CN2581056Y - 循环流化床烟气脱硫装置 - Google Patents
循环流化床烟气脱硫装置 Download PDFInfo
- Publication number
- CN2581056Y CN2581056Y CN 02285755 CN02285755U CN2581056Y CN 2581056 Y CN2581056 Y CN 2581056Y CN 02285755 CN02285755 CN 02285755 CN 02285755 U CN02285755 U CN 02285755U CN 2581056 Y CN2581056 Y CN 2581056Y
- Authority
- CN
- China
- Prior art keywords
- desulfurizing tower
- humidifying
- desulfurizing
- deduster
- fluidized bed
- Prior art date
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- 230000003009 desulfurizing Effects 0.000 title claims abstract description 93
- 230000004087 circulation Effects 0.000 title abstract description 10
- 239000000779 smoke Substances 0.000 title description 4
- 239000003546 flue gases Substances 0.000 claims abstract description 35
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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[O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 32
- 239000011901 water Substances 0.000 claims abstract description 25
- 239000002956 ash Substances 0.000 claims abstract description 21
- 239000000463 materials Substances 0.000 claims abstract description 21
- 238000009826 distribution Methods 0.000 claims abstract description 19
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims abstract description 13
- 235000015450 Tilia cordata Nutrition 0.000 claims abstract description 13
- 235000011941 Tilia x europaea Nutrition 0.000 claims abstract description 13
- 239000004571 lime Substances 0.000 claims abstract description 13
- 238000005507 spraying Methods 0.000 claims abstract description 8
- 239000003570 air Substances 0.000 claims description 29
- 239000007787 solids Substances 0.000 claims description 14
- 238000000889 atomisation Methods 0.000 claims description 10
- 238000006477 desulfuration reactions Methods 0.000 abstract description 33
- 238000007599 discharging Methods 0.000 abstract description 2
- 239000000428 dust Substances 0.000 abstract 4
- 230000032798 delamination Effects 0.000 abstract 2
- 239000003795 chemical substances by application Substances 0.000 description 18
- 238000006243 chemical reactions Methods 0.000 description 13
- 238000005516 engineering processes Methods 0.000 description 11
- 238000000926 separation method Methods 0.000 description 9
- 239000002245 particles Substances 0.000 description 7
- 239000007921 sprays Substances 0.000 description 7
- 239000011575 calcium Substances 0.000 description 6
- 238000000034 methods Methods 0.000 description 6
- 238000000746 purification Methods 0.000 description 5
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- 239000000292 calcium oxide Substances 0.000 description 4
- 229910000118 calcium oxide Inorganic materials 0.000 description 4
- 235000012255 calcium oxide Nutrition 0.000 description 4
- 230000003134 recirculating Effects 0.000 description 4
- AXCZMVOFGPJBDE-UHFFFAOYSA-L Calcium hydroxide Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 3
- 239000000920 calcium hydroxide Substances 0.000 description 3
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000007789 gases Substances 0.000 description 3
- 239000007788 liquids Substances 0.000 description 3
- 229910001890 sulfur dioxide Inorganic materials 0.000 description 3
- RAHZWNYVWXNFOC-UHFFFAOYSA-N sulphur dioxide Chemical compound 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- 239000002351 wastewater Substances 0.000 description 3
- JGIATAMCQXIDNZ-UHFFFAOYSA-N Calcium sulfide Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 [Ca]=S JGIATAMCQXIDNZ-UHFFFAOYSA-N 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N calcium Chemical compound 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- 238000005457 optimization Methods 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 238000001694 spray drying Methods 0.000 description 2
- 235000002918 Fraxinus excelsior Nutrition 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound 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[S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 238000009692 water atomization Methods 0.000 description 1
Abstract
一种循环流化床烟气脱硫装置，主要由石灰消化增湿装置2、给料装置3、布风板4、脱硫塔30、一级惯性分离器7、二级旋风分离器8、分层给水喷雾装置6、除尘器10以及返料器9组成。石灰消化增湿装置2通过给料装置3与脱硫塔30相联，在脱硫塔30下部布置有分层喷水雾化增湿装置6。在脱硫塔30的上部有惯性分离器7。惯性分离器7和除尘器10之间有旋风分离器8，除尘器10的出口经管路与引风机12连接。除尘器10下部装有灰料输送装置11和中间灰仓14及机械排灰装置15。脱硫塔下部安装文丘里布风板4和风室18。风室18与除尘器10之间装有烟气旁通管道19。本实用新型循环流化床烟气脱硫装置，结构紧凑，运行可靠，使用寿命长，一次性投资低，脱硫效率高。
Description
技术领域
本实用新型涉及烟气净化装置，尤其是一种循环流化床烟气脱硫净化装置。
本实用新型所述的循环流化床烟气脱硫装置是一种半干法脱硫装置，包括石灰消化预增湿装置、给料装置、脱硫塔、分层喷水雾化增湿装置、除尘器以及返料器。石灰消化预增湿装置通过给料装置与脱硫塔相连。脱硫塔内的下部区域沿高度方向安装有分层喷水雾化增湿装置，即分层雾化喷嘴。在脱硫塔的上部出口处安装有气固惯性分离器，气固惯性分离器再经过旋风分离器和除尘器连接，两级分离器通过一个共同的返料器与脱硫塔连通。除尘器的出口经管路与引风机连接。
脱硫塔下部安装有文丘里布风板。文丘里布风板为由多个文丘里喷管排列的布风孔板。文丘里布风板的下部为风室。风室与除尘器之间装有烟气旁通管道。
除尘器下部装有灰料输送装置和中间灰仓。中间灰仓下部设有机械排灰装置。
脱硫塔还装有水箱和雾化风机。
采用石灰消化预增湿装置，可使进入脱硫塔的消石灰预增湿到含水量5％～30％。
传统的气固分离技术一般采用一级旋风分离器，单级旋风分离器分离效率不高，影响脱硫剂的循环利用率，进而影响脱硫效率。只有保证脱硫灰与烟气有效分离并回送到脱硫塔内，对脱硫剂进行多次循环利用，才能在较低钙硫比的条件下，保证比较高的脱硫效率。本实用新型循环流化床烟气半干法脱硫装置采用先进的两级分离与循环技术，经一、二级分离器分离出的固体脱硫灰统一由回料装置送回到脱硫塔内进行再循环，在脱硫塔内新脱硫剂及脱硫循环灰与烟气充分混合有效接触，进一步与烟气中的二氧化硫反应，提高钙的利用率。脱硫灰的循环增加了脱硫塔中的脱硫剂质量浓度，提高了脱硫剂与烟气反应的接触面积，增大了反应机率，从而提高了脱硫效率。脱硫灰的循环次数越多，脱硫剂的利用率就越高，相应的脱硫效率越高、钙利用率越高、钙硫比越低。
本实用新型在脱离塔内采用不同分离方式的两级分离系统，并且两级分离的回料通过一个共同的返料器返回到脱硫塔内。在脱硫反应塔上部出口附近布置有惯性分离器，该气固惯性分离器既可以为槽型，也可以为纵向百叶窗型惯性分离器。在其尾部出口附近布置有旋风分离器，该旋风分离器既可以为轴流式旋风分离器，也可以是切向式旋风分离器。优点是：(1)在保证很高的总的分离效率的前提下，可以适当地调配各级的分离效率，使整个分离系统与灰循环系统达到优化；(2)在保证系统总分离效率的前提下，尽可能地降低系统阻力，达到引风机负压最小的优化。
本实用新型脱硫塔反应内的两级分离与除尘器相结合就构成了脱硫灰的三重外循环特征。除尘器既可以是静电除尘器，也可以是袋式除尘器。前两重循环分别由一级惯性分离器和二级旋风分离器组成，第三重循环则由除尘器组成。以两级气固分离来计算，若第一级分离效率为η1，第二级分离效率为η2，则总分离效率η＝η1+(1-η1)η2，若第一、二级分离效率分别为80％、90％，则两级总的分离效率可达98％；若两级的分离效率分别为70％、80％，则两级总分离效率仍然高达94％。前两级分离的外循环再加上除尘器第三级分离的外循环，假设除尘器的分离效率为99.5％，则三级外循环总的分离效率可高达99.99％以上，从而保证了脱硫塔内较高的脱硫剂浓度。而采用单级分离器则很难达到这样高的分离效率。
本实用新型的脱硫塔采用了沿脱硫塔高度方向上分层喷水技术，即于其下部沿高度方向上布置有多层给水雾化喷嘴，增湿水沿着脱硫塔高度方向上分成多层喷入，从而大大降低了脱硫反应塔内局部烟气的含湿率，大大降低了粘壁结垢的几率，提高了烟气平均温度，增强了化学反应速度，延长了液相脱硫反应时间，有效地提高了脱硫效率。在实际设计中，可根据实际需要设计成3～7层喷水。根据对循环流化床脱硫机理的研究，含湿颗粒的蒸发时间主要是受颗粒内部水分的控制，而脱离效率主要是受颗粒外部水分存在时间的控制，所以采用分层喷水可以大大延长颗粒的外部水分的存在时间，从而大大提高系统的脱硫效率。
本实用新型采用了采用喷水而不是喷浆技术，这样使系统大大简化，运行可靠性大大提高：(1)减少了制浆设备；(2)大大降低了管道、喷嘴和泵的磨损；(3)取消了价格昂贵的泥浆泵。
本实用新型采用了气流式雾化喷嘴。采用该喷嘴的好处是：(1)雾化效果好，液滴粒径均匀性好；(2)雾化质量基本不受水压的影响。当喷水量变化时，空气量可以保持不变或适当调节，从而有效的防止雾化质量变差；(3)结构简单、检修维护方便。
本实用新型采用了石灰消化预增湿装置，使进入脱硫塔的消石灰预增湿到含水量5％～30％(质量百分比)。石灰消化预增湿装置即可为机械预增湿装置，也可以为流化床式预增湿装置。众所周知，SO2与CaO的反应主要是在液态离子反应条件下进行的，所以干态生石灰的脱硫效率很低，只有20％～30％。而采用预增湿之后，CaO不但与水反应生成Ca(OH)2，而且还有一部分多余的水分保留在Ca(OH)2颗粒的内部以及表面。Ca(OH)2颗粒的内部水分接近饱和，再加上喷水增湿之后，Ca(OH)2颗粒的表面很容易形成液膜，从而形成液滴颗粒。与干态脱硫剂脱硫塔内增湿相比，缩短了颗粒增湿时间，延长了脱硫反应时间，提高了反应速度，从而大大提高脱硫效率。经过预增湿后的脱硫剂，通过给料装置输送进入脱硫反应塔。
本实用新型在流化床反应器下部采用了文丘里布风装置，该装置为由多个文丘里喷管按照一定排列方式组成的布风孔板。文丘里流化布风板是一种特殊设计的布风板，其流通截面的形状为文丘里缩放喷管。文丘里喷管的排列方式有很多种，既可以是方形排列，也可以是三角形排列，其具体的排列方式由具体的设计决定。采用文丘里喷管的好处是，在比较高的风速情况下，可以保持相对比较低的阻力。同时采用了文丘里布风板结构，能使气流分布更加均匀，有效地降低了粘壁现象的发生，提高了脱硫效率。采用文丘里结构可在保证相同的气流速度的前提下，大大降低布风板的阻力，从而可以减小风机的压头。同时在反应塔下部还设计了文丘里加速扩展段，其目的是：(1)使气流在整个容器内达到合理分布；(2)脱硫剂在文丘里扩展段加入，而气流在文丘里扩展段扩展，此时在边壁处产生回流，强化了气流与脱硫剂之间的湍流混合，使烟气中的SO2与脱硫剂的混合更加均匀，大大提高了脱硫效率。
