CN108889082A - A kind of emission-control equipment - Google Patents
A kind of emission-control equipment Download PDFInfo
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- CN108889082A CN108889082A CN201810801514.5A CN201810801514A CN108889082A CN 108889082 A CN108889082 A CN 108889082A CN 201810801514 A CN201810801514 A CN 201810801514A CN 108889082 A CN108889082 A CN 108889082A
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- Prior art keywords
- water
- soluble
- cabinet
- gas pipeline
- blower
- Prior art date
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 60
- 238000006243 chemical reaction Methods 0.000 claims abstract description 20
- 238000010438 heat treatment Methods 0.000 claims abstract description 9
- 230000004888 barrier function Effects 0.000 claims description 11
- 238000005192 partition Methods 0.000 claims description 6
- 230000007246 mechanism Effects 0.000 claims description 4
- 241000883990 Flabellum Species 0.000 claims description 3
- 238000007664 blowing Methods 0.000 claims description 3
- 238000009833 condensation Methods 0.000 claims description 3
- 230000005494 condensation Effects 0.000 claims description 3
- 239000011521 glass Substances 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 3
- 230000004044 response Effects 0.000 claims description 3
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 claims description 3
- 229910052721 tungsten Inorganic materials 0.000 claims description 3
- 239000010937 tungsten Substances 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 2
- 239000004744 fabric Substances 0.000 claims 1
- 239000007788 liquid Substances 0.000 claims 1
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 abstract description 34
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical compound S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 abstract description 18
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 12
- 229910002091 carbon monoxide Inorganic materials 0.000 abstract description 12
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 9
- 229910052799 carbon Inorganic materials 0.000 abstract description 9
- 239000002245 particle Substances 0.000 abstract description 8
- 239000008188 pellet Substances 0.000 abstract description 7
- 238000000034 method Methods 0.000 abstract description 6
- 230000008569 process Effects 0.000 abstract description 5
- 239000000809 air pollutant Substances 0.000 abstract description 4
- 231100001243 air pollutant Toxicity 0.000 abstract description 4
- 239000000126 substance Substances 0.000 abstract description 4
- 239000007789 gas Substances 0.000 description 66
- 238000010586 diagram Methods 0.000 description 5
- 230000000505 pernicious effect Effects 0.000 description 5
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 4
- 239000005864 Sulphur Substances 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 230000008859 change Effects 0.000 description 4
- 238000007254 oxidation reaction Methods 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 230000037452 priming Effects 0.000 description 3
- 239000002912 waste gas Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 241000220317 Rosa Species 0.000 description 2
- 238000012271 agricultural production Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- TXKMVPPZCYKFAC-UHFFFAOYSA-N disulfur monoxide Inorganic materials O=S=S TXKMVPPZCYKFAC-UHFFFAOYSA-N 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000009776 industrial production Methods 0.000 description 2
- 239000013618 particulate matter Substances 0.000 description 2
- 238000009827 uniform distribution Methods 0.000 description 2
- JISVROCKRBFEIQ-UHFFFAOYSA-N [O].O=[C] Chemical compound [O].O=[C] JISVROCKRBFEIQ-UHFFFAOYSA-N 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 229960004424 carbon dioxide Drugs 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/005—Separation 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 heat treatment
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
- B01D47/02—Separating dispersed particles from gases, air or vapours by liquid as separating agent by passing the gas or air or vapour over or through a liquid bath
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
- B01D47/06—Spray cleaning
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/14—Separation 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
- B01D53/1456—Removing acid components
- B01D53/1475—Removing carbon dioxide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/14—Separation 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
- B01D53/1456—Removing acid components
- B01D53/1481—Removing sulfur dioxide or sulfur trioxide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/14—Separation 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
- B01D53/18—Absorbing units; Liquid distributors therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/75—Multi-step processes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
- F23G7/061—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/30—Sulfur compounds
- B01D2257/302—Sulfur oxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/50—Carbon oxides
- B01D2257/502—Carbon monoxide
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
- Y02A50/2351—Atmospheric particulate matter [PM], e.g. carbon smoke microparticles, smog, aerosol particles, dust
Abstract
The present invention discloses a kind of emission-control equipment, including exhaust gas entrance, gas pipeline, blower, thermal reaction chamber, water-soluble room and chimney, the gas pipeline left end connects exhaust gas entrance, then blower is connected, then thermal reaction chamber is connected, subsequently connect water-soluble room, finally connect chimney, carbon monoxide is disposed by setting heating room, the substances such as sulfur monoxide and some not sufficiently combusted carbon particles, sulfur dioxide and part pellet are disposed by water-soluble room again, blower is set simultaneously and accelerates exhaust-gas treatment process, the present invention consumes a small amount of electric energy and water resource can effectively deal with sulfur monoxide, sulfur dioxide, the air pollutants such as carbon monoxide and pellet.
