CN204816077U - Gaseous purifier of fountain - Google Patents
Gaseous purifier of fountain Download PDFInfo
- Publication number
- CN204816077U CN204816077U CN201520607375.4U CN201520607375U CN204816077U CN 204816077 U CN204816077 U CN 204816077U CN 201520607375 U CN201520607375 U CN 201520607375U CN 204816077 U CN204816077 U CN 204816077U
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- reservoir
- thick bamboo
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- sedimentation basin
- liquid
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Abstract
The utility model relates to a gaseous purifier of fountain, its structure is including a purification section of thick bamboo that sets up highly test in proper order, sedimentation tank and reservoir, it sprays the orifice plate to be provided with in the inside that purifies a section of thick bamboo, so that liquid can through the cloth liquid hole on it even drench purify a section of thick bamboo in, top purifying a section of thick bamboo has connect the pipe of discharging fume, be used for the draught fan of drawing forth the gas after purifying discharging fume to be equipped with on the pipe, the lateral wall lower part that purifies a section of thick bamboo connects the admission line of connecting the boiler exhaust port, bottom purifying a section of thick bamboo has connect the fluid -discharge tube, the fluid -discharge tube communicates in the sedimentation tank, the drain pipe has been connect between sedimentation tank and reservoir, the liquid pipe has been connect between the top of a reservoir and a purification section of thick bamboo, be equipped with the last liquid pump in being used for going into to purify a section of thick bamboo with the liquor pump in the reservoir on last liquid pipe. The utility model discloses simple structure easily builds and implements, no potential safety hazard, and practice thrift the energy consumption, and low cost, application scope is wide.
Description
Technical field
The utility model relates to a kind of flue gas processing device, specifically a kind of fountain gas cleaning plant.
Background technology
At present, the flue gas of the industrial equipment discharges such as boiler is caused discharge duct by air-introduced machine and is discharged in upper atmosphere through chimney, but owing to containing toxic gas and the pollutants such as a large amount of minute dusts, sulfur dioxide, nitrogen oxide or carbon black in flue gas, meeting major polluting atmosphere environment, therefore need to process the flue gas of discharge.And existing flue gas processing device structure is all more complicated, not easily build, and cost is higher, energy consumption is comparatively large, is unsuitable for extensive use.
Utility model content
The purpose of this utility model is just to provide a kind of fountain gas cleaning plant, to solve the problem that existing flue gas processing device complex structure, energy consumption are comparatively large and cost is higher.
The utility model is achieved in that
A kind of fountain gas cleaning plant, comprise the purifying tube of rational height test successively, sedimentation basin and reservoir, the inside of described purifying tube is provided with spray orifice plate, smoke exhaust pipe is connected at the top of described purifying tube, described smoke exhaust pipe is provided with air-introduced machine, the admission line connecting boiler smoke outlet is connected in the lower sidewall of described purifying tube, discharging tube is connected in the bottom of described purifying tube, described discharging tube is communicated in described sedimentation basin, drain pipe is connected between described sedimentation basin and described reservoir, liquid pipe is connected between described reservoir and the top of described purifying tube, liquid pipe is provided with liquid pump on described.
The bottom of described purifying tube is cone, and the end leakage fluid dram of described cone is communicated with by the inlet of discharging tube with described sedimentation basin, and the liquid outlet of described sedimentation basin is connected by the inlet of drain pipe with described reservoir.
Described sedimentation basin has two, and two described sedimentation basins are arranged in parallel.
The bottom position of described purifying tube is higher than the top of described sedimentation basin, and the bottom position of described sedimentation basin is higher than the top of described reservoir.
During use, in unlatching, the spray liquid in reservoir is pumped into the top of purifying tube by liquid pump, the spray liquid entering purifying tube top is sprayed downwards uniformly by spray orifice plate, pending flue gas from boiler enters in purifying tube from the admission line of purifying tube bottom, flue gas sprays with the spray orifice plate from purifying tube the liquid got off and fully contacts in the process risen, pernicious gas in flue gas and pollutant are absorbed by spray liquid or settle down, and enter in sedimentation basin with spray liquid through the leakage fluid dram of purifying tube end, purified gas is introduced after smoke exhaust pipe through air-introduced machine and is discharged, enter the liquid of sedimentation basin after precipitation, upper clear supernate is entered in reservoir by drain pipe and recycles, and bottom precipitation thing is regularly cleared up.
The rational height of purifying tube, sedimentation basin and reservoir test successively in the utility model, Liquid transfer between purifying tube and sedimentation basin and between sedimentation basin and reservoir is carried out under gravity, decrease the use of transmission pump, thus saved energy consumption, reduce cost.The utility model structure is simple, is easy to build implement, without potential safety hazard, and with low cost, applied widely.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In figure: 1, purifying tube, 2, spray orifice plate, 3, sedimentation basin, 4, reservoir, 5, admission line, 6, boiler, 7, discharging tube, 8, upper liquid pipe, 9, upper liquid pump, 10, smoke exhaust pipe, 11, air-introduced machine, 12, drain pipe.
Detailed description of the invention
As shown in Figure 1, the utility model is primarily of part compositions such as purifying tube 1, sedimentation basin 3 and reservoirs 4.
Purifying tube 1 is column-shaped barrel, its size can be determined according to the number of pernicious gas such as equipment exhausting such as boiler 6 grade, be provided with admission line 5 in the bottom of the cylinder lateral wall of purifying tube 1, admission line 5 is connected with the exhaust smoke hole of boiler 6, and the flue gas from boiler 6 enters in purifying tube 1 from cylindrical shell bottom, spray orifice plate 2 is provided with in the position level that the inner barrel of purifying tube 1 is top, purifying tube 1 is divided into upper and lower two chambers by spray orifice plate 2, inlet is provided with at the top of upper chamber, this inlet is connected with reservoir 4 by upper liquid pipe 8, upper liquid pipe 8 is provided with liquid pump 9, in order to the liquid in reservoir 4 is pumped in upper chamber, spray orifice plate 2 is evenly distributed with liquid distributing hole, drenched uniformly into bottom chamber by liquid distributing hole to enable the liquid entering upper chamber, thus the flue gas from cylindrical shell bottom is purified, smoke exhaust pipe 10 is connected at the top of upper chamber, smoke exhaust pipe 10 is provided with air-introduced machine 11, for purified gas is drawn, the lower chambers end of purifying tube 1 is set to cone, so that spray liquid is converged at a place, has leakage fluid dram at the end of cone, and this leakage fluid dram is connected with sedimentation basin 3 by discharging tube 7.
Sedimentation basin 3 is for the liquid that receives from purifying tube 1 and make it precipitate, the inlet of sedimentation basin 3 is connected by discharging tube 7 with the leakage fluid dram of purifying tube 1 end, the liquid outlet of sedimentation basin 3 is connected by the inlet of drain pipe 12 with reservoir 4, after liquid precipitates in sedimentation basin 3, upper clear supernate is entered in reservoir 4 by drain pipe 12 and recycles, and bottom precipitation thing is regularly cleared up; Sedimentation basin 3 is preferably set to two, and two sedimentation basins 3 are arranged in parallel, and can be used alternatingly, so that can not affect the operation of whole device when clearing up one of them.
Reservoir 4 is for storing spray liquid, according to the composition of flue gas to be clean, in spray liquid, add suitable material regulate its character, to carry out purified treatment to flue gas better, such as can add appropriate alkaline matter in reservoir 4, while minute dusts in flue gas is purified, the acid ingredient in all right and in flue gas.
Sedimentation basin 3 is arranged on the position higher than reservoir 4 top by the utility model, purifying tube 1 is arranged on the position higher than sedimentation basin 3 top, Liquid transfer between purifying tube 1 and sedimentation basin 3 and between sedimentation basin 3 and reservoir 4 is carried out under gravity, thus has saved energy consumption.
Upper liquid pipe 8 also can stretch in the upper chamber of purifying tube 1 from inlet level by the utility model, and installs several downward shower nozzles on upper liquid pipe 8, thus liquid is sprayed more uniformly, makes gas-liquid contact more abundant.
Claims (4)
1. a fountain gas cleaning plant, it is characterized in that, comprise the purifying tube of rational height test successively, sedimentation basin and reservoir, the inside of described purifying tube is provided with spray orifice plate, smoke exhaust pipe is connected at the top of described purifying tube, described smoke exhaust pipe is provided with air-introduced machine, the admission line connecting boiler smoke outlet is connected in the lower sidewall of described purifying tube, discharging tube is connected in the bottom of described purifying tube, described discharging tube is communicated in described sedimentation basin, drain pipe is connected between described sedimentation basin and described reservoir, liquid pipe is connected between described reservoir and the top of described purifying tube, liquid pipe is provided with liquid pump on described.
2. fountain gas cleaning plant according to claim 1, it is characterized in that, the bottom of described purifying tube is cone, the end leakage fluid dram of described cone is communicated with by the inlet of discharging tube with described sedimentation basin, and the liquid outlet of described sedimentation basin is connected by the inlet of drain pipe with described reservoir.
3. fountain gas cleaning plant according to claim 2, is characterized in that, described sedimentation basin has two, and two described sedimentation basins are arranged in parallel.
4. fountain gas cleaning plant according to claim 1, is characterized in that, the bottom position of described purifying tube is higher than the top of described sedimentation basin, and the bottom position of described sedimentation basin is higher than the top of described reservoir.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520607375.4U CN204816077U (en) | 2015-08-13 | 2015-08-13 | Gaseous purifier of fountain |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520607375.4U CN204816077U (en) | 2015-08-13 | 2015-08-13 | Gaseous purifier of fountain |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204816077U true CN204816077U (en) | 2015-12-02 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520607375.4U Active CN204816077U (en) | 2015-08-13 | 2015-08-13 | Gaseous purifier of fountain |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204816077U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107233781A (en) * | 2017-06-08 | 2017-10-10 | 浙江正翰环保科技有限公司 | A kind of waste gas recuperation of heat condenser system and its waste gas processing method |
-
2015
- 2015-08-13 CN CN201520607375.4U patent/CN204816077U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107233781A (en) * | 2017-06-08 | 2017-10-10 | 浙江正翰环保科技有限公司 | A kind of waste gas recuperation of heat condenser system and its waste gas processing method |
| CN107233781B (en) * | 2017-06-08 | 2019-12-06 | 浙江寰龙环境科技有限公司 | Waste gas heat recovery and condensation system and waste gas treatment method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |