CN202654927U - 旋流整流气液吸收塔 - Google Patents
旋流整流气液吸收塔 Download PDFInfo
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- CN202654927U CN202654927U CN 201220229978 CN201220229978U CN202654927U CN 202654927 U CN202654927 U CN 202654927U CN 201220229978 CN201220229978 CN 201220229978 CN 201220229978 U CN201220229978 U CN 201220229978U CN 202654927 U CN202654927 U CN 202654927U
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- gas
- absorption tower
- eddy flow
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- flow rectification
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- 239000007788 liquid Substances 0.000 title claims abstract description 33
- 239000002002 slurry Substances 0.000 claims abstract description 20
- 238000010521 absorption reaction Methods 0.000 claims description 63
- 238000005192 partition Methods 0.000 claims description 27
- 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 description 27
- 238000005507 spraying Methods 0.000 claims description 7
- 239000000779 smoke Substances 0.000 abstract description 5
- 238000006477 desulfuration reaction Methods 0.000 abstract description 4
- 230000003009 desulfurizing Effects 0.000 abstract description 3
- 239000000428 dust Substances 0.000 abstract description 3
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 238000000034 method Methods 0.000 abstract 2
- 239000007789 gas Substances 0.000 description 67
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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- 239000006028 limestone Substances 0.000 description 3
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L Calcium sulfate Chemical compound 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Abstract
本实用新型涉及一种旋流整流气液吸收塔，包含立式吸收塔，塔体设有气体进口管和气体出口管，吸收塔内部设置旋流整流隔板，该隔板由上、下开孔隔板及连接上下开孔隔板的多根倾斜气体导管组成。倾斜气体导管为一圈或多圈，其中任意一圈或多圈的倾斜气体导管的倾斜方向与其余不同。旋流整流隔板的数量可以是一个或多个，每个旋流整流隔板的上部或下部布置有浆液喷嘴组。本实用新型解决了吸收塔内部烟气分布不均、烟气停留时间短的问题，吸收效率高、除尘效率高、塔径小、能耗低、结构简单、适应性好、可靠性高，特别适用于烟气湿法脱硫工艺。
Description
旋流整流气液吸收塔
技术领域
[0001] 本实用新型涉及一种气液传质、传热设备，特别涉及一种高效的旋流整流气液吸收塔，适用于工业烟气净化吸收装置。
背景技术
[0002] 气液传质、传热设备，用来进行气液两相之间进行紧密接触，达到相间传质及传热的目的，可用作精馏、吸收、解吸和萃取等工作。在大气污染控制领域，工业烟气净化吸收装置广泛使用的石灰石/石灰-石膏湿法喷淋吸收塔，其吸收剂石灰石/石灰与烟气中的SO2反应生成亚硫酸钙和硫酸钙，在浆液中易产生饱和结晶，造成除雾器等设备的结垢堵塞，大大降低石灰石/石灰-石骨烟气湿法喷淋吸收塔的可用率。
[0003]目前广泛使用的喷淋吸收塔还有以下缺陷：
