CN205308119U - Acid mist absorption tower - Google Patents
Acid mist absorption tower Download PDFInfo
- Publication number
- CN205308119U CN205308119U CN201620014851.6U CN201620014851U CN205308119U CN 205308119 U CN205308119 U CN 205308119U CN 201620014851 U CN201620014851 U CN 201620014851U CN 205308119 U CN205308119 U CN 205308119U
- Authority
- CN
- China
- Prior art keywords
- tower body
- packing layer
- porous spherical
- spherical packing
- tower
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Gas Separation By Absorption (AREA)
Abstract
The utility model discloses a following technology, an acid mist absorption tower, its characterized in that: the tower body is hollow cylindrical glass steel, tower body bottom central point puts the row's of being provided with cinder notch, arrange the cinder notch and connect the water sealed tank, tower body top central point puts and is provided with out the steam ports, the inside crisscross a plurality of showers that are provided with of tower body, be provided with a plurality of nozzles on the shower downwards, tower body upper portion is provided with the defroster, upper portion is provided with porous spherical packing layer in the tower body, the inside level of porous spherical packing layer is provided with a plurality of pivots, the symmetry is provided with the paddle in the pivot, porous spherical packing layer right side is provided with driving motor, be connected through the chain between driving motor and the pivot, tower body left side bottom is provided with the steam inlet, the equipment structure is rationally normal, high durability and convenient use, can the effectual velocity of flow that reduces the acid mist through multi -level modular design, have and well get rid of the effect.
Description
Technical field
This utility model relates to utilizing gas-to-liquid contact field in separation in method or apparatus physically or chemically general in operation, espespecially a kind of acid fog absorption tower.
Background technology
Refine in the process of germanium in wet method, it is that the chlorinated distillation of thick germanium tetrachloride or the distillation process of pure germanium tetrachloride all can produce substantial amounts of acid mist gas, in the hydrolysis reaction of germanium tetrachloride, also can produce a certain amount of acid mist gas simultaneously, these acid mist gases generally adopt acid mist purifying tower to its absorption cleaning, but existing acid mist purifying tower, generally adopt the alkali liquor shower being crisscross arranged that the acid mist gas entering tower body is sprayed, owing to extracting or in distillation process at the thick of germanium tetrachloride, owing to temperature is significantly high, cause acid mist flow velocity quickly, simple spray is extremely difficult to removal effect well.
Summary of the invention
In order to solve above-mentioned technical problem, this utility model provides a kind of acid fog absorption tower, and this device structure reasonable standard is easy to use, can be effectively reduced the flow velocity of acid mist by multi-level modular design, have removal effect well.
For reaching above-mentioned purpose, this utility model adopts techniques below to realize, a kind of acid fog absorption tower, including tower body, shower, nozzle, porous spherical packing layer, drive motor, rotating shaft, blade, air intake, venthole, it is characterized in that: tower body is the cylindrical glass steel of hollow, tower body bottom centre position is provided with slag-drip opening, slag-drip opening connects water sealed tank, tower body top center is provided with venthole, tower body alternate internal is provided with some showers, to being arranged with some nozzles on shower, tower body top is provided with demister, tower body middle and upper part is provided with porous spherical packing layer, porous spherical packing layer inner horizontal is provided with some rotating shafts, rotating shaft is symmetrically arranged with some blades, it is provided with drive motor on the right side of porous spherical packing layer, it is connected by chain between drive motor with rotating shaft, tower body left bottom is provided with air intake.
As further improvement of the utility model, being provided with some corrugated platings in the middle part of described tower body, tower body middle and lower part is provided with ceramic packing layer, is respectively arranged with flow pipe in the middle part of corrugated plating, ceramic packing layer, being provided with circulating pump on flow pipe, the other end of flow pipe connects water sealed tank.
As further improvement of the utility model, between described tower body inner ceramic packing layer and slag-drip opening, it is provided with heat exchanger.
As further improvement of the utility model, described air intake lower end is U-shaped section, and U-shaped section of middle part connects water sealed tank by connecting tube.
