CN2581051Y - Secondary dusting, desulfurizing denitrificating integrated reaction tower - Google Patents

Secondary dusting, desulfurizing denitrificating integrated reaction tower Download PDF

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Publication number
CN2581051Y
CN2581051Y CN 02229751 CN02229751U CN2581051Y CN 2581051 Y CN2581051 Y CN 2581051Y CN 02229751 CN02229751 CN 02229751 CN 02229751 U CN02229751 U CN 02229751U CN 2581051 Y CN2581051 Y CN 2581051Y
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CN
China
Prior art keywords
reaction tower
tower
absorption liquid
waste gas
side wall
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Expired - Fee Related
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CN 02229751
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Chinese (zh)
Inventor
曾庆智
杨全志
曾东海
张义忠
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Henan University
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Individual
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Priority to CN 02229751 priority Critical patent/CN2581051Y/en
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Publication of CN2581051Y publication Critical patent/CN2581051Y/en
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Expired - Fee Related legal-status Critical Current

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  • Gas Separation By Absorption (AREA)

Abstract

本实用新型涉及一种对工业锅炉产生的烟气进行处理的二次除尘,脱硫、脱氮综合反应塔。该反应塔由反应塔和除湿塔双联而成,反应塔和除湿塔之间通过两塔上部侧壁上的一个百页窗式除水通道相连,除湿塔下部侧壁上设置有废气出口,反应塔底部为吸收液积聚部,吸收液积聚部侧壁上设有溢流孔,反应塔内吸收液积聚部上方设置有水平箅板,箅板上堆放有一层塑料空心球层,塑料空心球层上方反应塔内均匀安装有吸收液喷头,废气引入管出口向下设置,其出口高于溢流孔,低于箅板。

The utility model relates to a secondary dedusting, desulfurization and denitrification comprehensive reaction tower for processing flue gas produced by industrial boilers. The reaction tower is composed of a reaction tower and a dehumidification tower. The reaction tower and the dehumidification tower are connected by a louver-type water removal channel on the upper side wall of the two towers. The lower side wall of the dehumidification tower is provided with a waste gas outlet. The bottom of the reaction tower is the accumulation part of the absorption liquid, and an overflow hole is provided on the side wall of the absorption liquid accumulation part. A horizontal grate plate is arranged above the absorption liquid accumulation part in the reaction tower, and a layer of plastic hollow balls is stacked on the grate plate. Plastic hollow balls Absorption liquid nozzles are evenly installed in the reaction tower above the layer, and the outlet of the waste gas introduction pipe is set downward, and its outlet is higher than the overflow hole and lower than the grate plate.

Description

Final dusting, desulfurization, denitrogenation combined reaction tower
Technical field
The utility model relates to the final dusting that a kind of flue gas that Industrial Boiler is produced is handled, desulfurization, denitrogenation combined reaction tower.
Background technology
The flue dust that fuel combustion in the boiler produced, SO x, NO xMake atmosphere be subjected to serious pollution etc. harmful substance, and injured human beings'health.Along with the increase of development and national economy and energy development, utilization, the atmosphere pollution situation is also in rapid increase.In order to protect environment, make air more pure and fresh, must the discharge capacity of pollutant be limited, especially to flue dust, SO that fuel combustion in the boiler produced x, NO xControlled etc. the emission of harmful substances amount.
The utility model content
The purpose of this utility model is to provide a kind of final dusting, desulfurization, denitrogenation combined reaction tower.
For achieving the above object, the technical solution of the utility model is to have adopted a kind of final dusting, desulfurization, denitrogenation combined reaction tower, this reaction tower is formed by reaction tower and dehumidifying tower duplex, link to each other by a louvre type water removal channel on the two tower upper portion side wall between reaction tower and the dehumidifying tower, dehumidifying tower lower sides is provided with waste gas outlet, portion is gathered for absorption liquid in the reaction tower bottom, absorption liquid gathers portion's sidewall and is provided with spout hole, absorption liquid gathers the portion top and is provided with horizontal grate plate in the reaction tower, be stacked with one deck plastic hollow ball layer on the grate plate, in the reaction tower of plastic hollow ball layer top the absorption liquid shower nozzle is installed evenly, the outlet of waste gas inlet tube is provided with downwards, its outlet is higher than spout hole, is lower than grate plate.
The window page or leaf of described louvre type water removal channel is an arc page or leaf plate, and arc page or leaf plate is higher than reaction tower one side in a side of dehumidifying tower.
Above the absorption liquid shower nozzle, also be provided with the clear water shower nozzle.
The tower design of duplex of the present utility model, simple in structure and relatively more reasonable, when waste gas is guided to this final dusting, desulfurization, denitrogenation combined reaction tower when the waste gas inlet tube blows out downwards after one-time dedusting is handled, flue dust and waste gas blow pressure absorption liquid liquid level, the part of flue dust wherein, sulphur, nitrogen oxide can be absorbed, and waste gas slows down through grate plate and the rising of plastic hollow ball simultaneously.The spray of the droplet of absorption liquid shower nozzle ejection makes on the plastic hollow ball sphere to be covered with absorption liquid, has enlarged absorption area, waste gas is through out-of-date, the plastic hollow ball is bob thereupon, has increased time of contact again, can remove grit more fully and have grain and absorption liquid to flow back to the portion of gathering.Waste gas is by behind the plastic hollow ball layer, in the low speed uphill process, again can with absorption liquid droplet haptoreaction, can further remove the pernicious gas content in the waste gas.Waste gas can be finished the process of final dusting, desulfurization, denitrogenation basically through behind above a few step levels, has played good environmental-protection function, and is very helpful to improving air quality.The clear water shower nozzle that installs additional again on the absorption liquid shower nozzle can make full use of fan bearing cooling water and heat thereof, and waste gas is cleaned and humidification more up hill and dale, is convenient to the subsequent treatment of waste gas.The design of dehumidifying tower can utilize the heat of waste gas, in the dirty process of waste gas low speed, removes water content, further improves the quality of emission gases.
Description of drawings
Fig. 1 is a structural representation of the present utility model;
Fig. 2 is the A-A cutaway view of Fig. 1;
Fig. 3 is the C-C cutaway view of Fig. 2.
The specific embodiment
As Fig. 1, Fig. 2, shown in Figure 3, final dusting of the present utility model, desulfurization, denitrogenation combined reaction tower is formed by reaction tower 1 and dehumidifying tower 3 duplexs, link to each other by a louvre type water removal channel on the two tower upper portion side wall 2 between reaction tower 1 and the dehumidifying tower 3, the window page or leaf of louvre type water removal channel 2 is an arc page or leaf plate, arc page or leaf plate is higher than a side of reaction tower 1 in a side of dehumidifying tower 3, dehumidifying tower 3 lower sides are provided with waste gas outlet 4, portion 5 is gathered for absorption liquid in reaction tower 1 bottom, absorption liquid gathers portion's 5 sidewalls and is provided with spout hole 11, absorption liquid in the reaction tower 1 gathers portion 5 tops and is provided with horizontal grate plate 6, be stacked with one deck plastic hollow ball layer 7 on the grate plate 6, in the plastic hollow ball layer 7 top reaction tower absorption liquid shower nozzle 8 is installed evenly, above absorption liquid shower nozzle 8, also be provided with clear water shower nozzle 9, the outlet of waste gas inlet tube 10 is provided with downwards, its outlet is higher than spout hole 11, is lower than grate plate 6.

