CN102008863B - 锅炉水膜除尘器 - Google Patents

锅炉水膜除尘器 Download PDF

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CN102008863B
CN102008863B CN 201010580727 CN201010580727A CN102008863B CN 102008863 B CN102008863 B CN 102008863B CN 201010580727 CN201010580727 CN 201010580727 CN 201010580727 A CN201010580727 A CN 201010580727A CN 102008863 B CN102008863 B CN 102008863B
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boiler
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water film
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CN102008863A (zh
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李机旻
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HAOLUN BIOCHEMICAL ASSISTANT CO Ltd CHENZHOU
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Abstract

本发明涉及一种锅炉水膜除尘器,属于锅炉除尘器领域。其主要结构包括壳体(1)、进烟管(2)、出烟管(4)、导流管(3)、除尘室(5)和水灰池(8);壳体(1)内由隔板(9)分为几级除尘室(5),相邻级除尘室(5)之间用导流管(3)连接,每级除尘室(5)底部是水灰池(8);所述的进烟管(2)一端接锅炉烟管,另端伸到第一级除尘室(5)下部,且与导流管(3)平行;出烟管(4)从最末级除尘室(5)的上部引出,外接引风机。本发明结构简单合理、除尘效果好、效率高、节约水,是理想的水膜除尘器。

Description

锅炉水膜除尘器
技术领域
本发明涉及一种锅炉水膜除尘器,属于锅炉除尘器领域。
背景技术
现在公开的锅炉水膜除尘器都是利用水喷方式形成水膜除尘,此类水膜除尘器造成水资源浪费,并且形成二次污染;2003年5月14日中国发明专利申请公开号CN1416937A,公开了一种“锅炉水膜除尘器”,是在壳体内布置旋风子,壳体的底部为泥水斗,在旋风子筒体的中部设置隔板,将旋风子筒体间密封,由隔板向上到旋风子筒体上沿构成一个水箱;该水膜除尘器的烟尘通过旋风子筒体离心分离、隔板的水膜处理,脱硫除尘效率高。但隔板底部不能形成水膜,除尘效果大打折扣。
发明内容
本发明所要解决的技术问题是提供一种锅炉水膜除尘器,能克服以上两种形式除尘器的缺点,不会造成水源的浪费和二次污染,又具有及好的除尘效果。
本发明解决问题的技术方案是:一种锅炉水膜除尘器,包括壳体、进烟管、出烟管、导流管、除尘室和水灰池;壳体内由隔板分为几级除尘室,相邻级除尘室之间用导流管连接,导流管的上端口连通前级除尘室的上部,下端口伸到下级除尘室的下部;每级除尘室底部是水灰池;所述的进烟管一端接锅炉烟管,另端伸到第一级除尘室下部,且与导流管平行;出烟管从最末级除尘室的上部引出,外接引风机。
上述每级水灰池底部都成里高外低的斜坡,斜坡最低处设有清渣口;水灰池的水面要超过横梁的高度,使对应该级的除尘室和清渣口之间密封。
本发明利用引风机作为动力源,在引风机的作用下,使密封的除尘室内形成真空吸引力,把水灰池内的的水向上吸,吸上的水上下波动,除尘室内形成水膜,锅炉烟气与水充分接触而达到除尘效果。与现有技术比较,本发明所设计的导流管既起导流作用,又使锅炉烟气有一个垂直向下的速度对冲水,锅炉部分烟尘直接被水吸收。本发明锅炉水膜除尘器结构简单合理、除尘效果好、效率高、节约水,是理想的水膜除尘器。
附图说明
图1是本发明的结构图;
图2是图1的侧面图。
图中:1-壳体;2-进烟管;3-导流管;4-出烟管;5-除尘室;6-清渣口;7-横梁;8-水灰池;9-隔板。
具体实施方式
参考附图1,2,本实施例是一种锅炉水膜除尘器,包括壳体1、进烟管2、出烟管4、导流管3、除尘室5、水灰池8组成。壳体1内由隔板9分为几级除尘室5,相邻级除尘室5之间用导流管3连接,导流管3一端伸到除尘室5下部,控制炉烟的走向,使炉烟在每一级除尘室5内都从下部往上运动;除尘室5底部是水灰池8,水灰池8的水用来密封除尘室5和形成水膜;水灰池8既是水池又是灰池,被除尘室5清除的灰尘落在水灰池内便于灰尘的收集。除尘室5的炉烟出口都从除尘室5上部引出,在引风机的作用下,使每一级除尘室5内都形成水膜;本实施例的进烟管2接锅炉烟管,进烟管2伸到第一级除尘室5下部与导流管3平行,起导流作用;出烟管4由最末级除尘室5上部引出,外接引风机进气管;水灰池8底部做成斜坡,里面高,外面低,斜坡最低处设有清渣口6;便于灰尘收集和清理;使用本发明锅炉水膜除尘器时,水灰池8要装满水,水面要超过横梁7一定高度,使对应该级的除尘室5和清渣口6之间密封。