Operation principle of the present utility model:
This utility model provides a kind of acid fog absorption tower, this device structure reasonable standard, easy to use, by the shower being crisscross arranged, akaline liquid is sprayed inside tower body, neutralization can be effectively formed, the design of porous spherical packing layer simultaneously can effectively increase the contact area between alkali liquor and sour gas and time of contact, increase reaction therebetween fully, porous spherical packing layer is internally provided with rotating blade, timely and effectively the liquid saved bit by bit inside porous spherical packing layer can be got rid of, strengthen the reaction effect of porous spherical packing layer, pass through circulating pump simultaneously, ceramic packing layer, the alkali liquor on water sealed tank top can effectively be used by the modular design of corrugated plating, reach the recycling of alkali liquor, ceramic packing layer and corrugated plating can effectively reduce the flowing velocity of sour gas simultaneously, it is effectively increased contacting between alkali liquor with sour gas, the design of heat exchanger simultaneously can effectively reduce the energy of sour gas, reduce its flow velocity, moisture barrier in acid gas effectively can be formed liquid and be flowed into inside water sealed tank by the design of U-shaped section of air intake simultaneously, the steam neutralizing reaction release can be effectively removed in the design of demister.
This utility model compared with prior art has the advantages that:
1, this utility model provides a kind of acid fog absorption tower, this device structure reasonable standard, easy to use, by the shower being crisscross arranged, akaline liquid is sprayed inside tower body, neutralization can be effectively formed, the design of porous spherical packing layer simultaneously can effectively increase the contact area between alkali liquor and sour gas and time of contact, increase reaction therebetween fully, porous spherical packing layer is internally provided with rotating blade, timely and effectively the liquid saved bit by bit inside porous spherical packing layer can be got rid of, strengthen the reaction effect of porous spherical packing layer,
2, pass through circulating pump simultaneously, ceramic packing layer, the alkali liquor on water sealed tank top can effectively be used by the modular design of corrugated plating, reach the recycling of alkali liquor, ceramic packing layer and corrugated plating can effectively reduce the flowing velocity of sour gas simultaneously, it is effectively increased contacting between alkali liquor with sour gas, the design of heat exchanger simultaneously can effectively reduce the energy of sour gas, reduce its flow velocity, moisture barrier in acid gas effectively can be formed liquid and be flowed into inside water sealed tank by the design of U-shaped section of air intake simultaneously, the steam neutralizing reaction release can be effectively removed in the design of demister.
Accompanying drawing explanation
Fig. 1 is a kind of acid fog absorption tower structural representation;
Fig. 2 is porous spherical packing layer enlarged drawing set by a kind of acid fog absorption tower;
1-porous spherical packing layer in figure; 2-rotating shaft; 3-corrugated plating; 4-flow pipe; 5-air intake; 6-U type section; 7-connecting tube; 8-slag-drip opening; 9-water sealed tank; 10-circulating pump; 11-heat exchanger; 12-ceramic packing layer; 13-tower body; 14-nozzle; 15-drive motor; 16-blade; 17-shower; 18-demister; 19-venthole.