Claims (3)

1、一种二次除尘、脱硫、脱氮综合反应塔,其特征在于:该反应塔由反应塔和除湿塔双联而成,反应塔和除湿塔之间通过两塔上部侧壁上的一个百页窗式除水通道相连,除湿塔下部侧壁上设置有废气出口,反应塔底部为吸收液积聚部,吸收液积聚部侧壁上设有溢流孔,反应塔内吸收液积聚部上方设置有水平篦板,篦板上堆放有一层塑料空心球层,塑料空心球层上方反应塔内均匀安装有吸收液喷头,废气引入管出口向下设置,其出口高于溢流孔,低于篦板。1. A comprehensive reaction tower for secondary dust removal, desulfurization, and denitrification, characterized in that: the reaction tower is formed by a double connection of a reaction tower and a dehumidification tower, and the reaction tower and the dehumidification tower pass through a wall on the upper side wall of the two towers The louver-type dewatering channels are connected, and the side wall of the lower part of the dehumidification tower is provided with a waste gas outlet. The bottom of the reaction tower is an absorption liquid accumulation part, and an overflow hole is provided on the side wall of the absorption liquid accumulation part. There is a horizontal grate plate, and a layer of plastic hollow spheres is stacked on the grate plate. Absorption liquid nozzles are evenly installed in the reaction tower above the plastic hollow sphere layer. The outlet of the waste gas introduction pipe is set downward, and its outlet is higher than the overflow hole and lower than the grate plate. 2、根据权利要求1所述的综合反应塔,其特征在于:所述的百页窗式除水通道的窗页为弧形页板,弧形页板在除湿塔的一侧高于反应塔一侧。2. The comprehensive reaction tower according to claim 1, characterized in that: the window leaf of the louver-type water removal channel is an arc-shaped leaf plate, and the arc-shaped leaf plate is higher than the reaction tower on one side of the dehumidification tower side. 3、根据权利要求1所述的综合反应塔,其特征在于:在吸收液喷头上方还设置有清水喷头。3. The comprehensive reaction tower according to claim 1, characterized in that: a clear water nozzle is also arranged above the absorption liquid nozzle.
CN 02229751 2002-06-11 2002-06-11 Secondary dusting, desulfurizing denitrificating integrated reaction tower Expired - Fee Related CN2581051Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 02229751 CN2581051Y (en) 2002-06-11 2002-06-11 Secondary dusting, desulfurizing denitrificating integrated reaction tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 02229751 CN2581051Y (en) 2002-06-11 2002-06-11 Secondary dusting, desulfurizing denitrificating integrated reaction tower

Publications (1)

Publication Number Publication Date
CN2581051Y true CN2581051Y (en) 2003-10-22

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CN 02229751 Expired - Fee Related CN2581051Y (en) 2002-06-11 2002-06-11 Secondary dusting, desulfurizing denitrificating integrated reaction tower

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100363683C (en) * 2005-11-21 2008-01-23 孙克勤 Combined duct of fume desulfating
CN103301739A (en) * 2013-06-13 2013-09-18 江苏远东环保工程有限公司 Simple ammonia-method desulfurization tower with internally-arranged reactor
CN118376463A (en) * 2024-06-26 2024-07-23 河南省厚朴环保科技有限公司 A sampler for gas pollution detection and its use method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100363683C (en) * 2005-11-21 2008-01-23 孙克勤 Combined duct of fume desulfating
CN103301739A (en) * 2013-06-13 2013-09-18 江苏远东环保工程有限公司 Simple ammonia-method desulfurization tower with internally-arranged reactor
CN118376463A (en) * 2024-06-26 2024-07-23 河南省厚朴环保科技有限公司 A sampler for gas pollution detection and its use method

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C14 Grant of patent or utility model
GR01 Patent grant
ASS Succession or assignment of patent right

Owner name: HE NAN UNIV.

Free format text: FORMER OWNER: ZENG QINGZHI

Free format text: FORMER OWNER: YANG QUANZHI ZENG DONGHAI

Effective date: 20041105

C41 Transfer of patent application or patent right or utility model
TR01 Transfer of patent right

Effective date of registration: 20041105

Address after: 475000 Henan province city Minglun Street No. 85

Patentee after: Henan University

Address before: 475000, building 41, No. 1 corner street, Kaifeng, Henan

Co-patentee before: Yang Quanzhi

Patentee before: Zeng Qingzhi

Co-patentee before: Zeng Donghai

C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee