CN203090739U - 一种脱硫吸收塔 - Google Patents
一种脱硫吸收塔 Download PDFInfo
- Publication number
- CN203090739U CN203090739U CN 201320115785 CN201320115785U CN203090739U CN 203090739 U CN203090739 U CN 203090739U CN 201320115785 CN201320115785 CN 201320115785 CN 201320115785 U CN201320115785 U CN 201320115785U CN 203090739 U CN203090739 U CN 203090739U
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- China
- Prior art keywords
- slurries
- layer
- tower
- absorption tower
- desulfurization
- 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.)
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- 238000006477 desulfuration reaction Methods 0.000 title claims abstract description 34
- 238000010521 absorption reaction Methods 0.000 title claims abstract description 29
- 230000003009 desulfurizing Effects 0.000 title abstract description 17
- 239000002002 slurry Substances 0.000 claims abstract description 111
- 239000007921 spray Substances 0.000 claims abstract description 25
- 239000000779 smoke Substances 0.000 claims abstract description 18
- 238000005507 spraying Methods 0.000 claims description 35
- 230000003647 oxidation Effects 0.000 claims description 10
- 238000007254 oxidation reaction Methods 0.000 claims description 10
- 241000282326 Felis catus Species 0.000 claims description 3
- 238000003756 stirring Methods 0.000 claims description 3
- 238000003912 environmental pollution Methods 0.000 abstract 1
- 239000003595 mist Substances 0.000 abstract 1
- 239000003546 flue gas Substances 0.000 description 26
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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[O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 25
- 239000007789 gas Substances 0.000 description 20
- 239000010440 gypsum Substances 0.000 description 4
- 229910052602 gypsum Inorganic materials 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000003245 coal Substances 0.000 description 3
- 239000000284 extract Substances 0.000 description 3
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L Calcium sulfate Chemical compound 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- 239000003344 environmental pollutant Substances 0.000 description 2
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- 238000010248 power generation Methods 0.000 description 2
- GBAOBIBJACZTNA-UHFFFAOYSA-L Calcium sulfite Chemical compound 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[Ca+2].[O-]S([O-])=O GBAOBIBJACZTNA-UHFFFAOYSA-L 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 235000010261 calcium sulphite Nutrition 0.000 description 1
- 230000000875 corresponding Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
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- 238000000746 purification Methods 0.000 description 1
- 230000001105 regulatory Effects 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound 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[S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
Abstract
本实用新型涉及一种脱硫吸收塔，包括吸收塔，所述吸收塔塔顶设有烟气出口，塔身设有烟气入口，塔底设有浆液池，所述烟气出口与烟气入口之间设有气体脱硫层，所述气体脱硫层设有浆液喷淋层和浆液喷淋层下方的浆液喷射层，所述浆液喷淋层的喷嘴向下设置，所述浆液喷射层的喷嘴向上设置。烟气经烟气入口进入，先经浆液喷射层接触脱硫，再与浆液喷淋层接触进一步脱硫，经喷淋层上方的除雾器除去雾滴后，烟气由烟气出口排出；本实用新型采用两种不同的喷淋方式对烟气进行脱硫处理，提高了烟气与浆液的接触面积和接触时间，并且提高了烟气与浆液的混合程度和吸收塔的液气比，提高了脱硫效率，降低了对环境的污染。
Description
一种脱硫吸收塔
技术领域
[0001] 本实用新型涉及烟气净化技术领域，具体涉及一种脱硫吸收塔。
背景技术
[0002] 燃煤发电是煤炭利用的主要途径之一，燃煤火电机组需排放大量污染物，其中SO2以及粉尘对环境的危害较为严重，也是需要重点控制的主要污染物。因而，需要在燃煤发电的烟气排放处设置脱硫系统。烟气脱硫技术包括湿法脱硫和干法脱硫等，其中湿法脱硫技术的运用最为广泛。湿法烟气脱硫吸收塔的原理是利用石灰石碱性浆液从上向下喷淋，烟气从下向上流动，石灰石浆液滴在下落过程中吸收烟气中的SO2，生成石膏等副产品，达到脱除烟气中的SO2的目的。但是烟气在脱硫塔中气流速度很快，气流量也很大，使得烟气与脱硫液体不能有效充分接触，降低了脱硫效率。
发明内容
[0003] 有鉴于此，本实用新型的目的是提供一种脱硫吸收塔，提高了烟气在吸收塔内与浆液的混合程度，从而提高了脱硫效率。
[0004] 本实用新型公开了一种脱硫吸收塔，包括吸收塔，所述吸收塔塔顶设有烟气出口，塔身设有烟气入口，塔底设有浆液池，所述烟气出口与烟气入口之间设有气体脱硫层，所述气体脱硫层设有浆液喷淋层和浆液喷淋层下方的浆液喷射层，所述浆液喷淋层的喷嘴向下设置，所述浆液喷射层的喷嘴向上设置。
[0005] 进一步，所述烟气出口与气体脱硫层之间设有除雾器。
[0006] 进一步，所述吸 收塔设有用于搅拌浆液的搅拌器。
[0007] 进一步，所述吸收塔设有氧化风机，所述氧化风机出口设有氧化气管插入浆液池中。
[0008] 进一步，所述浆液喷淋层至少为I层，所述浆液喷射层为I层或2层。
[0009] 进一步，所述吸收塔设有与浆液喷淋层层数相同的浆液喷淋循环泵，所述浆液喷淋循环泵入口与浆液池连通，浆液喷淋循环泵出口与浆液喷淋层入口连接。
[0010] 进一步，所述吸收塔设有与浆液喷射层层数相同的浆液喷射循环泵，所述浆液喷射循环泵入口与浆液池连通，浆液喷射循环泵出口与浆液喷射层入口连接。
[0011] 本实用新型的有益效果在于:本实用新型一种脱硫吸收塔，在气体脱硫层设置了向下喷淋的浆液喷淋层和向上喷射的浆液喷射层；烟气经烟气入口进入，先经浆液喷射层接触脱硫，再与浆液喷淋层接触进一步脱硫，最后烟气由烟气出口排出；本实用新型采用两种不同的喷淋方式对烟气进行脱硫处理，提高了烟气与浆液的接触面积和接触时间，并且提高了烟气与浆液的混合程度和吸收塔的液气比，提高了脱硫效率，降低了对环境的污染。
附图说明
[0012] 为了使实用新型的目的、技术方案和优点更加清楚，下面将结合附图对本实用新型作进一步的详细描述，其中:
[0013] 图1为本实用新型的结构示意图；
[0014] 图2为本实用新型的平面布置图。
具体实施方式
[0015] 下面将结合附图，对本实用新型的优选实施例进行详细的描述。
[0016] 如图所示，本实用新型的一种脱硫吸收塔，包括吸收塔1，所述吸收塔I塔顶设有烟气出口 4，塔身设有烟气入口 3，塔底设有浆液池2，浆液池2容积根据实际脱硫量调节相对应的大小；所述烟气出口 4与烟气入口 3之间设有气体脱硫层，所述气体脱硫层设有浆液喷淋层8和浆液喷淋层8下方的浆液喷射层6，，所述浆液喷淋层8的喷嘴向下设置，所述浆液喷射层6的喷嘴向上设置，从上、下两个方位喷射浆液，形成严密的反应区域，防止原烟气泄露，并且提高浆液与原烟气接触的面积和时间，使原烟气中的SO2充分得到反应吸收。
[0017] 本实施例中，所述烟气出口 4与气体脱硫层之间设有除雾器10，脱除得到的净烟气中的液滴，防止浆液中的石膏随净烟气排出而形成石膏雨。
[0018] 本实施例中，所述吸收塔I设有用于搅拌浆液的搅拌器12，防止浆液沉淀。
[0019] 本实施例中，所述吸收塔I设有氧化风机9，所述氧化风机9出口设有氧化气管11插入浆液池2中，空气进入浆液池2把浆液中的亚硫酸钙氧化成硫酸钙(石膏)，提高脱硫效率。
[0020] 本实施例中，所述浆液喷淋层8为I层，所述浆液喷射层6为2层。
[0021] 本实施例中，所·述吸收塔I设有与浆液喷淋层8层数相同的浆液喷淋循环泵7，即
I台浆液喷淋循环泵7，所述浆液喷淋循环泵7入口与浆液池2连通，浆液喷淋循环泵7从浆液池2中抽取浆液，浆液喷淋循环泵7出口与浆液喷淋层8入口连接，使浆液从喷嘴中喷出。
[0022] 本实施例中，所述吸收塔I设有与浆液喷射层6层数相同的浆液喷射循环泵5，即
2台浆液喷射循环泵5，所述浆液喷射循环泵5入口与浆液池2连通，浆液喷射循环泵5从浆液池2中抽取浆液，浆液喷射循环泵5出口与浆液喷射层6入口连接，使浆液从喷嘴中喷出。
[0023]启动各设备，浆液喷淋循环泵7和浆液喷射循环泵5从浆液池2内抽取浆液，经管道输送至浆液喷淋层8和浆液喷射层6 ;当原烟气从吸收塔烟气入口 3进入，并向上进入到气体脱硫层中，与气体脱硫层中喷嘴喷出来的浆液喷雾进行气体脱硫反应，原烟气中的SO2被吸收；最后经除雾器10脱除烟气中的液滴，得到净烟气通过烟气出口 4进入烟囱排入大气中。本实用新型采用两种不同的喷淋方式对烟气进行脱硫处理，提高了烟气与浆液的接触面积和接触时间，并且提高了烟气与浆液的混合程度和吸收塔的液气比，提高了脱硫效率，降低了对环境的污染。
[0024] 最后说明的是，以上实施例仅用以说明本实用新型的技术方案而非限制，尽管通过参照本实用新型的优选实施例已经对本实用新型进行了描述，但本领域的普通技术人员应当理解，可以在形式上和细节上对其作出各种各样的改变，而不偏离所附权利要求书所限定的本实用新型的精神和范围。
Claims (7)
1.一种脱硫吸收塔，其特征在于:包括吸收塔，所述吸收塔塔顶设有烟气出口，塔身设有烟气入口，塔底设有浆液池，所述烟气出口与烟气入口之间设有气体脱硫层，所述气体脱硫层设有浆液喷淋层和浆液喷淋层下方的浆液喷射层，所述浆液喷淋层的喷嘴向下设置，所述浆液喷射层的喷嘴向上设置。
2.根据权利要求1所述的一种脱硫吸收塔，其特征在于:所述烟气出口与气体脱硫层之间设有除雾器。
3.根据权利要求1所述的一种脱硫吸收塔，其特征在于:所述吸收塔设有用于搅拌浆液的搅拌器。
4.根据权利要求1所述的一种脱硫吸收塔，其特征在于:所述吸收塔设有氧化风机，所述氧化风机出口设有氧化气管插入浆液池中。
5.根据权利要求1至4任意一项所述的一种脱硫吸收塔，其特征在于:所述浆液喷淋层至少为I层，所述浆液喷射层为I层或2层。
6.根据权利要求5所述的一种脱硫吸收塔，其特征在于:所述吸收塔设有与浆液喷淋层层数相同的浆液喷淋循环泵，所述浆液喷淋循环泵入口与浆液池连通，浆液喷淋循环泵出口与浆液喷淋层入口连接。
7.根据权利要求5所述的一种脱硫吸收塔，其特征在于:所述吸收塔设有与浆液喷射层层数相同的浆液喷射循环泵，所述浆液喷射循环泵入口与浆液池连通，浆液喷射循环泵出口与浆液喷射层入口 连接。
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| CN104998535A (zh) * | 2014-04-22 | 2015-10-28 | 上海映特环保技术有限公司 | 一种双效烟气净化装置及其净化方法 |
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| CN103120894A (zh) * | 2013-03-14 | 2013-05-29 | 中电投远达环保工程有限公司 | 一种脱硫吸收塔 |
| CN104998535A (zh) * | 2014-04-22 | 2015-10-28 | 上海映特环保技术有限公司 | 一种双效烟气净化装置及其净化方法 |
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