZGRkZGO3N0cm9rZTpub25lJyB3aWR0aD0nMzAwLjAnIGhlaWdodD0nMzAwLjAnIHg9JzAuMCcgeT0nMC4wJz4gPC9yZWN0Pgo8dGV4dCB4PScxMDAuNScgeT0nMTcwLjAnIGNsYXNzPSdhdG9tLTAnIHN0eWxlPSdmb250LXNpemU6NDBweDtmb250LXN0eWxlOm5vcm1hbDtmb250LXdlaWdodDpub3JtYWw7ZmlsbC1vcGFjaXR5OjE7c3Ryb2tlOm5vbmU7Zm9udC1mYW1pbHk6c2Fucy1zZXJpZjt0ZXh0LWFuY2hvcjpzdGFydDtmaWxsOiNFODQyMzUnID5IPC90ZXh0Pgo8dGV4dCB4PScxMjYuMScgeT0nMTg2LjAnIGNsYXNzPSdhdG9tLTAnIHN0eWxlPSdmb250LXNpemU6MjZweDtmb250LXN0eWxlOm5vcm1hbDtmb250LXdlaWdodDpub3JtYWw7ZmlsbC1vcGFjaXR5OjE7c3Ryb2tlOm5vbmU7Zm9udC1mYW1pbHk6c2Fucy1zZXJpZjt0ZXh0LWFuY2hvcjpzdGFydDtmaWxsOiNFODQyMzUnID4yPC90ZXh0Pgo8dGV4dCB4PScxMzguMCcgeT0nMTcwLjAnIGNsYXNzPSdhdG9tLTAnIHN0eWxlPSdmb250LXNpemU6NDBweDtmb250LXN0eWxlOm5vcm1hbDtmb250LXdlaWdodDpub3JtYWw7ZmlsbC1vcGFjaXR5OjE7c3Ryb2tlOm5vbmU7Zm9udC1mYW1pbHk6c2Fucy1zZXJpZjt0ZXh0LWFuY2hvcjpzdGFydDtmaWxsOiNFODQyMzUnID5PPC90ZXh0Pgo8L3N2Zz4K data:image/svg+xml;base64,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 O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 8
- 239000003513 alkali Substances 0.000 claims description 19
- 239000000428 dust Substances 0.000 claims description 10
- 238000000605 extraction Methods 0.000 claims description 7
- 240000007594 Oryza sativa Species 0.000 claims description 2
- 235000007164 Oryza sativa Nutrition 0.000 claims description 2
- NTHWMYGWWRZVTN-UHFFFAOYSA-N Sodium silicate Chemical compound 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[Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 claims description 2
- 239000011248 coating agent Substances 0.000 claims description 2
- 238000000576 coating method Methods 0.000 claims description 2
- 230000000875 corresponding Effects 0.000 claims description 2
- 235000019353 potassium silicate Nutrition 0.000 claims description 2
- 239000000843 powder Substances 0.000 claims description 2
- 235000009566 rice Nutrition 0.000 claims description 2
- 238000006477 desulfuration reaction Methods 0.000 abstract description 9
- 230000000694 effects Effects 0.000 abstract description 9
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- 235000011121 sodium hydroxide Nutrition 0.000 abstract description 6
