CN102441323A - 旋流双超重力机 - Google Patents
旋流双超重力机 Download PDFInfo
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- CN102441323A CN102441323A CN2011103426746A CN201110342674A CN102441323A CN 102441323 A CN102441323 A CN 102441323A CN 2011103426746 A CN2011103426746 A CN 2011103426746A CN 201110342674 A CN201110342674 A CN 201110342674A CN 102441323 A CN102441323 A CN 102441323A
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- eddy flow
- impeller
- gravity
- swirl
- liquid
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- 239000007789 gases Substances 0.000 claims abstract description 41
- 239000007788 liquids Substances 0.000 claims abstract description 37
- 238000000889 atomisation Methods 0.000 claims abstract description 21
- 239000011257 shell materials Substances 0.000 claims abstract description 11
- 239000003480 eluents Substances 0.000 claims description 14
- 239000010410 layers Substances 0.000 claims description 6
- 230000000694 effects Effects 0.000 abstract description 13
- 238000005406 washing Methods 0.000 abstract description 4
- 238000010521 absorption reactions Methods 0.000 abstract description 3
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- 239000003034 coal gas Substances 0.000 description 5
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- 238000006243 chemical reactions Methods 0.000 description 3
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- CURLTUGMZLYLDI-UHFFFAOYSA-N carbon dioxide Chemical compound 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O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxides Inorganic materials 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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[O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
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- 239000003546 flue gases Substances 0.000 description 1
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- 238000000034 methods Methods 0.000 description 1
- UFWIBTONFRDIAS-UHFFFAOYSA-N naphthalene Chemical compound 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C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 1
- 239000011049 pearl Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000001172 regenerating Effects 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
