CN203170176U - Combined dust remover - Google Patents

Combined dust remover Download PDF

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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
Application number
CN 201320170588
Other languages
Chinese (zh)
Inventor
林嘉祥
陈清芳
庄国法
黄智金
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
XIAMEN JIADA GREEN CONSTRUCTION ENGINEERING Co Ltd
Original Assignee
XIAMEN JIADA GREEN CONSTRUCTION ENGINEERING Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by XIAMEN JIADA GREEN CONSTRUCTION ENGINEERING Co Ltd filed Critical XIAMEN JIADA GREEN CONSTRUCTION ENGINEERING Co Ltd
Priority to CN 201320170588 priority Critical patent/CN203170176U/en
Application granted granted Critical
Publication of CN203170176U publication Critical patent/CN203170176U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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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

Complex dust collector
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.
CN 201320170588 2013-04-08 2013-04-08 Combined dust remover Expired - Fee Related CN203170176U (en)

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)

* Cited by examiner, † Cited by third party
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

Cited By (4)

* Cited by examiner, † Cited by third party
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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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