Description
Technical field
The present invention relates to exhaust-gas treatment fields, and in particular to a kind of emission-control equipment.
Background technique
Environmental problem is increasingly serious, and air pollution situation is increasingly severe, and the requirement for environmental protection is also higher and higher, therefore
It just needs to administer the pernicious gas generated during industrial and agricultural production, but industrial or agricultural is related to national economy, according to
The modes such as factory are closed to reduce the discharge of pernicious gas and be tantamount to the useless food of choke, so needing to generate to during industrial and agricultural production
Pernicious gas first handled and discharged again, pernicious gas has very much, and most common is exactly sulfur monoxide, sulfur dioxide, an oxygen
Change carbon and pellet, therefore these pernicious gases should be handled emphatically.
Chinese Patent Application No.：201711408174.1 disclosing a kind of waste gas treatment equipment, this waste gas treatment equipment energy
It is enough to cool down to exhaust gas, improve adaptability；And it can sufficiently eliminate the impurity in exhaust gas, improve use reliability；
Including air inlet pipe, Rose Box, filter screen, disinfect box, pallet, ultraviolet lamp group and exhaust pipe, Rose Box is internally provided with work
Make chamber, disinfect box is internally provided with working chamber；Further include cabinet, partition, cooling box, blowoff basin, priming reservoir, the first water pump and
Second water pump, cooling box are internally provided with cyclic water channel and airflow line, and blowoff basin is mounted on the top of partition, priming reservoir peace
Mounted in the top of partition, blowoff basin is connected to priming reservoir；It further include reaction chamber, air-introduced machine, humidifier, mist guide tube, spray head, charging
It manages, plasma waste gas treating device, is difficult to effectively handle the pollution such as sulfur monoxide, sulfur dioxide, carbon monoxide in the program
Object.
Summary of the invention
The purpose of the present invention is to provide a kind of emission-control equipments, dispose carbon monoxide, one by setting heating room
The substances such as sulfur oxide and some not sufficiently combusted carbon particles, then sulfur dioxide and part are disposed by water-soluble room and may be inhaled
Particulate matter, while blower is set and accelerates exhaust-gas treatment process, the present invention consumes a small amount of electric energy and water resource can effectively deal with one
The air pollutants such as sulfur oxide, sulfur dioxide, carbon monoxide and pellet.
A kind of emission-control equipment, including exhaust gas entrance, gas pipeline, blower, thermal reaction chamber, water-soluble room and chimney, institute
Gas pipeline left end connection exhaust gas entrance is stated, blower is then connected, then connects thermal reaction chamber, subsequently connect water-soluble room,
Finally connect chimney, the lock that the exhaust gas entrance is equipped with valve and matches with outlet port, the flabellum of the blower
Part is located in gas pipeline, and blower blowing mouth is on right side；
The thermal reaction chamber includes air blower, heater and wire mesh, and the air blower is fixedly connected on gas pipeline
On outer wall, and be connected in the inflatable mouth of air blower and gas pipeline, the heater be fixedly connected on gas pipeline outer wall and
It is electrically connected with wire mesh, the wire mesh is set in gas pipeline, and the surrounding of wire mesh and gas pipeline inner wall
It is fixedly connected；
The water-soluble interior is set there are three water-soluble cabinet, and three water-soluble cabinets are connected in series, are equipped in the water-soluble cabinet
Multi-layer porous partition, and water-soluble cabinet lower end is equipped with water outlet, water outlet is connected to water tank, and water pump is equipped in water tank, and water pump connects
Have a water pipe, water pipe is equipped with tap, and the tap is equipped with three groups, and three groups of taps respectively with three water-soluble cabinet upper ends
It connects, the gas outlet of the water-soluble room is connected by gas pipeline with chimney.
