CN202460441U - Horizontal type spray purification tower - Google Patents
Horizontal type spray purification tower Download PDFInfo
- Publication number
- CN202460441U CN202460441U CN2011204486010U CN201120448601U CN202460441U CN 202460441 U CN202460441 U CN 202460441U CN 2011204486010 U CN2011204486010 U CN 2011204486010U CN 201120448601 U CN201120448601 U CN 201120448601U CN 202460441 U CN202460441 U CN 202460441U
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- spray
- section
- absorber portion
- tower body
- purifying column
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- Treating Waste Gases (AREA)
Abstract
The utility model discloses a horizontal type spray purification tower, comprising a tower body (1), wherein the interior of the tower body (1) is sequentially horizontally provided with an air inlet section (2), at least one group of acid mist absorption section composed of a spray absorption section (3) and a filler absorption section (4), a waterproof section (5), a demisting section (6) and an air outlet section (7); the spray absorption section is provided with a spray system (9), the spray system is provided with multiple nozzles (17), spray directions of the nozzles (17) are consistent with acid gas flowing direction, and the tower body is horizontally placed, thus the acid gas can horizontally pass through the spray purification tower. The horizontal type spray purification tower disclosed by the utility model has higher absorption efficiency; and a horizontal type is adopted, thus the horizontal type spray purification tower is more convenient and flexible to mount.
Description
Technical field
The utility model relates to a kind of equipment for treating industrial waste gas, particularly a kind of absorbing and purifying device of sour gas.
Background technology
In commercial production such as chemical industry, plating, machining; The capital has a large amount of acid mist gas to produce; Thereby contaminated air and environment; Thereby and human body is damaged unhealthful, China is to the legislation of the emission requirement of these industrial waste gases, the regulation industrial waste gas must National standard could discharge.The acid mist treatment facility adopts vertical acid mist purifying column usually at present, and it is when handling sour gas, and the area that the gas-liquid two-phase adverse current makes air-flow greatly reduce hydrojet makes the contact area of gas-liquid two-phase reduce, thereby has reduced the purification efficiency of waste gas; Vertical acid mist purifying column must vertically be placed and also there has been restriction in the place simultaneously, and the equipment that makes is installed underaction.
Summary of the invention
Goal of the invention: to the problem and shortage of above-mentioned existing existence, the utility model provides a kind of absorption efficiency high, easy for installation Horizental showering purifying column.
Technical scheme: in order to reach the foregoing invention purpose; The utility model adopts following technical scheme: a kind of Horizental showering purifying column; Comprise tower body, this tower body inside flatly is provided with wind inlet section, at least one group of acid mist absorber portion, water proof section, demist section and the wind outlet section of being made up of spray absorber portion and filler absorber portion successively; Said spray absorber portion is provided with spray system, and this spray system is provided with a plurality of nozzles, and the hydrojet direction of this nozzle is consistent with the direction that sour gas flows, and said tower body is a horizontal positioned, makes sour gas physical efficiency level pass through spray purification tower.
During work, sour gas gets into spray purification tower from wind inlet section, under the dynamic action of ventilation blower; Be full of wind inlet section rapidly, during through first order spray section, sour gas is identical with nozzle ejection liquid direction; Alkaline matter generation chemical reaction in gas phase middle acid substance and the absorption liquid; Uniformly through first order filler absorber portion, the solubility salt that reaction generates flows in the liquid storage section of bottom with absorption liquid, thereby disposes the sour gas middle acid substance then.Gas phase flows to the water proof section and removes wherein residual absorption liquid at this moment, then further removes wherein residual droplet through the demist section, enters atmosphere through wind outlet section at last.
The preferred two groups of acid mist absorber portions of the utility model, thus first order spray absorber portion, first order filler absorber portion, second level spray absorber portion and second level filler absorber portion formed.Be difficult to an Ex-all when the sour gas middle acid substance is higher, this moment, second level spray absorber portion and second level filler absorber portion can guarantee further that the acidic materials removing is clean.
As preferably, the nozzle quantity of said second level spray absorber portion and the absorption liquid pressure of ejection is all greater than first order spray absorber portion, thereby improves the efficient of second level absorption.
As preferably, also comprise the absorption liquid EGR; Said tower body bottom also is provided with the liquid storage section, and said absorption liquid EGR is connected with said liquid storage section and spray system, thereby has improved the utilization rate of absorption liquid greatly, reduces the discharging of waste liquid.