- 238000004140 cleaning Methods 0.000 abstract description 2
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- 239000007921 spray Substances 0.000 abstract description 2
- 239000003517 fume Substances 0.000 abstract 3
- 239000007789 gas Substances 0.000 abstract 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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[O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 16
- 239000003546 flue gas Substances 0.000 description 16
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L Calcium sulfate Chemical compound 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[Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L calcium carbonate Chemical compound 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[Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
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- 239000007788 liquid Substances 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N sulphur dioxide Chemical compound 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O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 229960003563 Calcium Carbonate Drugs 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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Abstract
本发明是一种二级脱硫除尘装置。它包括壳体和碱液循环系统，其特征在于它由自下而上依次安装的低阻喷头，低速文丘里管，撞击挡板和环形排列的折流板除雾器组成。本发明的有益效果是：二级脱硫循环中，采用低速文丘里+撞击挡板板结构，使得气阻力低，脱硫效率高，并起到了一级脱水的作用，而脱硫塔上部的低阻除雾器能彻底除掉烟气中细小水滴，保证烟气不带水。该结构改变了传统除雾器平面布置的方式，改为单元式结构，在单位面积上增加脱水折板的周长，便于安装、检修更为方便，由于折流板竖直安装脱水更为彻底，避免了烟气二次夹带，比平面安装允许流速更高，设备更紧凑，节省了空间。
Description
技术领域
本发明涉及锅炉脱硫除尘技术，特别是一种二级脱硫除尘装置。
背景技术
中小型电厂和大中型工业锅炉烟气脱硫除尘，关系到区域内空气质量和环境保护，与人民群众的健康紧密相关。在该领域现有技术中经常使用单独的除尘器，或烟气除尘与脱硫共用的除尘器，这类除尘器对烟尘颗粒物的清除具有较好的效果，但是对脱硫效果不佳。特别是在除尘与脱硫合一工作中，常常出现结垢现象。在加碱运行时，由于设备内部填料和装置空间较小，抗结垢能力差，脱硫液体在高温烟气作用下，产生硫酸钙和碳酸钙结晶堵塞设备，造成设备不能正常运行；另外由于没有专门的烟气除雾装置，造成风机带水，不能有效去除烟气中的液滴。
发明内容
本发明的目的是为了克服现有技术的不足，而提供一种二级脱硫除尘装置，该装置通过设置文丘里管、撞击档板和折流板除雾器以及碱液循环系统，实现提高除尘效率，增加脱硫除雾功能。
本发明为解决上述问题所采用的方案是设计一种二级脱硫除尘装置。它包括壳体和碱液循环系统，其特征在于它由自下而上依次安装的喷头，文丘里管，撞击档板和环形排列的折流板除雾器组成。
本发明的有益效果是：二级脱硫循环中，采用低速文丘里+撞击挡板结构，使得气阻力低，脱硫效率高，并起到了一级脱水的作用，而脱硫塔上部的低阻除雾器能彻底除掉烟气中细小水滴，保证烟气不带水。该结构改变了传统除雾器平面布置的方式，改为单元式结构，在单位面积上增加脱水折板的周长，便于安装、检修更为方便，由于折流板竖直安装脱水更为彻底，避免了烟气二次夹带，比平面安装允许流速更高，设备更紧凑，节省了空间。
以下将结合本发明的实施例参照附图进行详细叙述。
附图说明
图1二级脱硫除尘装置示意图；图2文丘里管及撞击档板示意图；图3除雾器剖视图；图4除雾器主视图。
具体实施方式
本发明的二级脱硫除尘装置，包括壳体和碱液循环系统。它的壳体是一个上、下为敞开式的罐体。
在罐体内靠下部固定有一个支撑隔板4，板上设有多个圆孔，每个孔上对应固定一个流速为每秒15-20米的低速文丘里管2，而在每个低速文丘里管的上方，固定一个导流撞击档板3。支撑隔板下方对应低速文丘里管位置设有与碱液管相通的喷头1，该喷头则是要求其阻力降在2米水柱以内的低阻喷头。支撑隔板表面还涂敷有一层由水玻璃与铸石粉组成的涂层9。
在罐体内靠上部还固定有一个安装板5，板上也设有多个圆孔，每个孔上方对应固定一个除雾器6。除雾器设有环形排列着折流板10，环形折流板顶部为封闭的。
在该装置的碱液循环系统中，碱液由碱箱经碱泵碱液管7和泵入低阻喷头，喷入低速文丘里管，碱液经撞击档板除下的液体由排液口8流回碱箱，碱箱中的烟尘和生成物的沉渣由排渣管排入沉降池。
本发明的工作原理是：烟气从罐体下口进入低速文丘里管，与从低阻喷头喷出的碱液混合向上流动，在撞击档板的作用下转向流动，在此过程中烟气与碱液充分接触，二氧化硫被碱液吸收，烟气中的微尘得到进一步净化并强化了脱硫除尘效果，起到一次脱水的作用。经撞击挡板后烟气上行，烟气中的液滴会聚于隔板上，由排液口流回碱池。由于烟气中含尘量少，故生成物纯度高，便于回收利用。而支撑隔板则将除尘循环和脱硫循环分隔。脱硫后的烟气向上流动进入除雾器后改变流向，从水平方向流出，烟气中的液滴通过折流板被捕集，沿折板垂直流下汇集，而净化后的空气从罐体上口排出。
Claims (8)
1 一种二级脱硫除尘装置，包括壳体和碱液循环系统，其特征在于它由自下而上依次安装的喷头，文丘里管，撞击档板和环形排列的折流板除雾器组成。
2 按照权利要求1所述的除尘装置，其特征在于所说的壳体是一个上、下为敞开式的罐体。
3 按照权利要求1或2所述的除尘装置，其特征在于所说的罐体内靠下部固定有一个支撑隔板，板上设有多个圆孔，每个孔上对应固定一个文丘里管，而在每个文丘里管的上方，固定一个导流撞击档板；所说的支撑隔板下对应文丘里管位置设有与碱液管相通的喷头。
4 按照权利要求3所述的除尘装置，其特征在于所说的文丘里管是流速为每秒15-20米的低速文丘里管。
5 按照权利要求3所述的除尘装置，其特征在于所说的喷头是阻力降在2米水柱以内的低阻喷头。
6 按照权利要求3、4或5所述的除尘装置，其特征在于支撑隔板表面涂敷有一层由水玻璃与铸石粉组成的涂层。
7 按照权利要求1或6所述的除尘装置，其特征在于所说的罐体内靠上部还固定有一个安装板，板上也设有多个圆孔，每个孔上对应固定一个除雾器。
8 按照权利要求7所述的除尘装置，其特征在于所说的除雾器设有环形排列着折流板，环形折流板顶部为封闭的。
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104307345A (zh) * | 2014-11-19 | 2015-01-28 | 广西南宁华国环境科技有限公司 | 一种煤烟脱硫除尘器 |
| CN104667677A (zh) * | 2015-02-11 | 2015-06-03 | 中国核电工程有限公司 | 文丘里水洗过滤装置 |
| CN106000045A (zh) * | 2016-06-17 | 2016-10-12 | 王骞 | 锅炉烟气深度除尘脱硫脱硝设备 |
| CN106823742A (zh) * | 2017-02-16 | 2017-06-13 | 上海蓝科石化环保科技股份有限公司 | 一种双循环脱硫除尘装置及烟气的脱硫除尘方法 |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104307345A (zh) * | 2014-11-19 | 2015-01-28 | 广西南宁华国环境科技有限公司 | 一种煤烟脱硫除尘器 |
| CN104307345B (zh) * | 2014-11-19 | 2016-05-04 | 广西南宁华国环境科技有限公司 | 一种煤烟脱硫除尘器 |
| CN104667677A (zh) * | 2015-02-11 | 2015-06-03 | 中国核电工程有限公司 | 文丘里水洗过滤装置 |
| CN106000045A (zh) * | 2016-06-17 | 2016-10-12 | 王骞 | 锅炉烟气深度除尘脱硫脱硝设备 |
| CN106000045B (zh) * | 2016-06-17 | 2019-04-16 | 王骞 | 锅炉烟气深度除尘脱硫脱硝设备 |
| CN106823742A (zh) * | 2017-02-16 | 2017-06-13 | 上海蓝科石化环保科技股份有限公司 | 一种双循环脱硫除尘装置及烟气的脱硫除尘方法 |
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