CN106731354A - A kind of flue gas of refuse burning processing system - Google Patents

A kind of flue gas of refuse burning processing system Download PDF

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Publication number
CN106731354A
CN106731354A CN201710055647.8A CN201710055647A CN106731354A CN 106731354 A CN106731354 A CN 106731354A CN 201710055647 A CN201710055647 A CN 201710055647A CN 106731354 A CN106731354 A CN 106731354A
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Prior art keywords
water washing
pipeline
flue gas
processing system
washing tank
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CN201710055647.8A
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Chinese (zh)
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朱肖州
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Individual
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Priority to CN201710055647.8A priority Critical patent/CN106731354A/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D47/00Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/06Spray cleaning
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D36/00Filter circuits or combinations of filters with other separating devices
    • B01D36/04Combinations of filters with settling tanks
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D50/00Combinations of methods or devices for separating particles from gases or vapours
    • B01D50/60Combinations of devices covered by groups B01D46/00 and B01D47/00
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/002Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by condensation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B01D53/04Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1425Regeneration of liquid absorbents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1456Removing acid components
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1487Removing organic compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/18Absorbing units; Liquid distributors therefor

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Treating Waste Gases (AREA)

Abstract

The invention discloses a kind of flue gas of refuse burning processing system, including water washing device, liquefying plant and filter;Described water washing device is connected by pipeline A with liquefying plant;Described liquefying plant is connected by pipeline B with filter;Described water washing device includes inlet manifold, sedimentation basin, water washing tank and sprinkler part;Described liquefying plant includes gas pipeline, drive device, the hydraulic turbine and cistern;Described filter includes housing, active carbon layer and gas outlet;Described inlet manifold, pipeline A, gas pipeline and pipeline B are sequentially connected.The present invention includes water washing device, liquefying plant and filter, can will burn the dense smoke for producing carries out water washing cleaning, high-pressure atomization and filtering emission operation one by one, simple structure, process engineering rationally, effectively overcomes the smoke pollution problem of waste incineration.

Description

A kind of flue gas of refuse burning processing system
Technical field
The invention belongs to Purificatory Technology field, it is related to a kind of flue gas of refuse burning processing system.
Background technology
With expanding economy, the yield of house refuse also increases constantly.Current domestic rubbish disposal mode, it is main There are sanitary landfills, three kinds of methods of During High-Temperature Composting and burn sintering energy.Because sanitary landfills and During High-Temperature Composting two ways can be produced More serious problem of environmental pollution, thus burn sintering energy processing mode is the direction of urban garbage disposal.But burn House refuse is harmful into by containing a large amount of dioxin, heavy metal, HCl etc. in the flue gas produced after high temperature incineration during system can be processed Point, it is therefore necessary to qualified discharge after processing flue gas.With carrying forward vigorously for national energy-saving emission reduction policy, discarded object is arranged The standard requirement put is increasingly stricter, and advance, reliability to flue-gas cleaning devices, security, applicability it is also proposed more Requirement high.
And current fume treatment auxiliary be usually present complex structure, high cost, clean-up effect difference the problems such as, be unfavorable for Flue gas of refuse burning treatment technology is widely popularized and long-term use.
The content of the invention
The present invention is in order to overcome the deficiencies in the prior art, there is provided one kind integrates washing, atomization and filtering emission, only Change efficiency high, practical flue gas of refuse burning processing system.
To achieve these goals, technical scheme is as follows:
A kind of flue gas of refuse burning processing system, including water washing device, liquefying plant and filter;Described water washing device leads to Piping A is connected with liquefying plant;Described liquefying plant is connected by pipeline B with filter;
Described water washing device includes inlet manifold, sedimentation basin, water washing tank and sprinkler part;The top of described water washing tank with enter Gas house steward connects;Described water washing tank is installed in sedimentation basin;Described sprinkler part includes spray house steward, shower and spray Device;A pair of showers are provided with described water washing tank, shower is longitudinally mounted in water washing tank;Described shower is connected in parallel to spray Drench on house steward;Spray thrower is uniformly provided with described shower, the spray thrower on a pair of showers in water washing tank interlocks peace Dress;
Described liquefying plant includes gas pipeline, drive device, the hydraulic turbine and cistern;Described drive device and the hydraulic turbine Connection;The described hydraulic turbine is fixed in cistern by bearing;Described gas pipeline is connected with the hydraulic turbine;
Described filter includes housing, active carbon layer and gas outlet;The outlet of described gas pipeline and the top of housing Connection;Described active carbon layer is located at housing central section, and there is gap with housing bottom;Described gas outlet is upper located at housing Side;
Described inlet manifold, pipeline A, gas pipeline and pipeline B are sequentially connected.
The flue gas of refuse burning processing system also includes purifier;Described purifier includes multistage infiltration pond, oozes Press cascade arrangement in saturating pond;Described sedimentation basin is provided with water outlet A, and first order osmotic cell is connected with the water outlet A of sedimentation basin; Described osmotic cell includes pond body, permeation unit and water outlet B;Described permeation unit by dividing plate, sand layer of charcoal and pond body side Wall is surrounded;Described dividing plate is arranged in pond body;Height of the thickness of described sand layer of charcoal less than dividing plate;The bottom of described dividing plate Portion is concordant with the bottom of sand layer of charcoal, exists with pond body bottom and is spaced;The side wall of described osmotic cell is provided with delivery port.
Preferably, above-described water washing tank has-group;Described water washing tank is staggered installed in precipitation by front and back position In pond.Water washing tank is arranged in " product " font or " V " type, reduces floor space,
Preferably, the above-described hydraulic turbine includes circular housing, blade and drive shaft;Described blade is distributed on drive shaft On;Breach is provided with below described circular housing;The bottom of described circular housing/-/place immersion cistern liquid level under Side;Described drive shaft is connected with drive device.
Preferably, the above-described hydraulic turbine is provided with-group.
As a further improvement, the flue gas of refuse burning processing system also includes also including the circulatory system;Described circulation System includes circulating pump and circulation pipe;Described circulating pump is arranged on the top of osmotic cell;The water inlet pipe peace of described circulating pump Mounted in sand layer of charcoal top, the outlet pipe of circulating pump is connected with one end of circulation pipe;The other end of described circulation pipe is total with spray Pipe is connected.
Preferably, above-described circulating pump is arranged on the top of afterbody osmotic cell.
Preferably, the height of above-described active carbon layer for body height/-/.Gas filtration completely, is realized without dirt Dye discharge.
Preferably, above-described spray thrower is spiral spray thrower.
Operation principle of the invention:The flue gas produced after waste incineration is passed through after inlet manifold enters into water washing tank, in spray In the presence of spray thrower in shower pipe, the sediment in flue gas is settled down in sedimentation basin completely;Flue gas after cleaning passes through pipeline A Enter into liquefaction system, drive device impeller machine is synchronized with the movement, turbine drives the water in cistern to rotate at a high speed, leaf In turbine pressure increase, into turbine flue gas in the presence of high-pressure cold water transient liquefaction, the fog for eventually forming lead to Piping B enters into filter, by being discharged by filtering after active carbon layer;Sewage in sedimentation basin is by the layer in osmotic cell Layer infiltration, in the presence of sand layer of charcoal, sewage is purified, it is possible to is recycled in water washing tank and is circulated utilization.
The present invention has the advantage that and has the beneficial effect that:
1st, the present invention includes water washing device, liquefying plant and filter, can will burn the dense smoke for producing and be washed one by one Purification, high-pressure atomization and filtering emission operation, simple structure, process engineering rationally, effectively overcome waste incineration Smoke pollution problem.
2nd, of the invention that a pair of showers are installed in each water washing tank, the spray thrower on a pair of showers is staggered installation of, The spray without dead angle is realized, so as to fully be washed to entering the flue gas in water washing tank, it is ensured that the washing cooling purification of flue gas Effect.
3rd, multigroup water washing tank of the invention is staggered installation of by front and back position, is arranged in " product " font or " V " type, is reduced and is accounted for Ground area, improves the practicality of device.
4th, the present invention devises liquefying plant, in the presence of the hydraulic turbine drives liquid at high speed to rotate, improves in the hydraulic turbine Pressure, flue gas encounters high-pressure cold water transient liquefaction, reduces the final discharge of gas, while having reached further washing cigarette The purpose of gas, strengthens the purification function to flue gas.
5th, the outer casing bottom of the hydraulic turbine of the invention is provided with breach, and top is connected with gas pipeline, when the spindle is rotated, leaf Piece drives water to rotate at a high speed, and high pressure is formd in shell, and the gas in gas pipeline is fast after running into cold water in hyperbaric environment Speed liquefaction, reduces the discharge of gas, and design science is reasonable, simple structure, with very strong practicality.
6th, the present invention is provided with multistage infiltration pond, and using the principle of underground water, the sewage to settling acquisition in sedimentation basin is carried out Permeation filtration, finally obtained the water after purification step by step, reduce the discharge of sewage.
7th, the present invention realizes the recycling of water by circulation pipe by the water circulation after permeation filtration to water washing tank, Efficent use of resources.
Brief description of the drawings
Fig. 1 is structural representation of the invention.
Fig. 2 is the partial schematic diagram in Fig. 1.
Fig. 3 is the schematic top plan view of the water washing device of embodiment 3.
Accompanying drawing is identified:
101- inlet manifold, 102- spray house stewards, 103- water washing tanks, 104- water outlet As, 105- sedimentation basins, 106- showers, 107- spray throwers;
2- pipelines A;
301- gas pipelines, the 302- hydraulic turbines, 303- cisterns, 304- blades, 305- drive shafts, 306- circular housings, 307- Drive device;
4- pipelines B;
501- housings, 502- active carbon layers, 503- gas outlets;
601- circulation pipes, 602- circulating pumps;
701- osmotic cells, 702- pond bodies, 703- dividing plates, 704- sand layer of charcoal;705- water outlet Bs.
Specific embodiment
The present invention will be further described below in conjunction with the accompanying drawings.
Embodiment 1:
A kind of flue gas of refuse burning processing system, including water washing device, liquefying plant and filter;Described water washing device leads to Piping A2 is connected with liquefying plant;Described liquefying plant is connected by pipeline B4 with filter.
Described water washing device includes inlet manifold 101, sedimentation basin 105, water washing tank 103 and sprinkler part;Described water The top of cleaning of evaporator 103 is connected with inlet manifold 101;4-8 groups water washing tank 103 is provided with, water washing tank 103 interlocks in product by front and back position Font arrangement is arranged in sedimentation basin 105;Described sprinkler part includes spray house steward 102, shower 106 and spray thrower 107; A pair of showers 106 are provided with described water washing tank 103, shower 106 is longitudinally mounted in water washing tank 103;Described spray Pipe 106 is connected in parallel on spray house steward 102;Spray thrower 107, in water washing tank 103 one have been uniformly provided with described shower 106 Spray thrower 107 on shower 106 is staggered installation of;Described spray thrower 107 is spiral spray thrower 107.
Described liquefying plant includes gas pipeline 301, drive device 307, the hydraulic turbine 302 and cistern 303;Described Drive device 307 is connected with the hydraulic turbine 302;The described hydraulic turbine 302 is fixed in cistern 303 by bearing, is provided with 3 groups of water Turbine 302;Described gas pipeline 301 is connected with the hydraulic turbine 302.
The described hydraulic turbine 302 includes circular housing 306, blade 304 and drive shaft 305;Described blade 304 is distributed on In drive shaft 305;The lower section of described circular housing 306 is provided with breach;The 1/4-1/3 of the bottom of described circular housing 306 The liquid level lower section of place's immersion cistern 303;Described drive shaft 305 is connected with drive device 307.
Described filter includes housing 501, active carbon layer 502 and gas outlet 503;Described gas pipeline 301 Outlet is connected with the top of housing 501;Described active carbon layer 502 exists located at the middle part of housing 501 with the bottom of housing 501 Gap;The height of active carbon layer 502 is the 2/3-3/4 of the height of housing 501;Described gas outlet 503 is upper located at housing 501 Side.
Described inlet manifold 101, pipeline A2, gas pipeline 301 and pipeline B4 are sequentially connected.
The flue gas produced after waste incineration is passed through after inlet manifold 101 enters into water washing tank 103, on shower 106 In the presence of spiral spray thrower 107, the sediment in flue gas is settled down in sedimentation basin 105 completely;Flue gas after cleaning passes through Pipeline A2 is entered into liquefaction system, and the impeller machine 302 of drive device 307 is synchronized with the movement, and turbine 302 drives cistern Water in 303 rotates at a high speed, the pressure increase in turbine 302, and the flue gas into turbine 302 is in the presence of high-pressure cold water Transient liquefaction, the fog for eventually forming enters into filter by pipeline B4, by being discharged by filtering after active carbon layer 502. By the infiltration layer by layer in osmotic cell, in the presence of sand layer of charcoal, sewage is purified sewage in sedimentation basin, it is possible to circulate Utilization is circulated into water washing tank.
Embodiment 2:
The embodiment difference from Example 1 is:
Water washing device is provided with 6 groups of water washing tanks 103, and water washing tank 103 interlocks by front and back position and be arranged on sedimentation basin in V-shape arrangement In 105, liquefying plant is provided with 4 groups of hydraulic turbines.The flue gas of refuse burning processing system also includes purifier;Described purification dress Put including multistage infiltration pond 701, osmotic cell 701 presses cascade arrangement;Described sedimentation basin 105 is provided with water outlet A 104, the One-level osmotic cell 701 is connected with the water outlet A 104 of sedimentation basin 105;Described osmotic cell 701 includes pond body 702, permeation unit With water outlet B 705;Described permeation unit is surrounded by the side wall of dividing plate 703, sand layer of charcoal 704 and pond body 702;Described dividing plate 703 are arranged in pond body 702;Height of the thickness of described sand layer of charcoal 704 less than dividing plate 703;The bottom of described dividing plate 703 Bottom with sand layer of charcoal 704 is concordant, exists with the bottom of pond body 702 and is spaced;The side wall of described osmotic cell 701 is provided with water outlet Mouthful.By the infiltration layer by layer in osmotic cell 701, in the presence of sand layer of charcoal 704, sewage purification is obtained sewage in sedimentation basin 105 To recycle.
Embodiment 3:
The embodiment difference from Example 2 is:
Water washing device is provided with 8 groups of water washing tanks 103, and water washing tank 103 interlocks by front and back position and be arranged on sedimentation basin in Chinese character pin-shaped arrangement In 105.The flue gas of refuse burning processing system also includes the circulatory system;The described circulatory system includes circulating pump 602 and circulation Pipe 601;Described circulating pump 602 is arranged on the top of afterbody osmotic cell 701;The water inlet pipe peace of described circulating pump 602 Mounted in the top of sand layer of charcoal 704, the outlet pipe of circulating pump 602 is connected with one end of circulation pipe 601;Described circulation pipe 601 it is another One end is connected with spray house steward 102.Sewage in sedimentation basin 105 passes through the infiltration layer by layer in osmotic cell 701, in sand layer of charcoal 704 In the presence of, sewage is purified, and the water after purification can be recycled in water washing tank 103 by circulation pipe 601 and be circulated profit With.

Claims (9)

1. a kind of flue gas of refuse burning processing system, it is characterised in that:Including water washing device, liquefying plant and filter;Institute The water washing device stated passes through pipeline A(2)It is connected with liquefying plant;Described liquefying plant passes through pipeline B(4)Connect with filter Connect;
Described water washing device includes inlet manifold(101), sedimentation basin(105), water washing tank(103)And sprinkler part;Described Water washing tank(103)Top and inlet manifold(101)Connection;Described water washing tank(103)It is installed on sedimentation basin(105)In;Institute The sprinkler part stated includes spray house steward(102), shower(106)And spray thrower(107);Described water washing tank(103)Inside set There are a pair of showers(106), shower(106)It is longitudinally mounted to water washing tank(103)It is interior;Described shower(106)It is connected in parallel to Spray house steward(102)On;Described shower(106)On be uniformly provided with spray thrower(107), water washing tank(103)Interior a pair Shower(106)On spray thrower(107)It is staggered installation of;
Described liquefying plant includes gas pipeline(301), drive device(307), the hydraulic turbine(302)And cistern(303);Institute The drive device stated(307)With the hydraulic turbine(302)Connection;The described hydraulic turbine(302)Cistern is fixed on by bearing(303) In;Described gas pipeline(301)With the hydraulic turbine(302)Connection;
Described filter includes housing(501), active carbon layer(502)And gas outlet(503);Described gas pipeline (301)Outlet and housing(501)Top connection;Described active carbon layer(502)Located at housing(501)Middle part, and and shell Body(501)There is gap in bottom;Described gas outlet(503)Located at housing(501)Top;
Described inlet manifold(101), pipeline A(2), gas pipeline(301)With pipeline B(4)It is sequentially connected.
2. a kind of flue gas of refuse burning processing system according to claim 1, it is characterised in that:Also include purifier; Described purifier includes multistage infiltration pond(701), osmotic cell(701)By cascade arrangement;Described sedimentation basin(105)On It is provided with water outlet A(104), first order osmotic cell(701)With sedimentation basin(105)Water outlet A(104)Connection;Described infiltration Pond(701)Including pond body(702), permeation unit and water outlet B(705);Described permeation unit is by dividing plate(703), sand layer of charcoal (704)And pond body(702)Side wall surround;Described dividing plate(703)It is arranged at pond body(702)It is interior;Described sand layer of charcoal(704) Thickness be less than dividing plate(703)Height;Described dividing plate(703)Bottom and sand layer of charcoal(704)Bottom it is concordant, with pond body (702)There is interval in bottom;Described osmotic cell(701)Side wall be provided with delivery port.
3. a kind of flue gas of refuse burning processing system according to claim 1, it is characterised in that:Described water washing tank (103)There are 4-8 groups;Described water washing tank(103)It is staggered installed in sedimentation basin by front and back position(105)It is interior.
4. a kind of flue gas of refuse burning processing system according to claim 1, it is characterised in that:The described hydraulic turbine (302)Including circular housing(306), blade(304)And drive shaft(305);Described blade(304)It is distributed on drive shaft (305)On;Described circular housing(306)Lower section be provided with breach;Described circular housing(306)Bottom 1/4-1/3 Place's immersion cistern(303)Liquid level lower section;Described drive shaft(305)With drive device(307)Connection.
5. a kind of flue gas of refuse burning processing system according to claim 1, it is characterised in that:The described hydraulic turbine (302)It is provided with 3-4 groups.
6. a kind of flue gas of refuse burning processing system according to claim 2, it is characterised in that:Also include the circulatory system; The described circulatory system includes circulating pump(602)And circulation pipe(601);Described circulating pump(602)Installed in osmotic cell(701) Top;Described circulating pump(602)Water inlet pipe be arranged on sand layer of charcoal(704)Top, circulating pump(602)Outlet pipe with follow Endless tube(601)One end connection;Described circulation pipe(601)The other end with spray house steward(102)Connection.
7. a kind of flue gas of refuse burning processing system according to claim 6, it is characterised in that:Described circulating pump (602)Installed in afterbody osmotic cell(701)Top.
8. a kind of flue gas of refuse burning processing system according to claim 1, it is characterised in that:Described active carbon layer (502)Height be housing(501)The 2/3-3/4 of height.
9. a kind of flue gas of refuse burning processing system according to claim 1, it is characterised in that:Described spray thrower (107)It is spiral spray thrower(107).
CN201710055647.8A 2017-01-25 2017-01-25 A kind of flue gas of refuse burning processing system Pending CN106731354A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107890732A (en) * 2017-12-21 2018-04-10 中冶焦耐(大连)工程技术有限公司 A kind of vapor absorbing apparatus for adding water humidification dust falling system for coke intermediate bin
CN111888862A (en) * 2020-07-30 2020-11-06 安徽天顺环保设备股份有限公司 Circulating wet dedusting system

