CN203816426U - Large dust waste gas treatment device - Google Patents
Large dust waste gas treatment device Download PDFInfo
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- CN203816426U CN203816426U CN201420062967.8U CN201420062967U CN203816426U CN 203816426 U CN203816426 U CN 203816426U CN 201420062967 U CN201420062967 U CN 201420062967U CN 203816426 U CN203816426 U CN 203816426U
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- dust
- waste gas
- breather pipe
- deceleration
- process chamber
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Abstract
The utility model discloses a large dust waste gas treatment device, comprising a shell, wherein a dust treatment chamber, an atomizing treatment chamber and a deceleration cooling treatment chamber are arranged in the shell, waste odor enters the dust treatment chamber, the atomizing treatment chamber and the deceleration cooling treatment sequentially to be subjected to initial dust-removing sediment treatment, atomizing reaction treatment and deceleration cooling treatment respectively, and then the treated waste odor is discharged. By arranging the three main treatment chambers, namely the dust treatment chamber, the atomizing treatment chamber and the deceleration cooling treatment chamber, the initial dust-removing sediment treatment, the atomizing reaction treatment and the deceleration cooling treatment are performed on the large dust waste gas; according to actual different large dust waste gas and required emission standard, the large dust waste gas treatment device can be properly deformed according to actual demand so that the large dust waste gas treatment is wide in application range, low in treatment cost, simple to operate and capable of meeting the treatment requirement of the large dust waste gas.
Description
Technical field
The utility model relates to dust waste gas treatment equipment field, in particular a kind of large dust and waste gas treatment device.
Background technology
Along with industrialized development, factory is more and more, the industrial waste gas and the industrial fumes that bring also roll up thereupon, if be directly discharged to meeting serious environment pollution in atmosphere without processing, Carbon Dioxide in Air, sulfur dioxide and other pernicious gases can roll up, and cause the formation of greenhouse effects and acid rain; While is the serious harm mankind's health also, causes cough, asthma patient number to present seasonal sharply rising, the even high incidence of cancer.And the effect of more existing exhaust gas and smoke treating apparatus is not very desirable, some effect can but complex structure is processed loaded down with trivial detailsly, increased undoubtedly processing cost, apply very limited.
Therefore, prior art has yet to be improved and developed.
Summary of the invention
The purpose of this utility model is to provide a kind of large dust and waste gas treatment device, is intended to solve the undesirable or complex structure of existing flue dust treating apparatus treatment effect, processing is loaded down with trivial details, increases the problem of processing cost.
The technical solution of the utility model is as follows: a kind of large dust and waste gas treatment device, wherein, comprise housing, in described housing, be provided with dust process chamber, atomization process chamber and deceleration cooling processing chamber, large dust waste gas enters successively dust process chamber, atomization process chamber and deceleration cooling processing chamber and processes discharge;
Described dust process chamber comprises dedusting portion and exhaust portion, in described dust process chamber, is provided with the first air inlet, is provided with first row gas port in described exhaust portion; In described dedusting portion, be evenly provided with the fine dust bags of a plurality of carbon, the fine dust bag inlet end of carbon is connected with the first air inlet;
On described atomization process chamber, be provided with the second air inlet and second row gas port, described the second air inlet is communicated with first row gas port; In described atomization process chamber, be evenly provided with a plurality of pulverizer plates, be provided with mist pipe on pulverizer plate, mist pipe is by the external atomized liquid of atomizer; On pulverizer plate, be also evenly provided with a plurality of air-vents;
Described deceleration cooling processing chamber comprises the 3rd air inlet and the 3rd exhaust outlet, and the 3rd air inlet is communicated with second row gas port; Described deceleration cooling processing is indoor is also evenly provided with many deceleration tubes, and deceleration tube runs through whole deceleration cooling processing chamber, and described deceleration tube comprises the first breather pipe, the second breather pipe and the 3rd breather pipe; Described second breather pipe one end connects the first breather pipe, and the other end connects the 3rd breather pipe; Described the first breather pipe, the second breather pipe and the 3rd breather pipe form the shape of hierarchic structure; Indoor a plurality of cooling tubes, the external cooling fluid of described cooling tube of being also provided with of described deceleration cooling processing.
Described large dust and waste gas treatment device, wherein, described dust process chamber, atomization process chamber and deceleration cooling processing chamber can arrange a plurality of according to actual needs.
Described large dust and waste gas treatment device wherein, is provided with gas distribution plate between described the first air inlet and the fine dust bag inlet end of carbon, on described gas distribution plate, is evenly provided with a plurality of minutes pores.
Described large dust and waste gas treatment device, wherein, the exhaust end bottom gap of the fine dust bag of described carbon is provided with the bucket that gathers dust, exhaust end bottom does not contact with the bucket that gathers dust, described in gather dust to struggle against and be arranged to funnel structure, the upper end of struggling against of gathering dust is provided with switch flashboard.
Described large dust and waste gas treatment device, wherein, the bottom of described atomization process chamber is provided with atomized liquid mouth, and described atomized liquid mouth connects filter, and filter is connected with atomizer.
Described large dust and waste gas treatment device, wherein, described the first breather pipe and the 3rd breather pipe are obliquely installed, and one end that the first breather pipe is connected with the second breather pipe is higher than the other end, and one end that the 3rd breather pipe is connected with the second breather pipe is higher than the other end; Bottom, deceleration cooling processing chamber is provided with back liquid receiving mouth, and described time liquid receiving mouth connects filter, and filter is connected with atomizer.
Described large dust and waste gas treatment device, wherein, described large dust and waste gas treatment device also comprises extractor fan, described extractor fan can be arranged at the first air inlet place or the 3rd exhaust ports.
Described large dust and waste gas treatment device, wherein, described atomizer can adopt high-pressure atomizer or electrothermal atomizer according to actual needs.
The beneficial effects of the utility model: the utility model is by providing a kind of large dust and waste gas treatment device, this large dust and waste gas treatment device is by arranging dust process chamber, the main process chamber of atomization process chamber and three of deceleration cooling processing chambers, large dust waste gas is carried out to rough dusting precipitation process, atomization reaction treatment and last deceleration cooling processing; The large dust waste gas and the discharge standard that need to reach different according to reality, this large dust and waste gas treatment device can also suitably be out of shape according to actual needs, makes the applied widely of large dust and waste gas treatment device, and processing cost is low, simple to operate, meet the processing requirements of large dust waste gas.
Accompanying drawing explanation
Fig. 1 is the structural representation of large dust and waste gas treatment device in the utility model.
Fig. 2 is the structural representation of deceleration tube in the utility model.
The specific embodiment
For making the purpose of this utility model, technical scheme and advantage clearer, clear and definite, referring to the accompanying drawing embodiment that develops simultaneously, the utility model is further described.
As shown in Figure 1, be the structural representation of large dust and waste gas treatment device in the utility model.Described large dust and waste gas treatment device comprises housing 100, in described housing 100, be provided with dust process chamber 200, atomization process chamber 300 and deceleration cooling processing chamber 400, waste odour-gas enters dust process chamber 200 successively to carry out rough dusting precipitation process, atomization process chamber 300 and carries out atomization reaction treatment and deceleration cooling processing chamber 400 cooling processing of slowing down, and discharge is disposed.
Described dust process chamber 200 comprises dedusting portion 210 and exhaust portion 220, is provided with the first air inlet 230 in described dust process chamber 200, in described exhaust portion 220, is provided with first row gas port; The interior fine dust bags 211 of a plurality of carbon that are evenly provided with of described dedusting portion 210, fine dust bag 211 inlet ends of carbon are connected with the first air inlet 230.
On described atomization process chamber 300, be provided with the second air inlet and second row gas port, described the second air inlet is communicated with first row gas port; Described atomization process chamber 300 is interior is evenly provided with a plurality of pulverizer plates 320, is provided with mist pipe 321 on pulverizer plate 320, and mist pipe 321 is by the external atomized liquid of atomizer; On pulverizer plate 320, be also evenly provided with a plurality of air-vents.
Described deceleration cooling processing chamber 400 comprises that the 3rd air inlet and the 3rd exhaust outlet 420, the three air inlets are communicated with second row gas port; In described deceleration cooling processing chamber 400, be also evenly provided with many deceleration tubes 410, deceleration tube 410 runs through whole deceleration cooling processing chamber 400, and described deceleration tube 410 comprises the first breather pipe 411, the second breather pipe 412 and the 3rd breather pipe 413; Described second breather pipe 412 one end connect the first breather pipe 411, and the other end connects the 3rd breather pipe 413; Described the first breather pipe 411, the second breather pipe 412 and the 3rd breather pipe 413 form the shape (as shown in Figure 2) of hierarchic structure, the gas entering are played to the effect of deceleration; In described deceleration cooling processing chamber 400, be also provided with a plurality of cooling tubes 440, the external cooling fluid of described cooling tube 440.
According to the class of pollution of smoke exhaust and the discharge standard that need to reach, described dust process chamber 200, atomization process chamber 300 and deceleration cooling processing chamber 400 can arrange a plurality of according to actual needs, spread pattern is mutually determined according to actual needs: can be dust process chamber 200-atomization process chamber 300-deceleration cooling processing chamber 400 apart from one another by setting, can be also that a plurality of dust process chambers 200 connect successively setting-a plurality of atomization process chambers 300 and connect successively setting-a plurality of deceleration cooling processing chamber 400 and connect successively setting.
Too concentrated in order to prevent from being entered by the first air inlet 230 the large dust waste gas of dedusting portion 210, the fine dust bag 211 of carbon can not fully be processed large dust waste gas, affect treatment effect, between described the first air inlet 230 and fine dust bag 211 inlet ends of carbon, be provided with gas distribution plate 240, on described gas distribution plate 240, be evenly provided with a plurality of minutes pores 241, like this, pending large dust waste gas is assigned to equably in the fine dust bag 211 of each carbon and carries out dust removal process by gas distribution plate 240.
For the convenient dust precipitating through dust process chamber 200 of collecting, the exhaust end bottom gap of the fine dust bag 210 of described carbon is provided with the bucket 250 that gathers dust, exhaust end bottom does not contact with the bucket 250 that gathers dust, the described bucket 250 that gathers dust is arranged to funnel structure, bucket 250 the upper end of gathering dust is provided with switch flashboard: like this, the dust precipitating through dust process chamber 200 is all gathered on switch flashboard, when dust accumulation is when a certain amount of, open switch flashboard, dust is dropped to automatically gather dust in bucket 250, convenient dust is carried out to collection and treatment.
The switching of described switch flashboard can, by manually controlling, also can be controlled by machinery.In the present embodiment, the switching of described switch flashboard is controlled by machinery, described switch flashboard comprises fixedly round end and movable end, described fixedly round end is connected with the bucket 250 that gathers dust by rotating shaft, rotating shaft is connected with power set, the bucket that gathers dust is provided with fixing lock on 250: under normal circumstances, the movable end of switch flashboard is locked by fixing; When needs are discharged dust, machinery is controlled fixing lock and is opened, and the movable end of switch flashboard be take the rotating shaft of fixing round end and under the effect of gravity, rotated as pivot, and switch flashboard is opened thereupon, and dust drops in the bucket 250 that gathers dust under the effect of gravity; After dust is discharged, rotating shaft is spinning reduction under the drive of power set, and fixedly lock is locked fixing round end again.
Because can be retained in atomization process chamber 300 after the atomized liquid in atomization process chamber 300 contacts with gas, for the liquid to this part recycles, the bottom of described atomization process chamber 300 is provided with atomized liquid mouth, described atomized liquid mouth connects filter, filter is connected with atomizer: atomized liquid enters filter by leakage fluid dram after contacting with gas, after being filtered, enter atomizer, be again atomized, so recycle.
Because the gas that 300 atomizations are processed through atomization process chamber can be with the liquid being atomized, in the gas with atomized liquid enters deceleration cooling processing chamber 400, atomized liquid in the time of by deceleration cooling processing in gas know from experience because temperature compared with low coagulation in deceleration tube 410, for the atomized liquid to this part recycles, described the first breather pipe 411 and the 3rd breather pipe 413 are obliquely installed, one end that the first breather pipe 411 is connected with the second breather pipe 412 is higher than the other end, one end that the 3rd breather pipe 413 is connected with the second breather pipe 412 is higher than the other end: like this, the atomized liquid condensing in deceleration tube 410 is known from experience along the first breather pipe 411 being obliquely installed and the 3rd breather pipe 413 outflow deceleration tubes 410, be retained in 400 bottoms, deceleration cooling processing chamber, 400 bottoms, deceleration cooling processing chamber are provided with back liquid receiving mouth, and described time liquid receiving mouth connects filter, and filter is connected with atomizer, after being filtered, enters atomizer, is again atomized, and so recycles.
In order to carry power for whole large dust and waste gas treatment device, make large dust waste gas enter successively dust process chamber 200, atomization process chamber 300 and deceleration cooling processing chamber 400, described large dust and waste gas treatment device also comprises extractor fan, and described extractor fan can be arranged at the first air inlet 230 places or the 3rd exhaust outlet 420 places.
Described atomizer can adopt high-pressure atomizer or electrothermal atomizer according to actual needs.
The waste gas that atomized liquid in described atomization process chamber 300 can be processed according to actual needs and determining, can be water, can be also other can with the liquid of waste gas reaction, as NaOH, methyl alcohol, ethanol, etc.
This large dust and waste gas treatment device can be applicable in the processing occasion that in waste gas, Dust Capacity is larger, if ceramic manufactory, cement manufactory and steel-making manufactory are in the processing of dust, etc.; Utilize dust process chamber 200 first the big dust particle in waste gas to be carried out to precipitation process, then waste gas is carried out to follow-up processing, the dust in waste gas is effectively addressed, meet the processing requirements of large dust waste gas.
For this large dust and waste gas treatment device is maximized the use; can on the housing 100 of this large dust and waste gas treatment device, print various public service ads and environmental protection poster; not only can strengthen the attention to large dust exhaust-gas treatment and environmental protection, can also beautify this large dust and waste gas treatment device.
The operation of this large dust and waste gas treatment device is as follows: pending large dust waste gas enters dust process chamber 200 by the first air inlet 230, by gas distribution plate 240, be assigned to equably in the fine dust bag 211 of each carbon and carried out dust removal process, through fine dust bag 211 exhaust ends of carbon, discharge and enter exhaust portion 220, through first row gas port, discharge exhaust portion 220, through the second air inlet being communicated with first row gas port, enter atomization process chamber 300, gas is through the air-vent on pulverizer plate 320, with the abundant haptoreaction of the liquid being atomized, finally by crossing second row gas port, discharge atomization process chamber 300, through the 3rd air inlet being communicated with second row gas port, enter deceleration cooling processing chamber 400, by being evenly dispersed in each deceleration tube 410 with the 3rd air inlet, by being arranged to the deceleration tube 410 of hierarchic structure, the speed of gas is lowered greatly, and the simultaneously processing of lowering the temperature of the gas in 440 pairs of deceleration tubes 410 of cooling tube, makes gas reach discharge standard, through the 3rd exhaust outlet 420, discharge deceleration cooling processing chamber 400, so far, gas completes whole processing, discharges waste odour-gas treating apparatus.
This large dust and waste gas treatment device, by dust process chamber, the main process chamber of atomization process chamber and three of deceleration cooling processing chambers are set, carries out rough dusting precipitation process to large dust waste gas, atomization reaction treatment and last deceleration cooling processing; The large dust waste gas and the discharge standard that need to reach different according to reality, this large dust and waste gas treatment device can also suitably be out of shape according to actual needs, makes the applied widely of large dust and waste gas treatment device, and processing cost is low, simple to operate, meet the processing requirements of large dust waste gas.
Should be understood that; application of the present utility model is not limited to above-mentioned giving an example; for those of ordinary skills, can be improved according to the above description or convert, all these improvement and conversion all should belong to the protection domain of the utility model claims.
Claims (8)
1. a large dust and waste gas treatment device, it is characterized in that, comprise housing, be provided with dust process chamber, atomization process chamber and deceleration cooling processing chamber in described housing, large dust waste gas enters successively dust process chamber, atomization process chamber and deceleration cooling processing chamber and processes discharge;
Described dust process chamber comprises dedusting portion and exhaust portion, in described dust process chamber, is provided with the first air inlet, is provided with first row gas port in described exhaust portion; In described dedusting portion, be evenly provided with the fine dust bags of a plurality of carbon, the fine dust bag inlet end of carbon is connected with the first air inlet;
On described atomization process chamber, be provided with the second air inlet and second row gas port, described the second air inlet is communicated with first row gas port; In described atomization process chamber, be evenly provided with a plurality of pulverizer plates, be provided with mist pipe on pulverizer plate, mist pipe is by the external atomized liquid of atomizer; On pulverizer plate, be also evenly provided with a plurality of air-vents;
Described deceleration cooling processing chamber comprises the 3rd air inlet and the 3rd exhaust outlet, and the 3rd air inlet is communicated with second row gas port; Described deceleration cooling processing is indoor is also evenly provided with many deceleration tubes, and deceleration tube runs through whole deceleration cooling processing chamber, and described deceleration tube comprises the first breather pipe, the second breather pipe and the 3rd breather pipe; Described second breather pipe one end connects the first breather pipe, and the other end connects the 3rd breather pipe; Described the first breather pipe, the second breather pipe and the 3rd breather pipe form the shape of hierarchic structure; Indoor a plurality of cooling tubes, the external cooling fluid of described cooling tube of being also provided with of described deceleration cooling processing.
2. large dust and waste gas treatment device according to claim 1, is characterized in that, described dust process chamber, atomization process chamber and deceleration cooling processing chamber can arrange a plurality of according to actual needs.
3. large dust and waste gas treatment device according to claim 2, is characterized in that, between described the first air inlet and the fine dust bag inlet end of carbon, is provided with gas distribution plate, on described gas distribution plate, is evenly provided with a plurality of minutes pores.
4. large dust and waste gas treatment device according to claim 3, it is characterized in that, the exhaust end bottom gap of the fine dust bag of described carbon is provided with the bucket that gathers dust, and exhaust end bottom does not contact with the bucket that gathers dust, the described bucket that gathers dust is arranged to funnel structure, and the upper end of the bucket that gathers dust is provided with switch flashboard.
5. large dust and waste gas treatment device according to claim 4, is characterized in that, the bottom of described atomization process chamber is provided with atomized liquid mouth, and described atomized liquid mouth connects filter, and filter is connected with atomizer.
6. large dust and waste gas treatment device according to claim 5, it is characterized in that, described the first breather pipe and the 3rd breather pipe are obliquely installed, and one end that the first breather pipe is connected with the second breather pipe is higher than the other end, and one end that the 3rd breather pipe is connected with the second breather pipe is higher than the other end; Bottom, deceleration cooling processing chamber is provided with back liquid receiving mouth, and described time liquid receiving mouth connects filter, and filter is connected with atomizer.
7. large dust and waste gas treatment device according to claim 6, is characterized in that, described large dust and waste gas treatment device also comprises extractor fan, and described extractor fan can be arranged at the first air inlet place or the 3rd exhaust ports.
8. large dust and waste gas treatment device according to claim 7, is characterized in that, described atomizer can adopt high-pressure atomizer or electrothermal atomizer according to actual needs.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420062967.8U CN203816426U (en) | 2014-02-12 | 2014-02-12 | Large dust waste gas treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420062967.8U CN203816426U (en) | 2014-02-12 | 2014-02-12 | Large dust waste gas treatment device |
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| Publication Number | Publication Date |
|---|---|
| CN203816426U true CN203816426U (en) | 2014-09-10 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201420062967.8U Expired - Fee Related CN203816426U (en) | 2014-02-12 | 2014-02-12 | Large dust waste gas treatment device |
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| CN (1) | CN203816426U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109488035A (en) * | 2018-11-06 | 2019-03-19 | 陈玉振 | Dust-extraction unit is used in a kind of construction protection |
-
2014
- 2014-02-12 CN CN201420062967.8U patent/CN203816426U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109488035A (en) * | 2018-11-06 | 2019-03-19 | 陈玉振 | Dust-extraction unit is used in a kind of construction protection |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140910 Termination date: 20200212 |