[0004] (I)喷淋吸收塔的吸收效率低。烟气通常从单侧进入，造成吸收塔内部烟气分布不均，各处的流速不同、液气比不同，气液传质效果差。另外，为了防止除雾器负荷过大、保证气液逆流吸收，通常采用雾滴粒径较大的浆液喷嘴，造成气液反应表面积小。
[0005] (2)能耗大、投资高、运行费用高。由于浆液喷嘴的雾滴粒径较大，只好采用较大的液气比，使得吸收塔的浆液循环泵流量大，相应的管道、喷嘴等增多增大。
[0006] 针对喷淋塔技术的缺陷，中国实用新型CN201115813Y “气动脱硫塔”提出在塔内设置由多个气动脱硫单元所并联成的组合段，进行高效率脱硫，有效克服了除尘负荷过重、液气比高的弊端。但该实用新型存在组合段内气液接触不佳、烟气停留时间短等不足。
实用新型内容
[0007] 本实用新型的目的在于克服现有喷淋塔技术的不足，提出一种高效、节能、可靠、适应性强的旋流整流气液吸收塔，解决了吸收塔内部烟气分布不均、烟气停留时间短而导致吸收效率低的问题。
[0008] 本实用新型旋流整流气液吸收塔，包含立式吸收塔,塔体设有气体进口管和气体出口管，吸收塔内部设置旋流整流隔板，该隔板由上、下开孔隔板及连接上下开孔隔板的多根倾斜气体导管组成。
[0009] 所述的立式吸收塔，其塔体截面可以是圆形或矩形，气体进口管或气体出口管可以是一根或多根。
[0010] 所述的旋流整流隔板包含一圈或多圈的倾斜气体导管，其中任意一圈或多圈的倾斜气体导管的倾斜方向与其余不同，典型的布置方式是每相邻的两圈倾斜气体导管倾斜方向相反，形成更优化的气体流动状况。倾斜气体导管的直径、数量和倾斜角度需要经过计算机多次模拟和优化才能确定。倾斜气体导管的长径比为O. 5〜2，倾斜角度(见附图6中α角）为30〜60°。
[0011] 所述的旋流整流隔板的数量可以是一个或多个，每个旋流整流隔板的上部或下部布置有浆液喷嘴组。[0012] 所述的浆液喷嘴组可以是布置于吸收塔内部的浆液喷淋层，也可以是布置于吸收塔竖直壁面上、进行水平或近似水平喷雾的喷嘴组。
[0013] 所述的立式吸收塔，其气体进口管和气体出口管的布置可以是气体进口管布置在下方、气体出口管布置在上方，也可以是气体进口管布置在上方、气体出口管布置在下方。
[0014] 本实用新型的有益效果是：
[0015] I、吸收效率高。（I)气体通过旋流整流隔板之后，完全消除了位于吸收塔侧面的气体进口管道形成的偏流，气体分布均匀，各处的液气比接近相同，提高了气液接触效果。(2)大直径气体导管既作为气体通道，又同时作为液体流动通道，并由于气体导管的倾斜放置，形成液幕，进一步增强了气液接触效果。（3)气体通过旋流整流隔板之后，气体形成旋流流场，吸收塔中部还可以同时形成相反的流动方向，延长了气体停留时间。（4)可利用多级的原理，布置多个旋流整流隔板，每个旋流整流隔板将前一级的气体重新混合、汇集后送入下 游，完全消除了气液接触死区，这种各级效率的叠加可实现很高的吸收效率。
[0016] 2、除尘效率高。气体通过旋流整流隔板时，流速可达15〜20m/s，形成强烈的湍流流动状态，使大量的烟尘得以除去。
[0017] 3、塔径小，投资费用低。本实用新型的吸收塔的空塔表观流速可达6m/s，而传统的喷淋塔最佳流速为3〜4m/s左右。较高的空塔表观流速可使吸收塔的直径减小，降低造价。
[0018] 4、能耗低。气体的旋流流动，延长了雾滴悬浮时间，提高了气液接触表面积，可在要求相同吸收效率的条件下，选用较小的液气比，每级可选为2至4L/Nm3，远低于传统湿法脱硫中每一层喷淋层的液气比，因此相应的浆液循环泵流量小，价格较低，消耗电能也少。
[0019] 5、结构简单，便于制作、安装。本实用新型不设精细、微小构件，可用不锈钢管和板材制作、安装。
[0020] 6、适应性好。由于形成了独特的气体流场，提高了气液传质、传热速率，可适应大范围变化的气体流量、不同的有害气体浓度，提高了运行操作弹性。
[0021] 7、可靠性高。（I)倾斜气体导管流通截面积较大，而且具有自冲洗作用，不易堵塞。
(2)旋流整流隔板将气体重新混合、汇集，完全消除了气液接触死区，个别喷嘴堵塞对吸收效率的影响很小。（3)由于气体导管的倾斜放置，上、下开孔隔板的开孔率较高，不易形成大面积的沉积。
[0022] 8、便于吸收塔防腐施工、检修等工作的进行。旋流整流隔板整体强度高，进行吸收塔的防腐施工、检修时，可以不用搭建脚手架。
附图说明
[0023] 图I是本实用新型实施例I的旋流整流气液吸收塔的结构示意图。
[0024] 图2是本实用新型实施例2的旋流整流气液吸收塔的结构示意图。
[0025] 图3是本实用新型实施例3的旋流整流气液吸收塔的结构示意图。
[0026] 图4是本实用新型实施例I的旋流整流隔板结构外观三维渲染轴侧图。
[0027] 图5是本实用新型实施例I的旋流整流隔板结构外观三维渲染俯视图。
[0028] 图6是本实用新型的倾斜气体导管结构示意图。
[0029] 图中：1、立式吸收塔；2、气体进口管道；3、气体出口管道；4、旋流整流隔板；4_1、上开孔隔板；4_2、下开孔隔板；4-3、倾斜气体导管；5、浆液喷嘴组；6、除雾器；7、浆液池。具体实施方式
[0030] 以下结合附图和具体实施例对本实用新型作进一步详细阐述。
[0031] 实施例I :如图I、图4和图5所示，本吸收塔I下部侧面设有两根气体进口管道2，吸收塔I顶部设有除雾器6，气体在塔内发生气液吸收反应、除雾后经气体出口管道3排出。本吸收塔I布置一个旋流整流隔板4，包含两圈倾斜方向相反的倾斜气体导管4-3。旋流整流隔板4上部、下部均布置进行水平喷雾的浆液喷嘴组5。吸收塔I底部设置浆液池7。
[0032] 实施例2 :与实施例I基本相同，如图2所示。与实施例I略有不同，本实施例的吸收塔I下部侧面设有一根气体进口管道2，布置两个旋流整流隔板4。吸收塔I底部不设置浆液池。
[0033] 本实施例适用于较高的入口气体有害气体浓度，两个旋流整流隔板4形成两级吸收塔，可以满足达标排放。
[0034] 实施例3 :与实施例I基本相同，如图3所示。与实施例I略有不同，本实施例的吸收塔I的旋流整流隔板4仅上部布置的浆液喷嘴组5，浆液喷嘴组5为布置于吸收塔I内部的浆液喷淋层。
[0035] 旋流整流隔板4布置多圈倾斜方向相反的倾斜气体导管4-3，由气体进口管道2侧面进入吸收塔I的气体经过旋流整流隔板4后，消除了气体偏流，气体分布趋于均匀，有利于气液高效吸收。
[0036] 旋流整流气液吸收塔工程应用如下。
[0037] 燃煤锅炉参数：两台25T/h循环流化床锅炉，标况烟气量2X25000Nm3/h，入口烟气温度 120°C左右，SO2 浓度 250(T3000mg/Nm3。
[0038] 选取吸收塔表观烟气流速为4. 2m/s,设计吸收塔直径2. 6m，吸收塔下部对称布置两根气体入口管道，顶部一根气体出口管道。考虑烟气中较高SO2浓度，本工程采用两级吸收塔。旋流整流隔板包含两圈倾斜方向相反的倾斜气体导管，内圈4根、外圈6根，长径比约为I. 5，倾斜角度45°，其中的气体流速为13m/s。经计算机数值模拟和现场测定，旋流整流隔板上部的气体流场为：约1/2半径至壁面的范围内，形成旋流流动，吸收塔中部约1/2半径范围内形成向下的流动。这种流场提高了气体停留时间，增强气液吸收反应效果：在Ca/S摩尔比为1.03时，吸收效率可达到98%以上。
Claims (5)
1. 一种旋流整流气液吸收塔，包含立式吸收塔，其特征在于：所述塔体设有气体进口管和气体出口管，吸收塔内部设置旋流整流隔板，该隔板由上、下开孔隔板及连接上下开孔隔板的多根倾斜气体导管组成。
2.根据权利要求I所述的旋流整流气液吸收塔，其特征在于：所述立式吸收塔，其塔体截面可以是圆形或矩形，气体进口管或气体出口管可以是一根或多根。
3.根据权利要求I或2所述的旋流整流气液吸收塔，其特征在于：所述的旋流整流隔板包含一圈或多圈的倾斜气体导管，其中任意一圈或多圈的倾斜气体导管的倾斜方向与其余不同；倾斜气体导管的长径比为O. 5〜2，倾斜角度α为30〜60°。
4.根据权利要求I或2所述的旋流整流气液吸收塔，其特征在于：所述的旋流整流隔板的数量为I〜5个,每个旋流整流隔板的上部或下部布置有衆液喷嘴组。
5.根据权利要求4所述的旋流整流气液吸收塔，其特征在于：所述的浆液喷嘴组可以是布置于吸收塔内部的浆液喷淋层，也可以是布置于吸收塔竖直壁面上、进行水平或近似水平喷雾的喷嘴组。
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104324574A (zh) * | 2013-07-22 | 2015-02-04 | 丰田自动车株式会社 | 涂装系统的除尘装置 |
| CN105617852A (zh) * | 2016-03-28 | 2016-06-01 | 上海龙净环保科技工程有限公司 | 设有多孔均流器的脱硫除尘吸收塔 |
| WO2017185564A1 (zh) * | 2016-04-29 | 2017-11-02 | 中电投远达环保工程有限公司重庆科技分公司 | 自适应沸腾式泡沫脱硫除尘装置 |
| CN111151106A (zh) * | 2018-11-07 | 2020-05-15 | 洛阳德明石化设备有限公司 | 一种提高wgs脱硫塔气液分离效果的系统及其应用 |
| CN113041642A (zh) * | 2021-03-26 | 2021-06-29 | 江西清绿环保有限公司 | 一种喷漆废气预处理系统 |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104324574A (zh) * | 2013-07-22 | 2015-02-04 | 丰田自动车株式会社 | 涂装系统的除尘装置 |
| CN105617852A (zh) * | 2016-03-28 | 2016-06-01 | 上海龙净环保科技工程有限公司 | 设有多孔均流器的脱硫除尘吸收塔 |
| WO2017185564A1 (zh) * | 2016-04-29 | 2017-11-02 | 中电投远达环保工程有限公司重庆科技分公司 | 自适应沸腾式泡沫脱硫除尘装置 |
| CN111151106A (zh) * | 2018-11-07 | 2020-05-15 | 洛阳德明石化设备有限公司 | 一种提高wgs脱硫塔气液分离效果的系统及其应用 |
| CN113041642A (zh) * | 2021-03-26 | 2021-06-29 | 江西清绿环保有限公司 | 一种喷漆废气预处理系统 |
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