CN211837205U - Chemical acid mist waste gas treatment equipment - Google Patents
Chemical acid mist waste gas treatment equipment Download PDFInfo
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- CN211837205U CN211837205U CN201922166293.1U CN201922166293U CN211837205U CN 211837205 U CN211837205 U CN 211837205U CN 201922166293 U CN201922166293 U CN 201922166293U CN 211837205 U CN211837205 U CN 211837205U
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- waste gas
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- 239000002912 waste gas Substances 0.000 title claims abstract description 24
- 239000002253 acid Substances 0.000 title claims abstract description 21
- 239000003595 mist Substances 0.000 title claims abstract description 21
- 239000000126 substance Substances 0.000 title claims abstract description 19
- 239000007788 liquid Substances 0.000 claims abstract description 43
- 238000010521 absorption reaction Methods 0.000 claims abstract description 23
- 239000007789 gas Substances 0.000 claims abstract description 9
- 238000005507 spraying Methods 0.000 claims abstract 4
- 238000012545 processing Methods 0.000 claims description 14
- 239000007921 spray Substances 0.000 claims description 14
- 239000000945 filler Substances 0.000 claims description 9
- 230000002745 absorbent Effects 0.000 claims description 8
- 239000002250 absorbent Substances 0.000 claims description 8
- 238000012856 packing Methods 0.000 claims description 8
- 239000000919 ceramic Substances 0.000 claims description 5
- 239000002131 composite material Substances 0.000 claims description 3
- 239000011152 fibreglass Substances 0.000 claims description 3
- 238000004064 recycling Methods 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 12
- 238000013461 design Methods 0.000 abstract description 7
- 238000006386 neutralization reaction Methods 0.000 abstract description 6
- 230000004323 axial length Effects 0.000 abstract description 3
- 230000003139 buffering effect Effects 0.000 abstract 1
- 238000000034 method Methods 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000000889 atomisation Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- Treating Waste Gases (AREA)
Abstract
Description
技术领域technical field
本实用新型涉及一种化工酸雾废气处理设备。The utility model relates to a chemical acid mist waste gas treatment equipment.
背景技术Background technique
酸雾,通常是指雾状的酸类物质。在空气中酸雾的颗粒很小,比水雾的颗粒要小,比烟的湿度要高,粒径为0.1~10μm,是介于烟气与水雾之间的物质,具有较强的腐蚀性。目前酸雾废气的处理中,成本较低的即为液体吸收法,采用吸收液体对酸雾废气进行中和吸收,传统的采用将废气直接通过吸收池内,由于气体间的聚集,酸雾废气粒子不能与吸收剂充分的接触,吸收效果较差。Acid mist, usually refers to mist-like acid substances. The particles of acid mist in the air are very small, smaller than those of water mist, and the humidity is higher than that of smoke. The particle size is 0.1-10 μm. sex. At present, in the treatment of acid mist waste gas, the lower cost is the liquid absorption method. The absorption liquid is used to neutralize and absorb the acid mist waste gas. The traditional method is to pass the waste gas directly through the absorption tank. Can not fully contact with the absorbent, the absorption effect is poor.
实用新型内容Utility model content
本实用新型的目的在于克服现有技术中存在的上述不足,而提供一种结构设计合理的化工酸雾废气处理设备。The purpose of this utility model is to overcome the above-mentioned deficiencies in the prior art, and to provide a chemical acid mist waste gas treatment equipment with a reasonable structure design.
本实用新型解决上述问题所采用的技术方案是:一种化工酸雾废气处理设备,包括处理腔体、喷雾机构以及折流层,所述的折流层由若干折流盘自上而下依次等距间隔构成,所述的折流盘的上端面呈沿外侧向下倾斜设置,所述的喷雾机构包括通液轴以及通液盘,所述的通液盘依次间隔套设固定在通液轴上,所述的通液盘的外沿设置在相邻的折流盘的间隙上,所述的通液盘与通液轴的中空腔体连通,所述的通液盘设置在折流盘的间隙的部分上下端面设置有若干喷头,所述的通液盘的外沿端面与折流盘的端面平行设置,所述的通液轴与处理腔体的吸收剂入口连通,所述的处理腔体底部设置有废气进口以及回收液出口,所述的处理腔体顶部设置有废气出口,所述的折流盘设置有填料槽,所述的填料槽内填充设置有吸收填料,所述的填料槽的底部排布设置有若干通孔。The technical scheme adopted by the utility model to solve the above problems is: a chemical acid mist waste gas treatment equipment, including a treatment cavity, a spray mechanism and a baffle layer, the baffle layer is composed of several baffle plates in order from top to bottom Equidistant interval structure, the upper end surface of the baffle plate is inclined downward along the outer side, the spray mechanism includes a liquid-passing shaft and a liquid-passing disc, and the liquid-passing disc is sleeved and fixed on the liquid-passing disc in sequence. On the shaft, the outer edge of the liquid-passing disc is arranged on the gap between the adjacent baffle discs, the liquid-passing disc is communicated with the hollow cavity of the liquid-passing shaft, and the liquid-passing disc is arranged on the baffle plate. The upper and lower end faces of the gap of the disc are provided with a number of spray heads, the outer edge end face of the liquid passage disc is arranged in parallel with the end face of the baffle disc, the liquid passage shaft is communicated with the absorbent inlet of the processing cavity, and the A waste gas inlet and a recovery liquid outlet are arranged at the bottom of the treatment cavity, a waste gas outlet is arranged at the top of the treatment cavity, a packing groove is arranged on the baffle plate, and an absorption filler is filled in the filling groove, and the absorbing filler is arranged in the filling groove. The bottom of the packing groove is arranged with a number of through holes.
进一步的:所述的吸收填料采用陶瓷多孔球。Further: the absorbing filler adopts ceramic porous balls.
进一步的:所述的通液轴下端与驱动电机的输出轴固定连接,转动座的槽位内设置有轴承,所述的轴承的外圈与槽位的壁面固定,轴承的内圈与通液轴的外壁面固定,所述的槽位设置有通气孔,使得吸收剂入口与通液轴的中空腔体连通。Further: the lower end of the liquid-passing shaft is fixedly connected with the output shaft of the driving motor, a bearing is arranged in the groove of the rotating seat, the outer ring of the bearing is fixed with the wall surface of the groove, and the inner ring of the bearing is connected with the liquid-passing shaft. The outer wall surface of the shaft is fixed, and the slot is provided with a ventilation hole, so that the absorbent inlet is communicated with the hollow cavity of the liquid-passing shaft.
进一步的:所述的处理腔体设置有设备支撑架上。Further: the processing chamber is provided on an equipment support frame.
进一步的:所述的处理腔体包括主机壳体以及上盖,所述的主机壳体与上盖通过法兰盘配合连接并通过螺栓件固定。Further: the processing chamber includes a mainframe casing and an upper cover, and the mainframe casing and the upper cover are cooperatively connected by a flange plate and fixed by bolts.
进一步的:所述的喷头采用雾化喷头。Further: the spray head adopts atomization spray head.
进一步的:所述的处理腔体的内壁面采用复合玻璃钢。Further: the inner wall surface of the processing cavity is made of composite glass fiber reinforced plastic.
本实用新型与现有技术相比,具有以下优点和效果:结构设计合理,通过多层折流盘的设计,对气流进行有效的缓冲,减小废气与吸收液作用的轴向长度,即有效减少设备的高度以及体积,提高气体与雾化的吸收液的中和吸收效果,通过通液盘的转动,进一步提高气流的扰动,提高中和吸收效果,同时本结构在折流板设置有陶瓷多孔球,陶瓷多孔球具有良好的耐腐蚀性,化学性能稳定,在多孔球内可有效滞留吸收液,在气流上升经过多孔球,经由若干多孔球形成的间隙与吸收液进行充分接触,保证了吸收的效果。Compared with the prior art, the utility model has the following advantages and effects: the structure design is reasonable, the air flow is effectively buffered through the design of the multi-layer baffle plate, and the axial length of the interaction between the exhaust gas and the absorbing liquid is reduced, that is, the effective Reduce the height and volume of the equipment, improve the neutralization and absorption effect of the gas and the atomized absorption liquid, and further improve the disturbance of the airflow and the neutralization absorption effect through the rotation of the liquid-passing plate. Porous balls, ceramic porous balls have good corrosion resistance and stable chemical properties. The absorbing liquid can be effectively retained in the porous balls. When the airflow rises through the porous balls, the gaps formed by several porous balls are fully contacted with the absorbing liquid to ensure that the absorbing liquid is fully contacted. absorption effect.
附图说明Description of drawings
图1是本实用新型实施例化工酸雾废气处理设备的结构示意图。FIG. 1 is a schematic structural diagram of a chemical acid mist waste gas treatment equipment according to an embodiment of the present invention.
图2是本实用新型实施例化工酸雾废气处理设备的横截面示意图。2 is a schematic cross-sectional view of the chemical acid mist waste gas treatment equipment according to the embodiment of the present invention.
图3是本实用新型实施例陶瓷多孔球的结构示意图。3 is a schematic structural diagram of a ceramic porous ball according to an embodiment of the present invention.
附图编号:处理腔体1,折流盘2,通液轴31,通液盘32,喷头33,吸收剂入口11,废气进口12,回收液出口13,废气出口14,填料槽21,吸收填料22,驱动电机34,转动座35,轴承36,通气孔37,设备支撑架4,主机壳体11,上盖12,法兰盘13,多孔球221。Drawing number:
具体实施方式Detailed ways
下面结合附图并通过实施例对本实用新型作进一步的详细说明,以下实施例是对本实用新型的解释而本实用新型并不局限于以下实施例。The present utility model will be further described in detail below with reference to the accompanying drawings and the embodiments. The following embodiments are the explanations of the present utility model and the present utility model is not limited to the following embodiments.
参见图1-图3,本实施例一种化工酸雾废气处理设备,包括处理腔体1、喷雾机构以及折流层,所述的折流层由若干折流盘2自上而下依次等距间隔构成,所述的折流盘2的上端面呈沿外侧向下倾斜设置,所述的喷雾机构包括通液轴31以及通液盘32,所述的通液盘32依次间隔套设固定在通液轴31上,所述的通液盘32的外沿设置在相邻的折流盘2的间隙上,所述的通液盘32与通液轴31的中空腔体连通,所述的通液盘32设置在折流盘2的间隙的部分上下端面设置有若干喷头33,所述的通液盘32的外沿端面与折流盘2的端面平行设置,所述的通液轴31与处理腔体1的吸收剂入口11连通,所述的处理腔体1底部设置有废气进口12以及回收液出口13,所述的处理腔体1顶部设置有废气出口14,所述的折流盘2设置有填料槽21,所述的填料槽21内填充设置有吸收填料22,所述的填料槽21 的底部排布设置有若干通孔,所述的吸收填料22采用陶瓷多孔球221,所述的喷头33采用雾化喷头33,本实施例涉及的一种化工酸雾废气处理设备,结构设计合理,将吸收液通过泵体输入通过通液轴31,在经由通液盘32的喷头33喷出液体,其中具体的喷头33采用雾化喷头33提高与废气的接触效果,本实施例中多层折流盘2的设计,对气流进行有效的缓冲,减小废气与吸收液作用的轴向长度,即有效减少设备的高度以及体积,提高气体与雾化的吸收液的中和吸收效果,同时本结构在折流板设置有陶瓷多孔球221,陶瓷多孔球221 具有良好的耐腐蚀性,化学性能稳定,在多孔球221内可有效滞留吸收液,在气流上升经过多孔球221,经由若干多孔球221形成的间隙与吸收液进行充分接触,保证了吸收的效果。Referring to Figures 1 to 3, a chemical acid mist waste gas treatment equipment in this embodiment includes a
同时本实施例中所述的通液轴31下端与驱动电机34的输出轴固定连接,转动座35的槽位内设置有轴承36,所述的轴承36的外圈与槽位的壁面固定,轴承36的内圈与通液轴31的外壁面固定,所述的槽位设置有通气孔37,使得吸收剂入口11与通液轴31的中空腔体连通,本实施例中通过通液盘32的转动,进一步提高气流的扰动,提高中和吸收效果,所述的处理腔体1设置有设备支撑架4上,所述的处理腔体1包括主机壳体11以及上盖12,所述的主机壳体11与上盖12通过法兰盘13配合连接并通过螺栓件固定,便于检修与设备安装,所述的处理腔体1的内壁面采用复合玻璃钢。At the same time, the lower end of the liquid-passing
本说明书中所描述的以上内容仅仅是对本实用新型所作的举例说明。本实用新型所属技术领域的技术人员可以对所描述的具体实施例做各种各样的修改或补充或采用类似的方式替代,只要不偏离本实用新型说明书的内容或者超越本权利要求书所定义的范围,均应属于本实用新型的保护范围。The above content described in this specification is only an illustration of the present invention. Those skilled in the art to which the present utility model belongs can make various modifications or supplements to the described specific embodiments or substitute in similar manners, as long as they do not deviate from the contents of the present utility model description or exceed the definitions in the claims The scope of the invention should belong to the protection scope of the present invention.
Claims (7)
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| CN201922166293.1U CN211837205U (en) | 2019-12-05 | 2019-12-05 | Chemical acid mist waste gas treatment equipment |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114870593A (en) * | 2022-04-07 | 2022-08-09 | 宜兴市苏哈电力设备有限公司 | Environment-friendly oxidation treatment device for wet flue gas desulfurization and denitrification |
| CN115282754A (en) * | 2022-07-11 | 2022-11-04 | 安徽昊源化工集团有限公司 | Organic waste gas treatment device in chemical production |
-
2019
- 2019-12-05 CN CN201922166293.1U patent/CN211837205U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114870593A (en) * | 2022-04-07 | 2022-08-09 | 宜兴市苏哈电力设备有限公司 | Environment-friendly oxidation treatment device for wet flue gas desulfurization and denitrification |
| CN115282754A (en) * | 2022-07-11 | 2022-11-04 | 安徽昊源化工集团有限公司 | Organic waste gas treatment device in chemical production |
| CN115282754B (en) * | 2022-07-11 | 2024-03-22 | 安徽昊源化工集团有限公司 | Organic waste gas treatment device in chemical production |
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Granted publication date: 20201103 Termination date: 20211205 |