CN203170176U - Combined dust remover - Google Patents
Combined dust remover Download PDFInfo
- Publication number
- CN203170176U CN203170176U CN 201320170588 CN201320170588U CN203170176U CN 203170176 U CN203170176 U CN 203170176U CN 201320170588 CN201320170588 CN 201320170588 CN 201320170588 U CN201320170588 U CN 201320170588U CN 203170176 U CN203170176 U CN 203170176U
- Authority
- CN
- China
- Prior art keywords
- catch basin
- differential
- air inlet
- petticoat pipe
- dehydration
- 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.)
- Expired - Fee Related
Links
- 239000000428 dust Substances 0.000 title claims abstract description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 29
- 238000006297 dehydration reaction Methods 0.000 claims abstract description 22
- 229910000831 Steel Inorganic materials 0.000 claims abstract description 19
- 239000010959 steel Substances 0.000 claims abstract description 19
- 229920000742 Cotton Polymers 0.000 claims abstract description 8
- 238000009434 installation Methods 0.000 claims description 9
- 206010016807 Fluid retention Diseases 0.000 claims description 3
- 238000007654 immersion Methods 0.000 claims description 3
- 230000000717 retained Effects 0.000 claims description 2
- 238000001914 filtration Methods 0.000 abstract description 4
- 238000007599 discharging Methods 0.000 abstract description 2
- 239000000779 smoke Substances 0.000 abstract 3
- 230000001681 protective Effects 0.000 abstract 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 16
- 239000003546 flue gas Substances 0.000 description 9
- 238000005516 engineering process Methods 0.000 description 7
- 241000219146 Gossypium Species 0.000 description 5
- 239000002912 waste gas Substances 0.000 description 5
- 239000007789 gas Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000000746 purification Methods 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-N Carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000000249 desinfective Effects 0.000 description 1
- 238000005755 formation reaction Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000006011 modification reaction Methods 0.000 description 1
- 230000003020 moisturizing Effects 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000035943 smell Effects 0.000 description 1
- 230000001954 sterilising Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Abstract
The utility model discloses a combined dust remover. The combined dust remover comprises a differential submerged dust-removing device, a dehydration layer and an air outlet filtering device, wherein the differential submerged dust-removing device is formed by a smoke inlet pipe, an air inlet smoke cover, a tapered flow guide plate, two layers or a plurality of layers of differential perforated plates, a baffle, a floating ball water inlet valve, a dirt discharging valve and a water storing groove; the dehydration layer is formed by an integrated structure of a steel structure framework and a supporting net, and a multi-face hollow sphere; and the air outlet filtering device is formed by an integrated structure of the steel structure framework and a protective net, and filtering cotton. The combined dust remover is high in dust removal and dehydration integration efficiency, low in setting cost, simple in structure and long in service life, and is water-saving and power-saving, low in operation cost, simple and convenient to operate, and safe and reliable in operation. The combined dust remover is particularly applied to dust removing of mediums including small-size industrial smoke and the like.
Description
Technical field
The utility model relates to a kind of dedusting technology field, especially the complex dust collector that can purify flue gas effectively.
Background technology
Exhaust-gas treatment claims waste gas purification again.Exhaust-gas treatment refers to the waste gas that produces at industrial site, factory floor and carry out preliminary treatment before externally discharging, to reach the work of the external emission standards of national waste gas.General exhaust-gas treatment has comprised aspects such as organic exhaust gas processing, dust exhaust-gas treatment, soda acid exhaust-gas treatment, peculiar smell exhaust-gas treatment and air disinfection sterilizing and purifying.The flue gas purifying technique form is more, by whether there being waste water to discharge in its system, can be divided into three kinds of wet methods, semidry method, dry method.Every kind of technology has multiple combining form that pluses and minuses are also arranged.
Treatment process comprises wet cleaning technology, semidry method process for purifying, dry purification process, and the pollutant purification of wet cleaning technology comparatively speaking is most effective, can satisfy strict emission control standards.But the characteristics of wet cleaning technology are the flow process complexity, and corollary equipment is more, and one-time investment and operating cost are higher, and numerous little little enterprises are difficult to bear.
Summary of the invention
In order to overcome existing deduster one-time investment and the higher deficiency of operating cost, the utility model provides a kind of complex dust collector, this complex dust collector not only purification efficiency is the highest, can satisfy strict emission control standards, and cost is low, easy construction, operating cost is low, need not maintenance, and is safe and reliable to operation.
The technical scheme that its technical problem that solves the utility model adopts is: a kind of complex dust collector comprises differential diving dust arrester, dehydration layer, the filter of giving vent to anger.Differential diving dust arrester is made up of smoke-intake pipe, air inlet petticoat pipe, conical baffle, two layers or multilayer differential perforated plate, baffle plate, ball float water intaking valve, blowoff valve, catch basin; The dehydration series of strata are made up of steel structure frame and support mesh integral structure and multiaspect hollow ball; The filter of giving vent to anger is made up of steel structure frame and protection network integral structure and filter cotton.Described air inlet petticoat pipe is the cone expansion body, and top is connected by flange with smoke-intake pipe, and conical baffle is arranged on air inlet petticoat pipe below, is connected immersion water plane, air inlet petticoat pipe bottom with the air inlet petticoat pipe by lacing wire.Upper strata differential perforated plate is installed air inlet petticoat pipe bottom, catch basin side and baffle plate, the flat following and average row of the water surface of the water surface, and lower floor's differential perforated plate is installed in air inlet petticoat pipe bottom, up is sloping shape with catch basin side and baffle plate four sides and tilts.Lower floor's differential perforated plate up is sloping shape and tilts to be conducive to waste gas evenly by lower floor's differential perforated plate, and increase waste gas contacts with water, improves clean-up effect.Described catch basin bottom is sloping shape and tilts, and blowoff valve is installed in catch basin inner slope low side surface; Described dehydration layer steel structure frame and support mesh integral structure are placed on the installation L shaped steel of catch basin medial surface, place the multiaspect hollow ball above.The multiaspect hollow ball has that blade is many, resistance is little, specific area is big, can fully solve advantages such as gas-liquid exchange.Dehydration layer is retained certain horizontal plane by on the catch basin blowoff valve installation site, and baffle plate is installed in below the dehydration layer side, and the ball float water intaking valve is installed on the retention water surface on the catch basin blowoff valve installation site.The steel structure frame of the described filter of giving vent to anger and protection network integral structure use hinge to be installed in the catch basin top, in filter cotton is set.
The technical work principle: ash-laden gas enters the air inlet petticoat pipe through smoke-intake pipe, enter in the water by the conical baffle shunting, flue gas passes lower floor's differential perforated plate with flue gas differential in water, passes upper strata differential perforated plate more further with flue gas tiny bubble differential behind the formation tiny bubble.Force flue gas fully to contact with water, fully react, fully wash; Gas-liquid two-phase fully contacts, and the pollutant in the flue gas is fully absorbed by water; Flue gas after being purified rises to the dehydration layer, contacts dehydration with the multiaspect hollow ball, and the water of deviating from flows in the catch basin, and dust sinks under the water and regularly discharges through blowoff valve, and the Purge gas after the dehydration directly enters atmosphere after filtering through filter pulp again.After the water surface of catch basin reduced, the ball float water intaking valve started moisturizing automatically.In order to reach better udst separation effect, according to different ash-laden gas character, can in water, add different additives to improve the efficiency of dust collection of ash-laden gas.
The beneficial effects of the utility model are that complex dust collector is with domestic existing similar technology comparison at present and following characteristics are arranged: 1, the dewatering integrated efficient height of dedusting; 2, arrange that cost is low, simple in structure, long service life; 3, water-saving, power saving, operating cost are low; 4, easy and simple to handle, safe and reliable to operation.Be applied to the dedusting of media such as back yard industry flue gas especially.
Below in conjunction with the drawings and specific embodiments the utility model is further described.
Description of drawings
Fig. 1 is the sectional structural map of facing of first embodiment of the utility model;
Fig. 2 is the side-looking sectional structural map of Fig. 1;
Fig. 3 is the sectional structural map of overlooking of Fig. 1;
1. dehydration layers among the figure, the filter of 2. giving vent to anger, 3. smoke-intake pipe, 4. air inlet petticoat pipe, 5. conical baffle, 6. differential perforated plate, 7. baffle plate, 8. ball float water intaking valve, 9. blowoff valve, 10. catch basin, 11. steel structure frames, 12. support mesh, 13. the multiaspect hollow ball, 14. protection networks, 15. filter cottons, 16. flange, 17. lacing wires, 18. horizontal planes, 19.L shaped steel, 20. hinges, 21. snap closes.
The specific embodiment
At the embodiment shown in Fig. 1,2,3, comprise differential diving dust arrester, dehydration layer (1), the filter of giving vent to anger (2).Differential diving dust arrester is made up of smoke-intake pipe (3), air inlet petticoat pipe (4), conical baffle (5), two layers or multilayer differential perforated plate (6), baffle plate (7), ball float water intaking valve (8), blowoff valve (9), catch basin (10); Dehydration layer (1) is to be made up of steel structure frame (11) and support mesh (12) integral structure and multiaspect hollow ball (13); The filter (2) of giving vent to anger is made up of steel structure frame (11) and protection network (14) integral structure and filter cotton (15).Described air inlet petticoat pipe (4) is the cone expansion body, top is connected by flange (16) with smoke-intake pipe (3), conical baffle (5) is arranged on air inlet petticoat pipe (4) below, is connected immersion water plane, air inlet petticoat pipe (4) bottom (18) with air inlet petticoat pipe (4) by lacing wire (17).Upper strata differential perforated plate (6) is installed air inlet petticoat pipe (2) bottom, catch basin (10) side and baffle plate (7), the water surface flat (18) is following parallel with the water surface flat (18), lower floor's differential perforated plate (6) is installed in air inlet petticoat pipe (2) bottom, up is sloping shape with catch basin (10) side and baffle plate (7) four sides and tilts.Described catch basin (10) bottom is sloping shape and tilts, and blowoff valve (9) is installed in catch basin (10) inner slope low side surface; Described dehydration layer (1) steel structure frame (11) is placed on the installation L shaped steel (19) of catch basin (10) medial surface with support mesh (12) integral structure, places multiaspect hollow ball (13) above.Dehydration layer (1) is leaning on catch basin (10) blowoff valve (9) installation site, retain certain horizontal plane (18), baffle plate (7) is installed in dehydration layer (1) below the side, and ball float water intaking valve (8) is installed on the retention water water surface (18) on catch basin (10) blowoff valve (9) installation site.The steel structure frame (11) of the described filter of giving vent to anger (2) and protection network (14) integral structure use hinge (20) and snap close (21) to be installed in catch basin (10) top, in filter cotton (15) is set.
Should be appreciated that in not breaking away from scope of the present utility model, can make multiple change to above-described embodiment, and be applied to other occasions.All any modifications of within spirit of the present utility model and principle, doing, be equal to and replace and improvement etc., all should be included within the protection domain of the present utility model.
Claims (5)
1. complex dust collector, comprise differential diving dust arrester, dehydration layer, the filter of giving vent to anger, it is characterized in that: differential diving dust arrester is made up of smoke-intake pipe, air inlet petticoat pipe, conical baffle, two layers or multilayer differential perforated plate, baffle plate, ball float water intaking valve, blowoff valve, catch basin; The dehydration series of strata are made up of steel structure frame and support mesh integral structure and multiaspect hollow ball; The filter of giving vent to anger is made up of steel structure frame and protection network integral structure and filter cotton.
2. complex dust collector according to claim 1, it is characterized in that: described air inlet petticoat pipe is the cone expansion body, and top is connected by flange with smoke-intake pipe, and conical baffle is arranged on air inlet petticoat pipe below, be connected immersion water plane, air inlet petticoat pipe bottom with the air inlet petticoat pipe by lacing wire.
3. complex dust collector according to claim 1, it is characterized in that: upper strata differential perforated plate is installed air inlet petticoat pipe bottom, catch basin side and baffle plate, the flat following and average row of the water surface of the water surface, lower floor's differential perforated plate is installed in air inlet petticoat pipe bottom, up is sloping shape with catch basin side and baffle plate four sides and tilts.
4. complex dust collector according to claim 1 is characterized in that: described catch basin bottom is sloping shape and tilts, and blowoff valve is installed in catch basin inner slope low side surface; Described dehydration layer steel structure frame and support mesh integral structure are placed on the installation L shaped steel of catch basin medial surface, place the multiaspect hollow ball above; Dehydration layer is retained certain horizontal plane by on the catch basin blowoff valve installation site, and baffle plate is installed in below the dehydration layer side, and the ball float water intaking valve is installed on the retention water surface on the catch basin blowoff valve installation site.
5. complex dust collector according to claim 1 is characterized in that: the steel structure frame of the described filter of giving vent to anger and protection network integral structure use hinge to be installed in the catch basin top, in filter cotton is set.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320170588 CN203170176U (en) | 2013-04-08 | 2013-04-08 | Combined dust remover |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320170588 CN203170176U (en) | 2013-04-08 | 2013-04-08 | Combined dust remover |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203170176U true CN203170176U (en) | 2013-09-04 |
Family
ID=49066931
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320170588 Expired - Fee Related CN203170176U (en) | 2013-04-08 | 2013-04-08 | Combined dust remover |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203170176U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105275542A (en) * | 2015-12-04 | 2016-01-27 | 广西玉柴机器股份有限公司 | Engine respirator |
| CN110384998A (en) * | 2019-07-26 | 2019-10-29 | 苏州萨瑟斯兰环境科技有限公司 | A kind of simultaneously cleaning industrial dedusting device |
-
2013
- 2013-04-08 CN CN 201320170588 patent/CN203170176U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105275542A (en) * | 2015-12-04 | 2016-01-27 | 广西玉柴机器股份有限公司 | Engine respirator |
| CN105275542B (en) * | 2015-12-04 | 2019-01-11 | 广西玉柴机器股份有限公司 | Rebreather of engine |
| CN110384998A (en) * | 2019-07-26 | 2019-10-29 | 苏州萨瑟斯兰环境科技有限公司 | A kind of simultaneously cleaning industrial dedusting device |
| CN110384998B (en) * | 2019-07-26 | 2021-09-21 | 威海世一电子有限公司 | Synchronous cleaning industrial dust removal device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130904 Termination date: 20140408 |