Claims (2)

1.一种锅炉水膜除尘器,包括壳体(1)、进烟管(2)、出烟管(4)、导流管(3)、除尘室(5)和水灰池(8);其特征在于:壳体(1)内由隔板(9)分为几级除尘室(5),相邻级除尘室(5)之间用导流管(3)连接,导流管(3)的上端口连通前级除尘室(5)的上部,下端口伸到下级除尘室(5)的下部;每级除尘室(5)底部是水灰池(8);所述的进烟管(2)一端接锅炉烟管,另端伸到第一级除尘室(5)下部,且与导流管(3)平行;出烟管(4)从最末级除尘室(5)的上部引出,外接引风机。
2.根据权利要求1所述的锅炉水膜除尘器;其特征在于:所述的每级水灰池(8)底部都成里高外低的斜坡;斜坡最低处设有清渣口(6);水灰池(8)的水面要超过横梁(7)的高度,使对应该级的除尘室(5)和清渣口(6)之间密封。
CN 201010580727 2010-12-02 2010-12-02 锅炉水膜除尘器 Expired - Fee Related CN102008863B (zh)

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CN106390640B (zh) * 2016-10-31 2019-03-15 重庆市南川区庆岩福利碱厂 用于硫化碱的锅炉除尘除垢器
CN106540940B (zh) * 2016-10-31 2019-03-15 重庆市南川区庆岩福利碱厂 具有除尘机构的烟气除尘箱

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US4609386A (en) * 1984-01-27 1986-09-02 Sibley John R Pulsating flow scrubber attachment
US5298043A (en) * 1992-05-19 1994-03-29 Mai Sung Chuan Filter system for smoke or polluted air
CN2408952Y (zh) * 1999-12-17 2000-12-06 梅家明 高效水膜除尘脱硫装置
CN1416937A (zh) * 2001-11-09 2003-05-14 长春市宽城锅炉排汽阀厂 锅炉水膜除尘器
CN2750856Y (zh) * 2004-12-20 2006-01-11 赖甸 废气多级净化装置
CN1911488A (zh) * 2005-08-11 2007-02-14 广东新明珠陶瓷集团有限公司 环保型烟气湿法除尘装置和使用该装置对烟气进行湿法除尘的方法
CN202028307U (zh) * 2010-12-02 2011-11-09 郴州浩伦生化助剂有限公司 锅炉水膜除尘器

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US6893484B2 (en) * 2003-10-06 2005-05-17 Desert Energy Ltd Low operating pressure gas scrubber

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4609386A (en) * 1984-01-27 1986-09-02 Sibley John R Pulsating flow scrubber attachment
US5298043A (en) * 1992-05-19 1994-03-29 Mai Sung Chuan Filter system for smoke or polluted air
CN2408952Y (zh) * 1999-12-17 2000-12-06 梅家明 高效水膜除尘脱硫装置
CN1416937A (zh) * 2001-11-09 2003-05-14 长春市宽城锅炉排汽阀厂 锅炉水膜除尘器
CN2750856Y (zh) * 2004-12-20 2006-01-11 赖甸 废气多级净化装置
CN1911488A (zh) * 2005-08-11 2007-02-14 广东新明珠陶瓷集团有限公司 环保型烟气湿法除尘装置和使用该装置对烟气进行湿法除尘的方法
CN202028307U (zh) * 2010-12-02 2011-11-09 郴州浩伦生化助剂有限公司 锅炉水膜除尘器

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