CN218741156U - Hydrogen fluoride tail gas absorption device - Google Patents
Hydrogen fluoride tail gas absorption device Download PDFInfo
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- CN218741156U CN218741156U CN202223405470.5U CN202223405470U CN218741156U CN 218741156 U CN218741156 U CN 218741156U CN 202223405470 U CN202223405470 U CN 202223405470U CN 218741156 U CN218741156 U CN 218741156U
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- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 title claims abstract description 44
- 229910000040 hydrogen fluoride Inorganic materials 0.000 title claims abstract description 40
- 239000007789 gas Substances 0.000 title claims abstract description 30
- 238000010521 absorption reaction Methods 0.000 title claims description 18
- 238000006243 chemical reaction Methods 0.000 claims abstract description 33
- -1 polytetrafluoroethylene Polymers 0.000 claims abstract description 23
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims abstract description 21
- 239000004810 polytetrafluoroethylene Substances 0.000 claims abstract description 21
- 238000003756 stirring Methods 0.000 claims abstract description 20
- 238000001816 cooling Methods 0.000 claims description 21
- 238000001035 drying Methods 0.000 claims description 15
- 229910052751 metal Inorganic materials 0.000 claims description 15
- 239000002184 metal Substances 0.000 claims description 15
- 239000007787 solid Substances 0.000 abstract description 13
- 239000002912 waste gas Substances 0.000 abstract description 12
- 238000001179 sorption measurement Methods 0.000 abstract description 9
- 238000012423 maintenance Methods 0.000 abstract description 4
- 239000002594 sorbent Substances 0.000 abstract 3
- 238000010009 beating Methods 0.000 abstract 2
- 230000001174 ascending effect Effects 0.000 abstract 1
- 239000000463 material Substances 0.000 abstract 1
- 239000003463 adsorbent Substances 0.000 description 11
- 238000000034 method Methods 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 238000000746 purification Methods 0.000 description 4
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 229910010272 inorganic material Inorganic materials 0.000 description 2
- 239000011147 inorganic material Substances 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000011368 organic material Substances 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 241001465754 Metazoa Species 0.000 description 1
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 239000000809 air pollutant Substances 0.000 description 1
- 231100001243 air pollutant Toxicity 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 238000006115 defluorination reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000009628 steelmaking Methods 0.000 description 1
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Abstract
Description
技术领域technical field
本实用新型涉及废气处理技术领域,尤其涉及氟化氢尾气吸收装置。The utility model relates to the technical field of waste gas treatment, in particular to a hydrogen fluoride tail gas absorption device.
背景技术Background technique
氟化氢废气其主要来源于冶金工业的铝电解和炼钢过程,氟化氢废气对动植物危害很大,是有害的空气污染物,因此,氟化氢废气必须在吸收净化后才可排放至大气中。Hydrogen fluoride waste gas mainly comes from the aluminum electrolysis and steelmaking processes in the metallurgical industry. Hydrogen fluoride waste gas is very harmful to animals and plants and is a harmful air pollutant. Therefore, hydrogen fluoride waste gas must be absorbed and purified before it can be discharged into the atmosphere.
如中国专利号为:CN210385463U的“一种制备氟化氢尾气吸收装置”,包括尾气处理箱,尾气处理箱的内部设置有反应仓,尾气处理箱的顶面设置有驱动电机,驱动电机的下端驱动轴上设置有搅拌板,搅拌板处于反应仓的内部,且驱动电机的下端驱动轴插接在限位件的内部,限位件固定在反应仓的内壁上,反应仓的底面设置有排污阀管,且尾气处理箱的内壁上设置有过滤板,过滤板处于反应仓的上方。For example, the Chinese patent number is: CN210385463U "A device for preparing hydrogen fluoride tail gas absorption", including a tail gas treatment box, the inside of the tail gas treatment box is provided with a reaction chamber, the top surface of the tail gas treatment box is provided with a drive motor, and the lower end of the drive motor drives the shaft There is a stirring plate on the top, the stirring plate is inside the reaction chamber, and the drive shaft at the lower end of the drive motor is plugged into the inside of the limiter, the limiter is fixed on the inner wall of the reaction chamber, and the bottom surface of the reaction chamber is provided with a drain valve tube , and a filter plate is arranged on the inner wall of the exhaust gas treatment box, and the filter plate is located above the reaction chamber.