Preferably, the indoor heater of the thermal response and wire mesh composition heating mechanism more than one set and mutually it
Between be equidistant, the heater be electric heater, the wire mesh be tungsten silk screen.
Preferably, through-hole is uniform-distribution on the porous barrier, porous barrier material is unorganic glass.
Preferably, the air inlet of the water-soluble cabinet is located at the upper left side of water-soluble cabinet, and the gas outlet of water-soluble cabinet is located at
The lower right of water-soluble cabinet, first water-soluble cabinet air inlet are connected to gas pipeline.
Preferably, it is equipped with liquidometer in the water tank, and the side wall above water tank is equipped with solenoid valve, the solenoid valve and outer
Boundary's water pipe is connected.
Preferably, condensation chamber is equipped in the chimney.
The advantage of the invention is that：Structure is simple, and it is convenient to operate, and disposes carbon monoxide, an oxygen by setting heating room
Change the substances such as sulphur and some not sufficiently combusted carbon particles, then sulfur dioxide and inhalable of part are disposed by water-soluble room
Grain object, while blower is set and accelerates exhaust-gas treatment process, the present invention consumes a small amount of electric energy and water resource can effectively deal with an oxygen
Change the air pollutants such as sulphur, sulfur dioxide, carbon monoxide and pellet.
Detailed description of the invention
Fig. 1 is the agent structure schematic diagram of apparatus of the present invention；
Fig. 2 is water-soluble box part structural schematic diagram in apparatus of the present invention；
Fig. 3 is the structural schematic diagram of porous barrier in apparatus of the present invention；
Fig. 4 is thermal reaction chamber partial structure diagram in apparatus of the present invention；
Fig. 5 is the structural schematic diagram of heater and wire mesh in apparatus of the present invention；
Wherein, 1, exhaust gas entrance, 2, gas pipeline, 3, blower, 4, thermal reaction chamber, 40, air blower, 41, heater, 42,
Wire mesh, 5, water-soluble room, 50, water-soluble cabinet, 51, water tank, 52, water pump, 53, water pipe, 54, tap, 55, porous barrier,
6, chimney.
Specific embodiment
To be easy to understand the technical means, the creative features, the aims and the efficiencies achieved by the present invention, below with reference to
Specific embodiment, the present invention is further explained.
As shown in Figures 1 to 5, a kind of emission-control equipment, including exhaust gas entrance 1, gas pipeline 2, blower 3, thermal response
Room 4, water-soluble room 5 and chimney 6,2 left end of gas pipeline connect exhaust gas entrance 1, then connect blower 3, then connection heat
Reaction chamber 4 subsequently connects water-soluble room 5, finally connects chimney 6, and the exhaust gas entrance 1 is equipped with valve and is discharged with exhaust gas
The lock that mouth matches, the flabellum part of the blower 3 is located in gas pipeline 2, and 3 blowing mouth of blower is on right side；
The thermal reaction chamber 4 includes air blower 40, heater 41 and wire mesh 42, and the air blower 40 is fixedly connected on
It on 2 outer wall of gas pipeline, and is connected in the inflatable mouth of air blower 40 and gas pipeline 2, the heater 41 is fixedly connected on defeated
It is electrically connected on 2 outer wall of feed channel and with wire mesh 42, the wire mesh 42 is set in gas pipeline 2, and wire mesh
42 surrounding is fixedly connected with 2 inner wall of gas pipeline；
It is set in the water-soluble room 5 there are three water-soluble cabinet 50, three water-soluble cabinets 50 are connected in series, the water-soluble cabinet 50
It is interior to be equipped with multi-layer porous partition 55, and 50 lower end of water-soluble cabinet is equipped with water outlet, water outlet is connected to water tank 51, sets in water tank 51
There is water pump 52, water pump 52 is connected to water pipe 53, and water pipe 53 is equipped with tap 54, and the tap 54 is equipped with three groups, and three groups of water
Faucet 54 is connected with three water-soluble 50 upper ends of cabinet respectively, and the gas outlet of the water-soluble room 5 passes through gas pipeline 2 and 6 phase of chimney
Even.
Heating mechanism more than one set that heater 41 in the thermal reaction chamber 4 and wire mesh 42 form and between each other
It is equidistant, the heater 41 is electric heater, and the wire mesh 42 is tungsten silk screen.
Through-hole is uniform-distribution on the porous barrier 55,55 material of porous barrier is unorganic glass.
The air inlet of the water-soluble cabinet 50 is located at the upper left side of water-soluble cabinet 50, and the gas outlet of water-soluble cabinet 50 is located at water
The lower right of molten cabinet 50, first water-soluble 50 air inlet of cabinet are connected to gas pipeline 2.
Liquidometer is equipped in the water tank 51, and the side wall of 51 top of water tank is equipped with solenoid valve, the solenoid valve and the external world
Water pipe is connected.
Condensation chamber is equipped in the chimney 6.
Specific embodiment and principle：
Embodiment one connects the exhaust gas entrance 1 of the present apparatus and outlet port, and exhaust gas enters defeated via exhaust gas entrance 1
In feed channel 2, exhaust gas first passes through blower 3 in gas pipeline 2, and blower 3 accelerates exhaust gas, exhaust gas is promoted to travel forward, then gives up
Gas enters thermal reaction chamber 4, further heats exhaust gas in thermal reaction chamber 4, is the oxidation wherein generated by incomplete combustion
Carbon and carbon particle full combustion become carbon dioxide, and sulfur monoxide full combustion is become sulfur dioxide, and subsequently exhaust gas enters
Sulfur dioxide in exhaust gas is dissolved in the water by water-soluble room 5 in water-soluble room 5, removes sulfur dioxide, while dissolving in some
The pellet of water, which is dissolved in the water, to be removed, and is finally removed sulfur monoxide, sulfur dioxide, carbon monoxide and be may be inhaled
The exhaust gas of particulate matter is discharged via chimney 6.
Embodiment two, exhaust gas are after entering thermal reaction chamber 4, and 4 front end of thermal reaction chamber is equipped with air blower 40, and air blower 40 will be outer
It is mixed in boundary's fresh air injection gas pipeline 2 with exhaust gas, subsequent mixed gas passes through the wire heated by heater 41
Net 42, the oxygen in carbon monoxide, sulfur monoxide and carbon particle and fresh air when by red-hot wire mesh 42, in exhaust gas
Oxidation reaction is come into full contact with and occurs, the heating mechanism more than one that the heater 41 and wire mesh 42 in thermal reaction chamber 4 form
Group, after the red-hot wire mesh 42 of multiple groups, carbon monoxide and carbon particle in exhaust gas become two with fully oxidized react of oxygen
Carbonoxide, the fully oxidized reaction of sulfur monoxide become sulfur dioxide.
Embodiment three, exhaust gas are after entering water-soluble room 5, and tap 54 is sprayed water from top to bottom, and water flows downwardly together with exhaust gas
It is dynamic, but due to being dispersed with the through-hole very to small-bore on porous barrier 5, porous barrier 55 contacted with water-soluble cabinet 50 closely, because
This water and exhaust gas can only enter next layer by the through-hole of these small-bores, so water and exhaust gas are by porous barrier from level to level
It is come into full contact with when 55, while continuing through three water-soluble cabinets 50 and sulfur dioxide is completely dissolved in water, removed with this
Remove the sulfur dioxide in exhaust gas；In the process, the water in water-soluble cabinet 50 can flow into water tank 51 via water outlet, while water
Pump 52 draws water from 51 bottom of water tank to be spilt down at the top of water-soluble cabinet 50 again, realizes the repeated recycling utilize of water, water is greatly saved
Resource.
Based on above-mentioned, the configuration of the present invention is simple, it is convenient to operate, and disposes carbon monoxide, an oxidation by setting heating room
The substances such as sulphur and some not sufficiently combusted carbon particles, then sulfur dioxide and part inhalable particles are disposed by water-soluble room
Object, while blower is set and accelerates exhaust-gas treatment process, the present invention consumes a small amount of electric energy and water resource can effectively deal with an oxidation
The air pollutants such as sulphur, sulfur dioxide, carbon monoxide and pellet.
As known by the technical knowledge, the present invention can pass through the embodiment party of other essence without departing from its spirit or essential feature
Case is realized.Therefore, embodiment disclosed above, in all respects are merely illustrative, not the only.Institute
Have within the scope of the present invention or is included in the invention in the change being equal in the scope of the present invention.
Claims (6)
1. a kind of emission-control equipment, which is characterized in that including exhaust gas entrance (1), gas pipeline (2), blower (3), thermal response
Room (4), water-soluble room (5) and chimney (6), gas pipeline (2) left end connect exhaust gas entrance (1), then connect blower
(3), thermal reaction chamber (4) then are connected, subsequently connects water-soluble room (5), finally connect chimney (6), on the exhaust gas entrance (1)
Equipped with valve and the lock to match with outlet port, the flabellum part of the blower (3) is located in gas pipeline (2), and
Blower (3) blowing mouth is on right side；
The thermal reaction chamber (4) includes air blower (40), heater (41) and wire mesh (42), and the air blower (40) is fixed
It is connected on gas pipeline (2) outer wall, and is connected in the inflatable mouth of air blower (40) and gas pipeline (2), the heater
(41) it is fixedly connected on gas pipeline (2) outer wall and is electrically connected with wire mesh (42), the wire mesh (42) is set to
In gas pipeline (2), and the surrounding of wire mesh (42) is fixedly connected with gas pipeline (2) inner wall；
It is set in the water-soluble room (5) there are three water-soluble cabinet (50), three water-soluble cabinets (50) are connected in series, the water-soluble cabinet
(50) multi-layer porous partition (55) being equipped in, and water-soluble cabinet (50) lower end is equipped with water outlet, water outlet is connected to water tank (51),
Water pump (52) are equipped in water tank (51), water pump (52) is connected to water pipe (53), and water pipe (53) is equipped with tap (54), the fire hose
Head (54) is equipped with three groups, and three groups of taps (54) are connected with three water-soluble cabinet (50) upper ends respectively, the water-soluble room (5)
Gas outlet is connected by gas pipeline (2) with chimney (6).
2. a kind of emission-control equipment according to claim 1, it is characterised in that：Heating in the thermal reaction chamber (4)
Device (41) and wire mesh (42) composition heating mechanism more than one set and be equidistant between each other, the heater (41) is
Electric heater, the wire mesh (42) are tungsten silk screen.
3. a kind of emission-control equipment according to claim 1, it is characterised in that：Uniformly divide on the porous barrier (55)
Cloth through-hole, porous barrier (55) material be unorganic glass.
4. a kind of emission-control equipment according to claim 1, it is characterised in that：The air inlet of the water-soluble cabinet (50)
Positioned at the upper left side of water-soluble cabinet (50), the gas outlet of water-soluble cabinet (50) is located at the lower right of water-soluble cabinet (50), and first
Water-soluble cabinet (50) air inlet is connected to gas pipeline (2).
5. a kind of emission-control equipment according to claim 1, it is characterised in that：Liquid level is equipped in the water tank (51)
Meter, and the side wall above water tank (51) is equipped with solenoid valve, which is connected with external water pipe.
6. a kind of emission-control equipment according to claim 1, it is characterised in that：Condensation chamber is equipped in the chimney (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810801514.5A CN108889082A (en) | 2018-07-20 | 2018-07-20 | A kind of emission-control equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810801514.5A CN108889082A (en) | 2018-07-20 | 2018-07-20 | A kind of emission-control equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108889082A true CN108889082A (en) | 2018-11-27 |
Family
ID=64351410
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810801514.5A Pending CN108889082A (en) | 2018-07-20 | 2018-07-20 | A kind of emission-control equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108889082A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110887052A (en) * | 2019-12-06 | 2020-03-17 | 江苏秉盛环保工程有限公司 | Series progressive waste gas and wastewater treatment system |
| CN111994910A (en) * | 2020-08-21 | 2020-11-27 | 郑州嵩山硼业科技有限公司 | Nanometer boron carbide powder production system for manufacturing shrapnel prevention piece |
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| CN201735315U (en) * | 2010-04-02 | 2011-02-09 | 张连山 | Reaction chamber for removing indium and sulfur of end gas in process of smelting nonferrous metal with carbon, hydrogen and oxide mixture |
| CN202606016U (en) * | 2012-05-18 | 2012-12-19 | 紫金矿业集团股份有限公司 | Purification and desulphurization device |
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| CN111994910A (en) * | 2020-08-21 | 2020-11-27 | 郑州嵩山硼业科技有限公司 | Nanometer boron carbide powder production system for manufacturing shrapnel prevention piece |
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Application publication date: 20181127 |