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Abstract
本发明公开了一种旋流双超重力机，包括壳体，在壳体内设有相通的旋流重力雾化段和离心重力场段；在所述的旋流重力雾化段内设有导流板，在所述的导流板上设有漏液孔；在导流板的下方设有由雾化网、固定叶轮、旋流叶轮和底板组成的圆筒形旋流重力雾化器，所述的固定叶轮和旋流叶轮包裹在雾化网内形成，底板设在旋流叶轮底部；在壳体的顶部设有洗脱液进口和气体进口，所述的导流板通过密封口圈与壳体的顶部密封后形成腔体，洗脱液进口与该腔体相通，气体进口通过管路连接穿过腔体与筒体相通；在所述的离心重力场段设有离心重力器，在离心重力器的上方设有环形隔板，在环形隔板中间留有汽液通孔，在环形隔板上留有筛孔；在壳体内设有中轴，所述的中轴与旋流叶轮片和离心重力器均相连。该旋流双超重力机克服气液简单并流接触的洗涤吸收缺点，提高常压下脱硫效果，具有很好的实用性，能够产生很好的经济效益和社会效益。
Description
旋流双超重力机
技术领域
[0001] 本发明涉及一种超重力设备，具体涉及一种旋流双超重力机。 背景技术
[0002] 超重力机是化工领域中的常用设备，常用来对气体进行洗脱分离杂质，例如：脱除气体中的硫化氢、二氧化硫、二氧化碳、氰化氢等杂质气体。在具体使用中，在2. OMPa以上的高中压下，气体穿越填料床，在高速离心力作用下，溶液穿越填料床，实现气液在填料中逆向接触吸收，该工艺技术适用于干净气体和高中压下操作。当进行焦炉煤气净化时，溶液从旋转的填料床上或内侧喷淋，在离心力作用下，很容易穿越填料床，由于焦化煤气净化系统压力低于0. 05Mpa，属于低气压力，焦化煤气很难逆向穿越填料与溶液形成逆流，只能与溶液并流沿离心力方向穿越填料床，这种低压并流吸收与高压逆流吸收相比，传质效果相差很大。不能够满足使用需求。
发明内容
[0003] 发明目的：针对现有技术中存在的不足，本发明的目的是提供一种旋流双超重力机，以使煤气在旋流双超重力机内，经过旋流雾化液洗涤吸收脱硫和离心力场的重力混合脱硫，克服气液简单并流接触的洗涤吸收缺点，达到雾化液与煤气预混合脱硫的作用，提高常压下脱硫效果。
[0004] 技术方案：为了实现上述发明目的，本发明采用的技术方案为：
一种旋流双超重力机，包括壳体，在壳体内设有相通的旋流重力雾化段和离心重力场段；在所述的旋流重力雾化段内设有导流板，在所述的导流板上设有漏液孔；在导流板的下方设有由雾化网、固定叶轮、旋流叶轮和底板组成的圆筒形旋流重力雾化器，所述的固定叶轮和旋流叶轮包裹在雾化网内形成，底板设在旋流叶轮底部；在壳体的顶部设有洗脱液进口和气体进口，所述的导流板通过密封口圈与壳体的顶部密封后形成腔体，洗脱液进口与该腔体相通，气体进口通过管路连接穿过腔体与筒体相通；在所述的离心重力场段设有离心重力器，在离心重力器的上方设有环形隔板，在环形隔板中间留有汽液通孔，在环形隔板上留有筛孔；在壳体内设有中轴，所述的中轴与旋流叶轮片和离心重力器均相连。
[0005] 所述的固定叶轮和旋流叶轮均由数个叶轮片组成，固定叶轮和旋流叶轮的叶轮片数量相同或不同。
[0006] 在所述环形隔板的汽液通孔周围设有拦液堰。
[0007] 本发明的旋流重力雾化段，可以设置在离心重力场段之上，也可以单独设置，如果气体压力太低，则需外加风机加压。
[0008] 离心重力器由龙骨架和填料床构成，在填料床上设置填料层。
[0009] 有益效果：与现有技术中的超重力机相比，本发明的旋流双超重力机具有的突出优点包括：结构简单，设计巧妙，根据焦炉煤气特点和净化工艺系统的工序组合规律，使煤气在旋流双超重力机内，经过旋流雾化液洗涤吸收脱硫和离心力场的重力混合脱硫，克服
3气液简单并流接触的洗涤吸收缺点，达到雾化液与煤气预混合脱硫的作用，提高常压下脱硫效果，具有很好的实用性，能够产生很好的经济效益和社会效益。
[0010] 此外，该旋流双超重力机，可适用于多种压力情况下，处理经过脱渣、脱焦油、脱萘后的煤气或其他气体。也适用于相平衡吸收和化学吸收，主要应用方向是气体脱除硫化氢、 氰化氢、二氧化硫等酸性气体，还可应用于水脱氧、脱挥、精馏、萃取、废水处理、烟气脱硫除尘、化工合成等。
附图说明
[0011] 图1是旋流双超重力机的结构示意图； 图2是旋流重力雾化器的结构示意图。 具体实施方式
[0012] 下面结合具体附图对本发明做进一步的解释。
[0013] 如图1所示，旋流双超重力机包括柱形壳体1，在壳体1的顶部设有洗脱液进口 8 和气体进口 11，侧边上设有备用口 12，底部侧边上设有气液出口 9。在壳体1的底部设有支架。壳体1的内部结构上由上下相通的两部分构成，即旋流重力雾化段和旋流重力雾化段， 旋流重力雾化段可以设在旋流重力雾化段之上或之下，优选设在旋流重力雾化段之上。以下重点以优选的方案进行介绍。
[0014] 旋流重力雾化段整体是一个圆形筒体，上部设有导流板2，在导流板2上设有漏液孔；在导流板2下设有旋流重力雾化器，旋流重力雾化器为由雾化网3包裹的由上至下依次设置固定叶轮4、旋流叶轮5和底板18，固定叶轮4固定不动，旋流叶轮5可以旋转，中轴7 驱动。固定叶轮4和旋流叶轮5均由数个叶轮片组成，固定叶轮4和旋流叶轮5的叶轮片数量相同或不同，优选不同。导流板2与壳体1顶部通过密封口圈14密封后形成腔体，洗脱液进口 8与该腔体相通。
[0015] 离心重力场段，直径与旋流重力雾化段相同，内设一个离心重力器6，其结构由龙骨架和填料床构成，在填料床上设置填料层，离心重力器6由中轴7驱动。
[0016] 为防止气液短路，在旋流重力雾化段底部与离心重力场段之间设置环形隔板13， 环形隔板13中央设有汽液通孔17，并沿汽液通孔17圆周设有一个环形挡板作为拦液堰 16。在环形隔板13上设有筛孔15，筛孔15正对填料床，使溶液均勻流入填料层。雾化气和气体由汽液通孔17进入离心力场，在填料床与下行溶液相遇接触反应。
[0017] 在驱动结构上，中轴7穿过汽液通孔17与旋流重力雾化段旋流板4相连，驱动旋流板4旋转。在壳体1内，中轴7与动力设备之间的机体密封采用磁力传动和密封技术，气体与润滑液之间采用胶件密封并设有一定的润滑液与回流口的高度，使气体不能由回流口泄露，保证正常运行。在传动部分箱体内部采用液态静压轴承或动态油膜轴承，由外部供给润滑系统，保证其润滑并把所产生的热量运出，其外供给润滑系统设有工作压力，既能静压轴承的压力流，也可供给动态油膜轴承润滑，并设有压力、等压面系统的安全阀设置和报警
直ο
[0018] 工作时，洗脱液B由导流板2上漏液孔向下喷淋，气体A由气体进口 11通入筒体内，洗脱液B由旋转的旋流叶轮5撞击成雾状与气体A混合，在旋转力的作用下，固定叶轮4 和旋转叶轮5上的洗脱液B产生旋流、撕裂，在离心力的作用下向四周溅射，雾化，与气体A结合，对气体A洗脱，溅射的气液体穿过雾化网3，进行再次的机械雾化完成第二次洗脱后， 碰向壳体1内壁，在重力的作用下下落，进入离心重力场段。气体A和液珠混合物被旋转的离心重力场中心吸入，并在重力场作用下由中央压入填料床，并沿切线方向旋转穿过填料层，最后抛入壳体1内壁，汇集在离心重力器6底部并从侧面切线方向的气液出口9引出气液混合物C。经另外设置的分液器分离出循环液，气液完成传质操作并分离。
[0019] 此外，工作时，洗脱液B和气体A也可以逆向进行，即洗脱液B由导流板2上漏液孔向下喷淋，气体A由气体出口 9通入筒体内，洗脱液B由旋转的旋流叶轮5撞击成雾状与气体A混合，在旋转力的作用下，固定叶轮4和旋转叶轮5上的洗脱液B产生旋流、撕裂，在离心力的作用下向四周溅射，雾化，与气体A结合，对气体A洗脱，此时，叶轮片优选由气液并行时的直片改为弯曲片，使气体A在旋转中产生一个向上的旋流力，使得干净气体从进口 11排出。其中，弯曲片可以为弧形片或有一定角度的折片。
[0020] 本发明的旋流双超重力旋流机兼容喷雾反应段和填料反应段的双重性能。喷雾吸收是依靠水力旋流产生的旋转、撞击、分割、雾化作用，使吸收液充分分散增加吸收表面积， 同时在旋转的搅动下使气体与液体之间接触表面不断更新。旋流是由固定叶轮4和旋转叶轮5在相互作用下产生旋流，在离心力的作用下，冲击下上叶片，割裂在下叶片的作用力下重新生成2倍个螺旋旋流并在旋流叶轮5的作用下冲向雾化网3，进行脱气运作过程，不断补给新洗脱液，穿越雾化网3后撞向壳体1内壁又一次雾化传质反应。经由重力旋流雾化反应后的气液混合物用环形隔板13分离，未雾化液集合到环形隔板13淋洒入填料层，而雾化液和气体混合进入离心重力机中央，并且在离心力作用下穿越填料床与垂直淋洒的溶液错流接触吸收硫化物。
[0021] 本发明的旋流双超重力机可根据处理气体的操作压力条件调整气液的进出口位置，因此适用于高中压气液反应工艺也适用于低压或常压反应工艺。
Claims (9)
1. 一种旋流双超重力机，包括壳体（1)；其特征在于：在壳体（1)内设有相通的旋流重力雾化段和离心重力场段；在所述的旋流重力雾化段内设有导流板（2)，在所述的导流板 (2)上设有漏液孔；在导流板（2)的下方设有由雾化网（3)、固定叶轮（4)、旋流叶轮（5)和底板（18)组成的圆筒形旋流重力雾化器，所述的固定叶轮（4)和旋流叶轮（5)包裹在雾化网（3)内形成，底板（18)设在旋流叶轮（5)底部；在壳体（1)的顶部设有洗脱液进口（8)和气体进口（ 11 )，所述的导流板（2)通过密封口圈（14)与壳体（1)的顶部密封后形成腔体，洗脱液进口（8)与该腔体相通，气体进口（11)通过管路连接穿过腔体与筒体相通；在所述的离心重力场段设有离心重力器（6)，在离心重力器（6)的上方设有环形隔板（13)，在环形隔板（13)中间留有汽液通孔（17)，在环形隔板（13)上留有筛孔（15);在壳体（1)内设有中轴 (7)，所述的中轴（7)与旋流叶轮片（5)和离心重力器（6)均相连。
2.根据权利要求1所述的旋流双超重力机，其特征在于：所述的固定叶轮（4)和旋流叶轮（5)均由数个叶轮片组成，固定叶轮（4)和旋流叶轮（5)的叶轮片数量相同或不同。
3.根据权利要求2所述的旋流双超重力机，其特征在于：所述的叶轮片为直片或弯曲片。
4.根据权利要求3所述的旋流双超重力机，其特征在于：所述的弯曲片为弧形片或有一定角度的折片。
5.根据权利要求1所述的旋流双超重力机，其特征在于：在所述环形隔板（13)的汽液通孔（17)周围设有拦液堰（16)。
6.根据权利要求1所述的旋流双超重力机，其特征在于：所述的中轴（7)设在汽液通孔 (17)内。
7.根据权利要求1所述的旋流双超重力机，其特征在于：所述的中轴（7)与外设动力设备之间为磁力传动。