As preferably, said absorption liquid EGR comprises the dosing tank that absorption liquid is housed, and this dosing tank inlet is connected with said liquid storage section, and this dosing tank outlet is passed through water pump and is communicated with spray system.Through such improvement, make things convenient for the dosing of absorption liquid and the dismounting maintenance of equipment.
As preferably, said nozzle adopts spiral nozzle, thereby makes the water smoke of ejection more even.
As preferably, said tower body adopts PP plate or fiberglass to process
Beneficial effect: compared with prior art, the utlity model has following advantage: the absorption efficiency to sour gas is higher; Adopt horizontal, equipment easier for installation flexibly.
Description of drawings
Fig. 1 is the structural representation of the utility model;
Fig. 2 is the structural representation of spray system in the utility model.
The specific embodiment
Below in conjunction with accompanying drawing and specific embodiment; Further illustrate the utility model; Should understand these embodiment only be used to the utility model is described and be not used in the restriction the utility model scope; After having read the utility model, those skilled in the art all fall within the application's accompanying claims institute restricted portion to the modification of the various equivalent form of values of the utility model.
Horizental showering purifying column as shown in Figure 1 comprises spray purification tower and absorption liquid EGR 13; This spray purification tower comprises tower body 1; This tower body 1 inner along continuous straight runs is provided with wind inlet section 2, first order spray absorber portion 3, first order filler absorber portion 4, second level spray absorber portion, second level filler absorber portion, water proof section 5, demist section 6 and wind outlet section 7 successively; This first spray absorber portion and the second spray absorber portion all are provided with spray system 9; Described spray system 9 all is provided with abundant nozzle 17 uniformly, therefore works as sour gas and can horizontal direction pass through tower body 1, and be filled with filler 10 in each filler absorber portion; Simultaneously be provided with liquid storage section 8 in this tower body 1 bottom;, the absorption liquid of spray can be collected into this liquid storage section 8 after absorbing acid mist; Send spray system 9 once more back to from nozzle 17 ejections through the absorption liquid EGR 13 that is communicated with this liquid storage section 8 again, thereby practiced thrift the use amount of absorption liquid greatly and improved absorptivity; This absorption liquid EGR 13 comprises that storage has the dosing tank 14 of absorption liquid; These dosing tank 14 sidewalls are provided with overfall 15; The bottom of this dosing tank 14 is communicated with liquid storage section 8 through water tank connecting pipe; This dosing tank 14 is communicated with spray system 9 through submerged pump 16 or centrifugal pump simultaneously, and the nozzle 17 hydrojet directions of this spray system 9 are consistent with the direction that sour gas flows.Above the first filler absorber portion, the second filler absorber portion and demist section 6, all be provided with simultaneously filler and add mouth 11, and thereunder be provided with discharge opening 12, be provided with the spray visor hole that is used to observe the spray situation at tower body 1.
Handle when discarding, sour gas gets into spray purification towers from wind inlet section 2, under the dynamic action of ventilation blower; Be full of wind inlet section 2 rapidly, during through first order spray section, sour gas is identical with nozzle ejection liquid direction; Alkaline matter generation chemical reaction in gas phase middle acid substance and the absorption liquid; Uniformly through first order filler absorber portion 4, the solubility salt that reaction generates flows in the liquid storage section 8 of bottom with absorption liquid, is difficult to an Ex-all when the sour gas middle acid substance is higher then; This moment, second level spray absorber portion and second level filler absorber portion can guarantee further that the acidic materials removing is clean, thereby disposed the sour gas middle acid substance.Gas phase flows to water proof section 5 and removes wherein residual absorption liquid at this moment, then further removes wherein residual droplet through demist section 6, enters atmosphere through wind outlet section 7 at last.
Claims (7)
1. Horizental showering purifying column; It is characterized in that: comprise tower body (1), this tower body (1) inside flatly is provided with wind inlet section (2), at least one group of acid mist absorber portion, water proof section (5), demist section (6) and the wind outlet section of being made up of spray absorber portion (3) and filler absorber portion (4) (7) successively; Said spray absorber portion is provided with spray system (9), and this spray system is provided with a plurality of nozzles (17), and the hydrojet direction of this nozzle (17) is consistent with the direction that sour gas flows.
2. Horizental showering purifying column according to claim 1 is characterized in that: comprise two groups of acid mist absorber portions, thereby form first order spray absorber portion, first order filler absorber portion, second level spray absorber portion and second level filler absorber portion.
3. Horizental showering purifying column according to claim 2 is characterized in that: the nozzle quantity of said second level spray absorber portion and the absorption liquid pressure of ejection are all greater than first order spray absorber portion.
4. Horizental showering purifying column according to claim 1 is characterized in that: also comprise absorption liquid EGR (13); Said tower body (1) bottom also is provided with liquid storage section (8), and said absorption liquid EGR (13) is connected with said liquid storage section (8) and spray system (9).
5. Horizental showering purifying column according to claim 4; It is characterized in that: said absorption liquid EGR (13) comprises the dosing tank (14) that absorption liquid is housed; This dosing tank inlet is connected with said liquid storage section (8), and this dosing tank (14) outlet is communicated with spray system (9) through water pump.
6. Horizental showering purifying column according to claim 5 is characterized in that: said nozzle is a spiral nozzle.
7. Horizental showering purifying column according to claim 1 is characterized in that: said tower body (1) adopts PP plate or fiberglass to process.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204486010U CN202460441U (en) | 2011-11-14 | 2011-11-14 | Horizontal type spray purification tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204486010U CN202460441U (en) | 2011-11-14 | 2011-11-14 | Horizontal type spray purification tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202460441U true CN202460441U (en) | 2012-10-03 |
Family
ID=46908642
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011204486010U Expired - Fee Related CN202460441U (en) | 2011-11-14 | 2011-11-14 | Horizontal type spray purification tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202460441U (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103071376A (en) * | 2013-01-24 | 2013-05-01 | 江苏新阪神太阳能有限公司 | Waste gas treatment device |
| CN103611404A (en) * | 2013-11-30 | 2014-03-05 | 竹山县秦家河矿业有限公司 | Wet flue gas desulfurization tower |
| CN105013294A (en) * | 2015-07-01 | 2015-11-04 | 太仓市顺邦防腐设备有限公司 | Horizontal exhaust gas purification tower |
| CN105363333A (en) * | 2015-11-20 | 2016-03-02 | 太仓市振锋化工设备有限公司 | Polypropylene acid mist absorption tower |
| CN106268248A (en) * | 2015-05-25 | 2017-01-04 | 中国石油集团川庆钻探工程有限公司长庆井下技术作业公司 | A kind of oil gas field acid waste gas skid processing means |
| CN106334417A (en) * | 2016-10-31 | 2017-01-18 | 华北电力大学（保定） | Boiler smoke treatment device and treatment method thereof |
| CN107376616A (en) * | 2017-08-04 | 2017-11-24 | 深圳市乐业科技有限公司 | It is a kind of to improve generating efficiency and carry the energy-saving acid mist purifying tower of dedusting function |
| CN114206473A (en) * | 2021-11-09 | 2022-03-18 | 无锡星亿智能环保装备股份有限公司 | Waste gas purification tower |
-
2011
- 2011-11-14 CN CN2011204486010U patent/CN202460441U/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103071376A (en) * | 2013-01-24 | 2013-05-01 | 江苏新阪神太阳能有限公司 | Waste gas treatment device |
| CN103611404A (en) * | 2013-11-30 | 2014-03-05 | 竹山县秦家河矿业有限公司 | Wet flue gas desulfurization tower |
| CN106268248A (en) * | 2015-05-25 | 2017-01-04 | 中国石油集团川庆钻探工程有限公司长庆井下技术作业公司 | A kind of oil gas field acid waste gas skid processing means |
| CN105013294A (en) * | 2015-07-01 | 2015-11-04 | 太仓市顺邦防腐设备有限公司 | Horizontal exhaust gas purification tower |
| CN105363333A (en) * | 2015-11-20 | 2016-03-02 | 太仓市振锋化工设备有限公司 | Polypropylene acid mist absorption tower |
| CN106334417A (en) * | 2016-10-31 | 2017-01-18 | 华北电力大学（保定） | Boiler smoke treatment device and treatment method thereof |
| CN106334417B (en) * | 2016-10-31 | 2019-04-02 | 华北电力大学（保定） | A kind of processing unit and its processing method of boiler smoke |
| CN107376616A (en) * | 2017-08-04 | 2017-11-24 | 深圳市乐业科技有限公司 | It is a kind of to improve generating efficiency and carry the energy-saving acid mist purifying tower of dedusting function |
| CN114206473A (en) * | 2021-11-09 | 2022-03-18 | 无锡星亿智能环保装备股份有限公司 | Waste gas purification tower |
| WO2023082033A1 (en) * | 2021-11-09 | 2023-05-19 | 无锡星亿智能环保装备股份有限公司 | Flue gas purification tower |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121003 Termination date: 20151114 |
|
| EXPY | Termination of patent right or utility model |