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CN203108363U (en) * 2013-03-08 2013-08-07 河南永兴锅炉集团有限公司 Flue-gas-driven centrifugal water film scrubber
CN203790767U (en) * 2014-01-16 2014-08-27 李志伟 Air purifying equipment for removing haze
CN203880722U (en) * 2014-03-13 2014-10-15 北京鑫睿胜达科技有限公司 Waste gas treatment tank
CN205269237U (en) * 2016-01-15 2016-06-01 张纯龙 Industrial sewage treatment filter equipment
CN205517195U (en) * 2016-02-01 2016-08-31 潘卓兮 Be used for garbage incinerator smoke and dust purifier
CN205635178U (en) * 2016-05-16 2016-10-12 苏凤全 Cascaded infiltration sewage treatment plant
CN206837724U (en) * 2017-01-25 2018-01-05 朱肖州 A kind of flue gas of refuse burning processing system

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102674631A (en) * 2012-05-10 2012-09-19 复旦大学 Method and system for advanced treatment of centralized rural domestic sewage
CN203108363U (en) * 2013-03-08 2013-08-07 河南永兴锅炉集团有限公司 Flue-gas-driven centrifugal water film scrubber
CN203790767U (en) * 2014-01-16 2014-08-27 李志伟 Air purifying equipment for removing haze
CN203880722U (en) * 2014-03-13 2014-10-15 北京鑫睿胜达科技有限公司 Waste gas treatment tank
CN205269237U (en) * 2016-01-15 2016-06-01 张纯龙 Industrial sewage treatment filter equipment
CN205517195U (en) * 2016-02-01 2016-08-31 潘卓兮 Be used for garbage incinerator smoke and dust purifier
CN205635178U (en) * 2016-05-16 2016-10-12 苏凤全 Cascaded infiltration sewage treatment plant
CN206837724U (en) * 2017-01-25 2018-01-05 朱肖州 A kind of flue gas of refuse burning processing system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107890732A (en) * 2017-12-21 2018-04-10 中冶焦耐(大连)工程技术有限公司 A kind of vapor absorbing apparatus for adding water humidification dust falling system for coke intermediate bin
CN111888862A (en) * 2020-07-30 2020-11-06 安徽天顺环保设备股份有限公司 Circulating wet dedusting system

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Application publication date: 20170531

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