8.根据权利要求1所述的旋流双超重力机，其特征在于：所述的离心重力器（6)由龙骨架和填料床构成，在填料床上设置填料层。
9.根据权利要求1所述的旋流双超重力机，其特征在于：所述的旋流重力雾化段设置在离心重力场段之上或单独设置。
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Cited By (6)
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| CN102908875A (zh) * | 2012-11-10 | 2013-02-06 | 李玉卫 | 消烟除尘脱硫器 |
| CN102974181A (zh) * | 2012-11-14 | 2013-03-20 | 江苏中显集团有限公司 | 一种烟气除尘脱硫脱硝工艺及其专用设备 |
| CN104043326A (zh) * | 2014-06-04 | 2014-09-17 | 北京化工大学 | 一种新型工业气体超重力脱除硫化氢的装置及工艺 |
| CN104772026A (zh) * | 2015-04-07 | 2015-07-15 | 王文树 | 烟尘吸收器 |
| CN104941246A (zh) * | 2015-04-21 | 2015-09-30 | 昆明理工大学 | 一种撞击流超重力液液萃取器 |
| CN109200819A (zh) * | 2018-10-29 | 2019-01-15 | 江苏科技大学 | 一种船舶尾气处理装置及其双转子超重力反应器 |
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| CN101036848A (zh) * | 2007-02-07 | 2007-09-19 | 江苏工业学院 | 一种气体吸收净化装置 |
| CN101224385A (zh) * | 2007-11-02 | 2008-07-23 | 杨传芳 | 多场细分子化综合作用管式烟气脱硫机 |
| CN101716448A (zh) * | 2010-01-04 | 2010-06-02 | 中国科学院过程工程研究所 | 一种强化传递的动态旋转旋流板装置 |
| CN202336335U (zh) * | 2011-11-03 | 2012-07-18 | 袁长胜 | 旋流双超重力机 |
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| CN101036848A (zh) * | 2007-02-07 | 2007-09-19 | 江苏工业学院 | 一种气体吸收净化装置 |
| CN101224385A (zh) * | 2007-11-02 | 2008-07-23 | 杨传芳 | 多场细分子化综合作用管式烟气脱硫机 |
| CN101716448A (zh) * | 2010-01-04 | 2010-06-02 | 中国科学院过程工程研究所 | 一种强化传递的动态旋转旋流板装置 |
| CN202336335U (zh) * | 2011-11-03 | 2012-07-18 | 袁长胜 | 旋流双超重力机 |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102908875A (zh) * | 2012-11-10 | 2013-02-06 | 李玉卫 | 消烟除尘脱硫器 |
| CN102974181A (zh) * | 2012-11-14 | 2013-03-20 | 江苏中显集团有限公司 | 一种烟气除尘脱硫脱硝工艺及其专用设备 |
| CN104043326A (zh) * | 2014-06-04 | 2014-09-17 | 北京化工大学 | 一种新型工业气体超重力脱除硫化氢的装置及工艺 |
| CN104043326B (zh) * | 2014-06-04 | 2016-08-17 | 北京化工大学 | 一种工业气体超重力脱除硫化氢的装置及工艺 |
| CN104772026A (zh) * | 2015-04-07 | 2015-07-15 | 王文树 | 烟尘吸收器 |
| CN104772026B (zh) * | 2015-04-07 | 2016-07-27 | 王文树 | 烟尘吸收器 |
| CN104941246A (zh) * | 2015-04-21 | 2015-09-30 | 昆明理工大学 | 一种撞击流超重力液液萃取器 |
| CN104941246B (zh) * | 2015-04-21 | 2016-09-21 | 昆明理工大学 | 一种撞击流超重力液液萃取器 |
| CN109200819A (zh) * | 2018-10-29 | 2019-01-15 | 江苏科技大学 | 一种船舶尾气处理装置及其双转子超重力反应器 |
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| CN102441323B (zh) | 2013-10-30 |
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