Detailed description of the invention
Below in conjunction with accompanying drawing, the invention will be further described:
Such as Fig. 1, a kind of acid fog absorption tower shown in Fig. 2, including tower body 13, shower 17, nozzle 14, porous spherical packing layer 1, drive motor 15, rotating shaft 2, blade 16, air intake 5, venthole 19, it is characterized in that: tower body 13 is the cylindrical glass steel of hollow, tower body 13 bottom centre position is provided with slag-drip opening 8, slag-drip opening 8 connects water sealed tank 9, tower body 13 top center is provided with venthole 19, tower body 13 alternate internal is provided with some showers 17, to being arranged with some nozzles 14 on shower 17, tower body 13 top is provided with demister 18, tower body 13 middle and upper part is provided with porous spherical packing layer 1, porous spherical packing layer 1 inner horizontal is provided with some rotating shafts 2, rotating shaft 2 is symmetrically arranged with some blades 16, drive motor 15 it is provided with on the right side of porous spherical packing layer 1, it is connected by chain between drive motor 15 with rotating shaft 2, tower body 13 left bottom is provided with air intake 5, some corrugated platings 3 it are provided with in the middle part of described tower body 13, tower body 13 middle and lower part is provided with ceramic packing layer 12, corrugated plating 3, flow pipe 4 it is respectively arranged with in the middle part of ceramic packing layer 12, flow pipe 4 is provided with circulating pump 10, the other end of flow pipe 4 connects water sealed tank 9, it is provided with heat exchanger 11 between described tower body 13 inner ceramic packing layer 12 and slag-drip opening 8, described air intake 5 lower end is U-shaped section 6, water sealed tank 9 is connected by connecting tube 7 in the middle part of U-shaped section 6, this utility model provides a kind of acid fog absorption tower, this device structure reasonable standard, easy to use, by the shower being crisscross arranged, akaline liquid is sprayed inside tower body, neutralization can be effectively formed, the design of porous spherical packing layer simultaneously can effectively increase the contact area between alkali liquor and sour gas and time of contact, increase reaction therebetween fully, porous spherical packing layer is internally provided with rotating blade, timely and effectively the liquid saved bit by bit inside porous spherical packing layer can be got rid of, strengthen the reaction effect of porous spherical packing layer, pass through circulating pump simultaneously, ceramic packing layer, the alkali liquor on water sealed tank top can effectively be used by the modular design of corrugated plating, reach the recycling of alkali liquor, ceramic packing layer and corrugated plating can effectively reduce the flowing velocity of sour gas simultaneously, it is effectively increased contacting between alkali liquor with sour gas, the design of heat exchanger simultaneously can effectively reduce the energy of sour gas, reduce its flow velocity, moisture barrier in acid gas effectively can be formed liquid and be flowed into inside water sealed tank by the design of U-shaped section of air intake simultaneously, the steam neutralizing reaction release can be effectively removed in the design of demister.
Claims (4)
1. an acid fog absorption tower, including tower body (13), shower (17), nozzle (14), porous spherical packing layer (1), drive motor (15), rotating shaft (2), blade (16), air intake (5), venthole (19), it is characterized in that: the cylindrical glass steel that tower body (13) is hollow, tower body (13) bottom centre position is provided with slag-drip opening (8), slag-drip opening (8) connects water sealed tank (9), tower body (13) top center is provided with venthole (19), tower body (13) alternate internal is provided with some showers (17), to being arranged with some nozzles (14) on shower (17), tower body (13) top is provided with demister (18), tower body (13) middle and upper part is provided with porous spherical packing layer (1), porous spherical packing layer (1) inner horizontal is provided with some rotating shafts (2), rotating shaft (2) is symmetrically arranged with some blades (16), porous spherical packing layer (1) right side is provided with drive motor (15), it is connected by chain between drive motor (15) with rotating shaft (2), tower body (13) left bottom is provided with air intake (5).
2. a kind of acid fog absorption tower according to claim 1, it is characterized in that: described tower body (13) middle part is provided with some corrugated platings (3), tower body (13) middle and lower part is provided with ceramic packing layer (12), corrugated plating (3), ceramic packing layer (12) middle part is respectively arranged with flow pipe (4), being provided with circulating pump (10) on flow pipe (4), the other end of flow pipe (4) connects water sealed tank (9).
3. a kind of acid fog absorption tower according to claim 2, it is characterised in that: it is provided with heat exchanger (11) between described tower body (13) inner ceramic packing layer (12) and slag-drip opening (8).
