CN201978663U - 工业烟气卧式脱硫反应器 - Google Patents
工业烟气卧式脱硫反应器 Download PDFInfo
- Publication number
- CN201978663U CN201978663U CN2011200599804U CN201120059980U CN201978663U CN 201978663 U CN201978663 U CN 201978663U CN 2011200599804 U CN2011200599804 U CN 2011200599804U CN 201120059980 U CN201120059980 U CN 201120059980U CN 201978663 U CN201978663 U CN 201978663U
- Authority
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- China
- Prior art keywords
- flue gas
- reactor
- pipe
- cavity
- desulfuration
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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[O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 20
- 239000003546 flue gas Substances 0.000 title claims abstract description 20
- 238000006477 desulfuration reaction Methods 0.000 title claims abstract description 15
- 239000003513 alkali Substances 0.000 claims abstract description 11
- 239000007789 gas Substances 0.000 claims abstract description 10
- 238000006243 chemical reaction Methods 0.000 claims description 13
- 230000003009 desulfurizing Effects 0.000 claims description 12
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Abstract
本实用新型公开了一种工业烟气卧式脱硫反应器，包括一水平卧置的管体，该管体中有一分布孔板将管体内腔分为上下两个空腔，其中上空腔为脱硫液分布室，下空腔为脱硫反应室，管体的顶部有碱液进口，用于向脱硫液分布室输入脱硫液，管体的两端一端有烟气进口，另一端有烟气出口，烟气从烟气进口进入脱硫反应室与碱液垂直交叉相遇进行脱硫反应。本实用新型结构简单，气液在反应室内垂直交叉接触，脱硫效果好，烟气与碱液非逆流运行，反应室内烟气运行方向无任何导流板，系统阻力小，电能耗低，可长期持续高效运行。
Description
工业烟气卧式脱硫反应器
技术领域
[0001] 本实用新型涉及一种工业烟气脱硫装置。 背景技术
[0002] 传统脱硫设备是竖立的脱硫反应塔，塔内设置有多层旋流分布板，将碱液用泵打至塔内上部，从旋流板上依次流下，烟气从塔底部入口进入塔内，逆流而上，与脱硫液充分接触，发生脱硫反应，脱硫后渣溶液从塔底流入沉淀池。
[0003] 传统旋流板式脱硫塔，从理论上说，塔内气液逆向运行，充分接触，脱硫效果好，但因塔内设置有多层旋流板，且烟气逆流而上，气流阻力系数非常大，系统运行电能耗高，且旋流板上易结垢，生产期无法入内清理，结到一定程度后，会完全堵塞旋流板，造成整个系统瘫痪，无法继续生产。
实用新型内容
[0004] 本实用新型的目的在于提供一种脱硫效果好，系统阻力小，可长期持续高效运行的工业烟气脱硫反应器。
[0005] 本实用新型提供的这种工业烟气卧式脱硫反应器，包括一水平卧置的管体，该管体中有一分布孔板将管体内腔分为上下两个空腔，其中上空腔为脱硫液分布室，下空腔为脱硫反应室，管体的顶部有碱液进口，用于向脱硫液分布室输入脱硫液，管体的两端一端有烟气进口，另一端有烟气出口，烟气从烟气进口进入脱硫反应室与碱液垂直交叉相遇进行脱硫反应。
[0006] 所述孔板的孔径大小为5_50mm。
[0007] 本实用新型结构简单，气液在反应室内垂直交叉接触，脱硫效果好，烟气与碱液非逆流运行，反应室内烟气运行方向无任何导流板，系统阻力小，电能耗低，可长期持续高效运行，减少维修成本。
附图说明
[0008] 图1是本实用新型的结构示意图。 具体实施方式
[0009] 从图1可以看出本实用新型具有管体1，该管体水平卧置，其一端开口是烟气进口 6，另一端开口是烟气出口 7。在管体1中有一水平布置的分布孔板2，将管体1的内腔分为上下两个空腔，上空腔是脱硫液分布室3，下空腔是脱硫反应室4，在管体1的顶部设有进液口 5，碱液通过水泵进液口 5打入脱硫分布室3。用这种工业烟气脱硫反应器进行烟气处理的方法是：烟气从烟气进口 6水平进入管体1的脱硫反应室4中，脱硫分布室3的碱液通过分布孔板不断向下喷射，与烟气垂直交叉撞击，与烟气进行充分地脱硫反应，同时烟气中的尘土被液洗落，烟气得到净化，从烟囱排到空气中。反应后渣液落到脱硫反应室的底部并流到烟囱下部的渣液池8中，从渣液池底部出口流入脱硫系统沉淀池。管体1和分布孔板 2材质为耐酸碱材质，管体1的外形大小、长度不限，根据要求设计，孔板分布器孔径大小为 5-50mm,数量不限，排列方式不限，材质也为耐酸碱质。
Claims (2)
1. 一种工业烟气卧式脱硫反应器，其特征在于该反应器包括一水平卧置的管体（1)， 该管体中有一分布孔板（2)将管体（1)内腔分为上下两个空腔，其中上空腔为脱硫液分布室（3)，下空腔为脱硫反应室（4)，管体的顶部有碱液进口（5)，用于向脱硫液分布室输入脱硫液，管体的两端一端有烟气进口（6)，另一端有烟气出口（7)，烟气从烟气进口进入脱硫反应室与碱液垂直交叉相遇进行脱硫反应。
2.根据权利要求1所述的工业烟气卧式脱硫反应器，其特征在于孔板（2)的孔径大小为 5-50mmo
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102179148A (zh) * | 2011-03-09 | 2011-09-14 | 娄底市兴华有色金属有限公司 | 工业烟气卧式脱硫反应器及烟气处理方法 |
| CN104069732A (zh) * | 2014-07-11 | 2014-10-01 | 北京科技大学 | 一种一体化卧式湿法脱硫装置 |
| CN104785042A (zh) * | 2015-05-05 | 2015-07-22 | 顾和根 | 一种多功能消烟除尘脱硫器 |
-
2011
- 2011-03-09 CN CN2011200599804U patent/CN201978663U/zh not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102179148A (zh) * | 2011-03-09 | 2011-09-14 | 娄底市兴华有色金属有限公司 | 工业烟气卧式脱硫反应器及烟气处理方法 |
| CN102179148B (zh) * | 2011-03-09 | 2012-10-03 | 娄底市兴华有色金属有限公司 | 工业烟气卧式脱硫反应器及烟气处理方法 |
| CN104069732A (zh) * | 2014-07-11 | 2014-10-01 | 北京科技大学 | 一种一体化卧式湿法脱硫装置 |
| CN104069732B (zh) * | 2014-07-11 | 2016-08-24 | 北京科技大学 | 一种一体化卧式湿法脱硫装置 |
| CN104785042A (zh) * | 2015-05-05 | 2015-07-22 | 顾和根 | 一种多功能消烟除尘脱硫器 |
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