但是现有技术中,氢氟酸能腐蚀金属、含硅的有机或无机材料,在吸收氟化氢的反应仓内设置连接有驱动电机的驱动轴,极易在使用过程中被腐蚀而损坏,不仅影响净化吸收效率,还会增大设备的日常养护成本。However, in the prior art, hydrofluoric acid can corrode metals, silicon-containing organic or inorganic materials, and the drive shaft connected to the drive motor is installed in the reaction chamber for absorbing hydrogen fluoride, which is very easy to be corroded and damaged during use, which not only affects The efficiency of purification and absorption will also increase the daily maintenance cost of equipment.
实用新型内容Utility model content
本实用新型的目的是为了解决现有的技术中存在的氢氟酸能腐蚀金属、含硅的有机或无机材料,在吸收氟化氢的反应仓内设置连接有驱动电机的驱动轴,极易在使用过程中被腐蚀而损坏,不仅影响净化吸收效率,还会增大设备的日常养护成本的问题,而提出的氟化氢尾气吸收装置。The purpose of this utility model is to solve the problem that hydrofluoric acid can corrode metals, silicon-containing organic or inorganic materials in the existing technology. A drive shaft connected to a drive motor is installed in the reaction chamber for absorbing hydrogen fluoride, which is very easy to use. Corrosion and damage during the process will not only affect the purification and absorption efficiency, but also increase the daily maintenance cost of the equipment, so the proposed hydrogen fluoride tail gas absorption device.
为了实现上述目的,本实用新型采用了如下技术方案:氟化氢尾气吸收装置,包括设备钣金,所述设备钣金的内侧固定安装有聚四氟乙烯罐,且聚四氟乙烯罐顶端内侧固定安装有干燥仓壳件,所述聚四氟乙烯罐顶部设有反应仓,且聚四氟乙烯罐底部设有冷却仓,所述冷却仓内固定安装有涡卷导入管,所述反应仓内活动安装有气动搅拌件,且反应仓顶部均匀固定插接有多个斜置增压管,所述反应仓内侧开设有滑槽,所述气动搅拌件包括环件,所述环件的外侧与滑槽滑动连接,且环件顶部均匀焊接有多个斜置板,所述环件底部均匀焊接有多个搅拌叶。In order to achieve the above purpose, the utility model adopts the following technical scheme: hydrogen fluoride exhaust gas absorption device, including equipment sheet metal, the inner side of the equipment sheet metal is fixedly installed with a polytetrafluoroethylene tank, and the inner side of the top of the polytetrafluoroethylene tank is fixedly installed There is a dry chamber shell, the top of the polytetrafluoroethylene tank is provided with a reaction chamber, and the bottom of the polytetrafluoroethylene tank is provided with a cooling chamber, and a scroll inlet pipe is fixedly installed in the cooling chamber. Pneumatic stirring parts are installed, and the top of the reaction chamber is uniformly fixed and connected with a plurality of oblique pressurization pipes. A chute is opened inside the reaction chamber. The grooves are slidingly connected, and the top of the ring is evenly welded with a plurality of inclined plates, and the bottom of the ring is evenly welded with a plurality of stirring blades.
优选的,所述环件外侧均匀转动安装有多个滚轴,且每个滚轴外侧均于滑槽内侧滑动连接。Preferably, a plurality of rollers are installed on the outer side of the ring to rotate evenly, and the outer side of each roller is slidingly connected to the inner side of the chute.
优选的,所述涡卷导入管顶端插接于反应仓底部,所述设备钣金顶端固定安装有封盖,且封盖上焊接有输出管。Preferably, the top end of the scroll inlet tube is plugged into the bottom of the reaction chamber, the top end of the sheet metal of the equipment is fixedly equipped with a cover, and an output tube is welded on the cover.
优选的,所述聚四氟乙烯罐上固定安装有空气导入组件,所述空气导入组件包括增压泵、环形管,所述增压泵与环形管相连通,且每个斜置增压管均与环形管相连通。Preferably, an air introduction assembly is fixedly installed on the polytetrafluoroethylene tank, and the air introduction assembly includes a booster pump and an annular pipe, the booster pump communicates with the annular pipe, and each inclined booster pipe All communicate with the ring pipe.
优选的,所述干燥仓壳件外侧底部均匀开设有多个通孔,且干燥仓壳件底端相连通有底管。Preferably, a plurality of through holes are uniformly opened on the outer bottom of the drying case, and the bottom end of the drying case is connected to a bottom pipe.
优选的,所述底管底端与冷却仓相连通,且冷却仓底端相连通有卸料管,所述卸料管上安装有阀门。Preferably, the bottom end of the bottom pipe is connected to the cooling bin, and the bottom end of the cooling bin is connected to a discharge pipe, and a valve is installed on the discharge pipe.
优选的,所述环形管的外壁与设备钣金通过螺栓固定安装。Preferably, the outer wall of the annular pipe and the equipment sheet metal are fixed and installed by bolts.
与现有技术相比,本实用新型的优点和积极效果在于:Compared with the prior art, the utility model has the advantages and positive effects that:
1、本实用新型中,斜置增压管将外界空气导入反应仓内,从上至下的空气不仅能与向上的氟化氢废气对流,使得氟化氢气体压至固体吸附剂中进行吸附处理,且从上至下的空气还能通过多个斜置板推动环件旋转,从而使得多个搅拌叶对固体吸附剂进行搅动,提升其吸附效率,搅动固体吸附剂无需增设驱动电机,并且聚四氟乙烯罐、干燥仓壳件、气动搅拌件均由不会被氟化氢腐蚀的聚四氟乙烯材质制成,避免了转轴被腐蚀损坏,增大维修频率的问题。1. In the utility model, the oblique pressurized pipe introduces the external air into the reaction chamber, and the air from top to bottom can not only convect with the upward hydrogen fluoride waste gas, but also press the hydrogen fluoride gas into the solid adsorbent for adsorption treatment, and from The air from top to bottom can also push the ring to rotate through multiple inclined plates, so that multiple stirring blades can stir the solid adsorbent to improve its adsorption efficiency. There is no need to add a drive motor to stir the solid adsorbent, and the polytetrafluoroethylene The tank, drying chamber shell, and pneumatic stirring parts are all made of polytetrafluoroethylene that will not be corroded by hydrogen fluoride, which avoids the problem of corrosion damage to the rotating shaft and increased maintenance frequency.
2、本实用新型中,被净化过的气体通过多个通孔导入至干燥腔内,且底管可将干燥空气所产生的水分导入至底部冷却仓内存储,可利用回收的水分进行氟化氢废气的冷却,更加节能环保。2. In this utility model, the purified gas is introduced into the drying chamber through multiple through holes, and the bottom pipe can guide the moisture generated by the drying air into the bottom cooling chamber for storage, and the recovered moisture can be used for hydrogen fluoride waste gas Cooling, more energy saving and environmental protection.
附图说明Description of drawings
图1为本实用新型提出氟化氢尾气吸收装置的剖视立体图;Fig. 1 is the sectional perspective view of hydrogen fluoride tail gas absorption device proposed by the utility model;
图2为本实用新型提出氟化氢尾气吸收装置的剖视正视图;Fig. 2 is the sectional front view of the hydrogen fluoride tail gas absorption device proposed by the utility model;
图3为本实用新型提出氟化氢尾气吸收装置的拆解示意图;Fig. 3 is the dismantling schematic diagram of the hydrogen fluoride tail gas absorption device proposed by the utility model;
图4为本实用新型提出氟化氢尾气吸收装置的气动搅拌件的立体图。Fig. 4 is a perspective view of the pneumatic stirring member of the hydrogen fluoride tail gas absorbing device proposed by the utility model.