4. a kind of acid fog absorption tower according to claim 3, it is characterised in that: described air intake (5) lower end is U-shaped section (6), and U-shaped section (6) middle part connects water sealed tank (9) by connecting tube (7).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620014851.6U CN205308119U (en) | 2016-01-08 | 2016-01-08 | Acid mist absorption tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620014851.6U CN205308119U (en) | 2016-01-08 | 2016-01-08 | Acid mist absorption tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205308119U true CN205308119U (en) | 2016-06-15 |
Family
ID=56201154
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620014851.6U Active CN205308119U (en) | 2016-01-08 | 2016-01-08 | Acid mist absorption tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205308119U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107198945A (en) * | 2017-08-06 | 2017-09-26 | 长沙善道新材料科技有限公司 | A kind of energy saving and environment friendly desulfurization removing nitric mercury removal device for power plant |
| CN109893982A (en) * | 2017-12-07 | 2019-06-18 | 孙兵 | A kind of efficient denitrifying device for pulverized-coal fired boiler |
| CN110772956A (en) * | 2019-10-10 | 2020-02-11 | 武汉云晶飞光纤材料有限公司 | Rectified germanium tetrachloride tail gas absorption device |
| CN114653085A (en) * | 2022-03-07 | 2022-06-24 | 广东长信精密设备有限公司 | Germanium tetrachloride production device and method |
-
2016
- 2016-01-08 CN CN201620014851.6U patent/CN205308119U/en active Active
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107198945A (en) * | 2017-08-06 | 2017-09-26 | 长沙善道新材料科技有限公司 | A kind of energy saving and environment friendly desulfurization removing nitric mercury removal device for power plant |
| CN107198945B (en) * | 2017-08-06 | 2020-06-26 | 西安旭旌再生资源有限公司 | Energy-saving environment-friendly desulfurization denitrification demercuration device for power plant |
| CN109893982A (en) * | 2017-12-07 | 2019-06-18 | 孙兵 | A kind of efficient denitrifying device for pulverized-coal fired boiler |
| CN110772956A (en) * | 2019-10-10 | 2020-02-11 | 武汉云晶飞光纤材料有限公司 | Rectified germanium tetrachloride tail gas absorption device |
| CN114653085A (en) * | 2022-03-07 | 2022-06-24 | 广东长信精密设备有限公司 | Germanium tetrachloride production device and method |
| CN114653085B (en) * | 2022-03-07 | 2023-12-01 | 广东长信精密设备有限公司 | Germanium tetrachloride production device and method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205308119U (en) | Acid mist absorption tower | |
| CN106422727A (en) | Full-automatic purification device for laboratory acid mist exhaust gas | |
| CN105617847B (en) | A kind of eddy flow coupling depth desulfurization reinforced module | |
| CN101642670B (en) | Rotational flow dust-removing desulfurization unit | |
| CN206184241U (en) | Full automatically cleaned device of laboratory acid mist waste gas | |
| CN106492614A (en) | A kind of wet purification method of acidic flue gas and device | |
| CN202427338U (en) | Glass fiber reinforced plastic acid gas purifying tower | |
| CN207546180U (en) | A kind of waste gas cleaning system | |
| CN102580504A (en) | Novel ammonia desulphurization absorption device | |
| CN202506306U (en) | Novel ammonia process desulfurization absorption device | |
| CN201244439Y (en) | Glass melting furnace flue gas desulfurization and dedusting integrated device | |
| CN208839362U (en) | A kind of fibreglass epoxy acid mist purifying column | |
| CN216440325U (en) | Water washing tower | |
| CN109364698A (en) | A kind of packed absorber | |
| CN205953577U (en) | A reaction tower for handling desulfurization waste water | |
| CN213492888U (en) | Contain sour high temperature tail gas treatment system | |
| CN209254448U (en) | A kind of packed absorber | |
| CN208626955U (en) | Flue gas washing system | |
| CN208771165U (en) | A kind of antiseep high temperature waste gas containing fluoride processing unit | |
| CN207254092U (en) | Flue gas removes fog cooling apparatus | |
| CN205556101U (en) | Conversion system of sulphuric acid technology | |
| CN205627582U (en) | Novel module is reinforceed in desulfurization of whirl coupling degree of depth | |
| CN211753863U (en) | Spray type flue gas desulfurization tower | |
| CN214261237U (en) | Flue gas desulfurization and dust removal device for calcining furnace | |
| CN218981083U (en) | High-efficient desulfurizing tower |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190610 Address after: 412000 Tianyi Science and Technology City A5, Tianyuan District, Zhuzhou City, Hunan Province Patentee after: Zhuzhou Torch Antai New Materials Co., Ltd. Address before: 650300 Baita Village, Hot Spring Town, Anning City, Kunming City, Yunnan Province Patentee before: KUIMING HUIQUAN GAOCHUN SEMICONDUCTOR MATERIAL CO., LTD. |
|
| TR01 | Transfer of patent right |