附图说明
图1为本实用新型循环流化床烟气脱硫装置构造图；图2为文丘里布风板的结构图；图3为机械预增湿装置结构简图。
图中，1为脱硫剂料斗，2为石灰消化预增湿装置，3为给料装置，4为文丘里布风板，5为扩散段，6为分层喷水雾化增湿装置，7为槽型气固惯性分离器，8为轴流式旋风分离器，9为返料器，10为袋式除尘器，11为灰料输送装置，12为引风机，13为风机，14为中间灰仓，15为机械排灰装置，16为雾化风机，17为水箱，18为风室，19为烟气旁通管道，20为烟囱，21为填充材料，22为文丘里喷管，23为电动机，24为进料口，25为喷淋装置，26为给水管道，27为出料口，28为搅拌叶片，29为主传动轴，30为脱硫塔。
Claims (5)
1.一种循环流化床烟气脱硫装置，其特征在于：该装置包括石灰消化预增湿装置、给料装置、脱硫塔、分层喷水雾化增湿装置、除尘器以及返料器；石灰消化预增湿装置通过给料装置与脱硫塔相连；脱硫塔内的下部区域沿高度方向安装有分层喷水雾化增湿装置，即分层雾化喷嘴；在脱硫塔的上部出口处安装有气固惯性分离器，气固惯性分离器和除尘器之间装有旋风分离器，两级分离器通过一个共同的返料器与脱硫塔连通；除尘器的出口经管路与引风机连接；除尘器下部装有灰料输送装置和中间灰仓；中间灰仓下部设有机械排灰装置；脱硫塔下部安装有文丘里布风板，脱硫塔文丘里布风板的下部为风室；风室与除尘器之间装有烟气旁通管道；脱硫塔还装有水箱和雾化风机。
2.按照权利要求1所述的循环流化床脱硫装置，其特征在于：文丘里布风板为由多个文丘里喷管排列的布风孔板。
3.按照权利要求1所述的循环流化床脱硫装置，其特征在于：石灰消化预增湿装置为机械预增湿装置；给料装置为螺旋机械输送装置。
4.按照权利要求1所述的循环流化床脱硫装置，其特征在于：除尘器为袋式除尘器。
5.按照权利要求1所述的循环流化床脱硫装置，其特征在于：灰料输送装置为空气输送斜槽。
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| CN100434146C (zh) * | 2006-04-11 | 2008-11-19 | 中国科学院过程工程研究所 | 一种干式内外双循环流化床脱硫装置及其脱硫方法 |
| CN100464825C (zh) * | 2006-12-27 | 2009-03-04 | 吉林安洁环保有限公司 | 双回料循环流化床半干法脱硫工艺 |
| WO2010139168A1 (zh) * | 2009-06-03 | 2010-12-09 | 江苏博际环保工程有限公司 | 一种消化循环流化床烟气脱硫方法及装置 |
| CN101559321B (zh) * | 2009-05-15 | 2011-06-15 | 武汉凯迪电力环保有限公司 | 循环流化床烟气脱硫系统的物料循环装置 |
| CN101284207B (zh) * | 2008-05-29 | 2011-08-17 | 东北电力大学 | 一种循环流化床烟气脱硫塔 |
| CN101224387B (zh) * | 2007-10-23 | 2011-08-31 | 张治忠 | 一种循环流化床烟气脱硫工艺及其脱硫装置 |
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| CN100464825C (zh) * | 2006-12-27 | 2009-03-04 | 吉林安洁环保有限公司 | 双回料循环流化床半干法脱硫工艺 |
| CN101224387B (zh) * | 2007-10-23 | 2011-08-31 | 张治忠 | 一种循环流化床烟气脱硫工艺及其脱硫装置 |
| CN101284207B (zh) * | 2008-05-29 | 2011-08-17 | 东北电力大学 | 一种循环流化床烟气脱硫塔 |
| CN101559321B (zh) * | 2009-05-15 | 2011-06-15 | 武汉凯迪电力环保有限公司 | 循环流化床烟气脱硫系统的物料循环装置 |
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| CN102716635A (zh) * | 2012-06-12 | 2012-10-10 | 清华大学 | 一种同时脱除烟气中重金属和细颗粒物的方法及系统 |
| CN103721484A (zh) * | 2012-10-15 | 2014-04-16 | 北京博朗环境工程技术股份有限公司 | 同轴短程快速循环协同脱除多种污染物的半干法烟气净化技术 |
| CN103691302A (zh) * | 2013-12-31 | 2014-04-02 | 吕宜德 | 一种干法脱硫装置及脱硫方法 |
| CN107233793A (zh) * | 2016-03-29 | 2017-10-10 | 沈阳铝镁设计研究院有限公司 | 一种电解铝烟气脱硫装置及脱硫方法 |
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