图例说明:1、设备钣金;2、封盖;20、输出管;3、涡卷导入管;4、聚四氟乙烯罐;40、冷却仓;41、卸料管;410、阀门;42、反应仓;420、滑槽;5、干燥仓壳件;50、通孔;51、底管;6、空气导入组件;60、环形管;61、斜置增压管;62、增压泵;7、气动搅拌件;70、环件;71、滚轴;72、搅拌叶;73、斜置板。Legend: 1. Equipment sheet metal; 2. Cover; 20. Output pipe; 3. Scroll inlet pipe; 4. Teflon tank; 40. Cooling chamber; 41. Discharge pipe; 410. Valve; 42 , reaction chamber; 420, chute; 5, drying chamber shell; 50, through hole; 51, bottom pipe; 6, air introduction component; 60, annular pipe; ; 7, pneumatic stirring piece; 70, ring piece; 71, roller; 72, stirring blade; 73, inclined plate.
具体实施方式Detailed ways
为了能够更清楚地理解本实用新型的上述目的、特征和优点,下面结合附图和实施例对本实用新型做进一步说明。需要说明的是,在不冲突的情况下,本申请的实施例及实施例中的特征可以相互组合。In order to understand more clearly the above purpose, features and advantages of the utility model, the utility model will be further described below in conjunction with the accompanying drawings and embodiments. It should be noted that, in the case of no conflict, the embodiments of the present application and the features in the embodiments can be combined with each other.
在下面的描述中阐述了很多具体细节以便于充分理解本实用新型,但是,本实用新型还可以采用不同于在此描述的其他方式来实施,因此,本实用新型并不限于下面公开说明书的具体实施例的限制。In the following description, a lot of specific details have been set forth in order to fully understand the utility model, but the utility model can also be implemented in other ways that are different from those described here. Therefore, the utility model is not limited to the specific details of the following disclosure EXAMPLE LIMITATIONS.
请参阅图1-3,本实用新型提供一种技术方案:氟化氢尾气吸收装置,包括设备钣金1,设备钣金1的内侧固定安装有聚四氟乙烯罐4,且聚四氟乙烯罐4顶端内侧固定安装有干燥仓壳件5,聚四氟乙烯罐4顶部设有反应仓42,且聚四氟乙烯罐4底部设有冷却仓40,冷却仓40内固定安装有涡卷导入管3,反应仓42内活动安装有气动搅拌件7,且反应仓42顶部均匀固定插接有多个斜置增压管61,反应仓42内侧开设有滑槽420,气动搅拌件7包括环件70,环件70的外侧与滑槽420滑动连接,且环件70顶部均匀焊接有多个斜置板73,环件70底部均匀焊接有多个搅拌叶72,涡卷导入管3顶端插接于反应仓42底部,设备钣金1顶端固定安装有封盖2,且封盖2上焊接有输出管20;本装置中设有不会被氟化氢所腐蚀的聚四氟乙烯结构,如聚四氟乙烯罐4、干燥仓壳件5、气动搅拌件7,采用吸附净化法取出氟化氢,而吸附净化法是将含氟化氢废气通过装填固体吸附剂进行吸附从而达到除氟的目的,可以采用工业氧化铝、氧化钙和氢氧化钙等作为吸附剂。本装置在使用时,在反应仓4内填充固体吸附剂,在冷却仓40内灌入清水,将氟化氢废气通过涡卷导入管3导入时,首先,将于冷却仓40内被冷却后,从下至上地排入反应仓42内,同时,多个斜置增压管61将外界空气导入反应仓4内,从上至下的空气不仅能与向上的氟化氢废气对流,使得氟化氢气体压至固体吸附剂中进行吸附处理,且从上至下的空气还能通过多个斜置板73推动环件70旋转,从而使得环件70底部的多个搅拌叶72对反应仓4内的固体吸附剂进行搅动,提升其吸附效率,然后,被吸附净化后的空气将向上通过干燥仓壳件5内的活性炭吸附后,由顶部输出管20处排出。Please refer to Figures 1-3, the utility model provides a technical solution: a hydrogen fluoride exhaust gas absorption device, including an equipment sheet metal 1, a polytetrafluoroethylene tank 4 is fixedly installed on the inner side of the equipment sheet metal 1, and the polytetrafluoroethylene tank 4 A
如图4所示,环件70外侧均匀转动安装有多个滚轴71,且每个滚轴71外侧均于滑槽420内侧滑动连接,滚轴71可降低环件70旋转时的摩擦力。As shown in FIG. 4 , a plurality of
如图2和图4所示,聚四氟乙烯罐4上固定安装有空气导入组件6,空气导入组件6包括增压泵62、环形管60,环形管60的外壁与设备钣金1通过螺栓固定安装,增压泵62与环形管60相连通,且每个斜置增压管61均与环形管60相连通,增压泵62吸入外界空气后,由环形管60导入至多个斜置增压管61内,并从反应仓4内向下斜侧喷出。As shown in Figures 2 and 4, an air introduction assembly 6 is fixedly installed on the polytetrafluoroethylene tank 4. The air introduction assembly 6 includes a booster pump 62 and an
如图1、图2和图3所示,干燥仓壳件5外侧底部均匀开设有多个通孔50,且干燥仓壳件5底端相连通有底管51,多个通孔50是用于流通被净化过的气体,底管51可将干燥空气所产生的水分导入至底部冷却仓40内,以利用回收的水分进行氟化氢废气的冷却。As shown in Fig. 1, Fig. 2 and Fig. 3, a plurality of through-
如图1、图2和图3所示,底管51底端与冷却仓40相连通,且冷却仓40底端相连通有卸料管41,卸料管41上安装有阀门410,可通过开启阀门410将冷却仓40内的污水排出。As shown in Fig. 1, Fig. 2 and Fig. 3, the bottom end of the
本装置的使用方法及工作原理:本装置在使用时,在反应仓4内填充固体吸附剂,在冷却仓40内灌入清水,将氟化氢废气通过涡卷导入管3导入时,首先,将于冷却仓40内被冷却后,从下至上地排入反应仓42内,同时,多个斜置增压管61将外界空气导入反应仓4内,从上至下的空气不仅能与向上的氟化氢废气对流,使得氟化氢气体压至固体吸附剂中进行吸附处理,且从上至下的空气还能通过多个斜置板73推动环件70旋转,从而使得环件70底部的多个搅拌叶72对反应仓4内的固体吸附剂进行搅动,提升其吸附效率,然后,被吸附净化后的空气将向上通过干燥仓壳件5内的活性炭吸附后,由顶部输出管20处排出。The use method and working principle of this device: when this device is in use, solid adsorbent is filled in the reaction chamber 4, clear water is poured into the
以上所述,仅是本实用新型的较佳实施例而已,并非是对本实用新型作其它形式的限制,任何熟悉本专业的技术人员可能利用上述揭示的技术内容加以变更或改型为等同变化的等效实施例应用于其它领域,但是凡是未脱离本实用新型技术方案内容,依据本实用新型的技术实质对以上实施例所作的任何简单修改、等同变化与改型,仍属于本实用新型技术方案的保护范围。The above is only a preferred embodiment of the utility model, and is not intended to limit the utility model in other forms. Any skilled person who is familiar with this profession may use the technical content disclosed above to change or remodel it into an equivalent change. The equivalent embodiments are applied to other fields, but any simple modifications, equivalent changes and modifications made to the above embodiments according to the technical essence of the present invention without departing from the content of the technical solution of the present utility model still belong to the technical solution of the present utility model scope of protection.
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CN202223405470.5U CN218741156U (en) | 2022-12-19 | 2022-12-19 | Hydrogen fluoride tail gas absorption device |
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CN202223405470.5U CN218741156U (en) | 2022-12-19 | 2022-12-19 | Hydrogen fluoride tail gas absorption device |
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CN218741156U true CN218741156U (en) | 2023-03-28 |
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CN202223405470.5U Expired - Fee Related CN218741156U (en) | 2022-12-19 | 2022-12-19 | Hydrogen fluoride tail gas absorption device |
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