CN2478666Y - Fluidization spray purifier - Google Patents
Fluidization spray purifier Download PDFInfo
- Publication number
- CN2478666Y CN2478666Y CN 01239997 CN01239997U CN2478666Y CN 2478666 Y CN2478666 Y CN 2478666Y CN 01239997 CN01239997 CN 01239997 CN 01239997 U CN01239997 U CN 01239997U CN 2478666 Y CN2478666 Y CN 2478666Y
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- casing
- baffler
- utility
- bubble
- model
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Abstract
The utility model discloses a fluidization spray purifier which relates to an environmental protection device. The top part of a casing is provided with a net gas outlet, the bottom part is provided with a smoke and sludge outlet, the side is provided with a smoke and air-current inlet, and the inner part of the casing is provided with a foggy spraying head. The utility model is characterized in that an inner cavity of the casing is provided with a bubble plate and a baffler, and nozzles are evenly arranged on the bubble plate. Every nozzle is connected with a bubble cap in hanging type, and linguiform holes are evenly arranged on the baffler. A flow guide pipe is arranged between the bubble plate and the baffler, and the bottom side of the casing is provided with a water overflow pipe leading to the outer part of the casing. The utility model has the characteristics of low cost, stable running and convenient maintenance, the dedusting efficiency reaches 99 percents, and the purifying rate of the harmful gas reaches from 50 percents to 70 percents.
Description
The utility model relates to environmental protection equipment, is a kind of fluidisation spraying clarifier.
At present, the equipment that is used for the processing of industrial waste gas clarifying smoke has multiple, water smoke wet scrubber, high-voltage electrostatic dust separator etc. are for example arranged, water smoke wet scrubber efficiency of dust collection about 90%, and water consumption is big, and the water of using is purified treatment again, high-voltage electrostatic dust separator cost height, operation maintenance requires tight, and these existing problems are limited to them, can not get extensive utilization.
The purpose of this utility model provides a kind of fluidisation spraying clarifier, its efficiency of dust collection height, and cost is low, and is stable, easy to maintenance.
The purpose of this utility model is to realize like this, the top of fluidisation spraying purifier shell is provided with the pure qi (oxygen) outlet, the bottom is provided with the flue dust sludge outlet, the side is provided with the dust inflow entrance, housing inner chamber top is provided with waterfog head, it is characterized in that: the housing inner chamber is provided with bubble cap tray and baffler, be laid with spout on the bubble cap tray, the all outstanding bubble-cap that is connected on each spout, be laid with the ligulate hole on the baffler, be provided with mozzle between bubble cap tray and the baffler, the bottom side side of housing is provided with overflow pipe and passes to outside the housing.
The utility model utilizes the wet dust removal principle, inertial collision, the dust of water droplet and grit organically are incorporated into one to water droplet diffusion into the surface, coring cohesion mechanism and fluidization mechanism, adopted special fluidisation blister configuration, the speed of related movement of gas and water droplet is strengthened, improve the purifying and dedusting effect, characteristics are: efficiency of dust collection can reach more than 99%, the cleaning harmful gas rate can reach 50-70%, cost is low, and is stable, easy to maintenance.
Embodiment further describes below in conjunction with accompanying drawing, and Fig. 1 is a structural principle schematic diagram of the present utility model.
Embodiment:, be 25000-30000NM with the purified treatment ability referring to Fig. 1
3The utility model of/H is an example, housing 1 two ends are tapered, the middle part is the garden cylindricality of 2 meters of φ, adopt the steel plate welding fabrication, critical piece is through fine finishining or punch forming, auxiliary equipment can arrive market and buy, uniformly on the bubble cap tray 6 be provided with 115 spouts 8, spout internal diameter 60mm, bubble-cap 9 is welded the top that is suspended at each spout 8 by gusset, and the flow of waterfog head 5 and flue dust sludge outlet 3 can be regulated, before the utility model uses, must distinguish UNICOM with water supply line, intake stack and flue dust sludge outlet pipeline, can turn round after the debugging.Narrate operation process below, at first make the supply channel running, as shown in Figure 1, waterfog head 5 is ejection water smoke constantly, when the surface area water water surface of bubble cap tray 6 exceeds mozzle 11 end faces, water enters the hypocone that mozzle 11 runs underneath to housing 1, and the water surface of housing hypocone is increased to overflow pipe 12 places, beginning spilling water outside housing.At this moment, open intake stack, HTHP flue dust air-flow enters in the housing from dust inflow entrance 4, and crude particle dust is deposited in the water on baffler 7 surfaces, be deposited in the lower cone mud through ligulate hole 10, simultaneously, air-flow enters spout 8, is subjected to stopping of bubble-cap 9, back enters in the water on bubble cap tray 6 surfaces, dust and pernicious gas major part are absorbed by water, and purified gas is deviate from from water, and the mist layer that produces through waterfog head 5 further purifies the back from pure qi (oxygen) outlet 2 effusions again.The flue dust mud of bubble cap tray face is with water process mozzle diffluence housing hypocone, the flue dust mud on baffler 7 surfaces then sinks to the housing hypocone through ligulate hole 10, the flue dust mud of post precipitation, from flue dust sludge outlet 3 outflows of bottom, the water that flows out from overflow pipe 12 then can be recycled.
Claims (1)
1. the top of fluidisation spraying purifier shell 1 is provided with pure qi (oxygen) outlet 2, the bottom is provided with flue dust sludge outlet 3, the side is provided with dust inflow entrance 4, the top of housing inner chamber is provided with waterfog head 5, it is characterized in that: the housing inner chamber is provided with bubble cap tray 6 and baffler 7, be laid with spout 8 on the bubble cap tray 6, the all outstanding bubble-cap 9 that is connected on each spout 8, be laid with ligulate hole 10 on the baffler 7, be provided with mozzle 11 between bubble cap tray and the baffler, the bottom side side of housing 1 is provided with overflow pipe 12 and passes to outside the housing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01239997 CN2478666Y (en) | 2001-05-11 | 2001-05-11 | Fluidization spray purifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01239997 CN2478666Y (en) | 2001-05-11 | 2001-05-11 | Fluidization spray purifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2478666Y true CN2478666Y (en) | 2002-02-27 |
Family
ID=33652317
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 01239997 Expired - Fee Related CN2478666Y (en) | 2001-05-11 | 2001-05-11 | Fluidization spray purifier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2478666Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102872664A (en) * | 2012-10-11 | 2013-01-16 | 无锡多灵环保工程设备有限公司 | Flue gas washing tower |
| CN105771477A (en) * | 2014-12-22 | 2016-07-20 | 中国科学院过程工程研究所 | Fluidization atomization-liquid film washing combined flue gas purifying device and method |
| CN109078479A (en) * | 2018-09-05 | 2018-12-25 | 无锡中天固废处置有限公司 | A kind of compound bio method processing sewage plant exhaust device and waste gas processing method |
-
2001
- 2001-05-11 CN CN 01239997 patent/CN2478666Y/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102872664A (en) * | 2012-10-11 | 2013-01-16 | 无锡多灵环保工程设备有限公司 | Flue gas washing tower |
| CN105771477A (en) * | 2014-12-22 | 2016-07-20 | 中国科学院过程工程研究所 | Fluidization atomization-liquid film washing combined flue gas purifying device and method |
| CN105771477B (en) * | 2014-12-22 | 2019-03-15 | 中国科学院过程工程研究所 | A kind of fluidisation atomization and liquid film wash combined flue gas purification device and method |
| CN109078479A (en) * | 2018-09-05 | 2018-12-25 | 无锡中天固废处置有限公司 | A kind of compound bio method processing sewage plant exhaust device and waste gas processing method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| 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 |