CN109420392A - A kind of controlling device of atmosphere pollution - Google Patents
A kind of controlling device of atmosphere pollution Download PDFInfo
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- CN109420392A CN109420392A CN201710718500.2A CN201710718500A CN109420392A CN 109420392 A CN109420392 A CN 109420392A CN 201710718500 A CN201710718500 A CN 201710718500A CN 109420392 A CN109420392 A CN 109420392A
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- 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
- B01D47/021—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 by bubbling the gas through a liquid bath
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/60—Combinations of devices covered by groups B01D46/00 and B01D47/00
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- 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
- B01D53/007—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 irradiation
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- 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
- B01D53/26—Drying gases or vapours
- B01D53/261—Drying gases or vapours by adsorption
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- 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
- B01D53/76—Gas phase processes, e.g. by using aerosols
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- 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
- B01D53/86—Catalytic processes
- B01D53/8678—Removing components of undefined structure
- B01D53/8687—Organic components
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- 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
- B01D53/86—Catalytic processes
- B01D53/88—Handling or mounting catalysts
- B01D53/885—Devices in general for catalytic purification of waste gases
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/10—Oxidants
- B01D2251/104—Ozone
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/102—Carbon
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/80—Type of catalytic reaction
- B01D2255/802—Photocatalytic
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/80—Employing electric, magnetic, electromagnetic or wave energy, or particle radiation
- B01D2259/804—UV light
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Abstract
The invention discloses a kind of controlling devices of atmosphere pollution, including pedestal, the upper surface of the pedestal is fixedly connected with water tank, the upper surface of the water tank is plugged with the first appendix and the second appendix, the upper surface of the pedestal is fixedly connected with aerostatic press, the output end of the aerostatic press is connected to one end of the first appendix, and the side on the water tank surface is fixedly connected with water inlet pipe, and the other side on the water tank surface is fixedly connected with outlet pipe.The discharge gas of host computer is pressed into water tank by the present invention by aerostatic press via the first appendix, since the bottom end of the first appendix is located under liquid level, so that gas is after the exit because gravity floats, so that some particles contained in flue gas are in water because self weight sinks or by Water Molecular Adsorption, to which the granule foreign in flue gas be filtered, flue gas is discharged out of second appendix after being detached from water body, to achieve the effect that the preliminary purification in water tank.
Description
Technical field
The present invention relates to environmental protection technical field, specially a kind of controlling device of atmosphere pollution.
Background technique
Glance coal is the aerosol and steam that pitch heating and the burning of bituminous substance generate, the volatile matter in glance coal
It is discharged into atmosphere, becomes as one of atmosphere pollution.Glance coal component is extremely complex, different and different with asphalt source.Pitch
The solid and liquid particle that existing pitch volatile component condenses into flue gas, and have the organic matter of steam condition, Asphalt Smoke Emission
Source is very wide, and 1. coking of producing cause and oil refining etc. generate the industrial hot procedure of pitch；2. heated asphalt is to produce Asphalt Production
The process of product；3. heated asphalt is to laying road, repairing house or the process for making anticorrosive paint；4. heating or burning contain drip
The process of green pitch articles, petroleum, bituminous coal, timber and oil shale.Bitumen flue gas is generally mingled with certain density flue dust,
In sepia or black, there is strong impulse effect.It is reported that being to skin and breathing containing compounds more than 6 carbon atoms
System has carcinogenesis.It is confirmed through research and zoopery, 3-4 benzos being extract from coal tar, pitch and organic solvent
Pyrene is strong carcinogen.Long term investigation obtains, often in contact with the worker of coal tar, pitch and oil shale, cutaneum carcinoma, carcinoma of scrotum,
Laryngocarcinoma and lung cancer morbidity rate are all quite high.
The processing method of country's glance coal mainly has incineration method, cooling method, oily absorption method, water spray washing+activity at present
Charcoal method and water spray washing+electric fishing oil process etc., it is most to add rear class processing unit using water spray washing, using above-mentioned side
The treatment effect that method carries out glance coal is unsatisfactory, since water sprinkler system will use a large amount of water resource, not only wastes water
Resource and water pollution is caused, and the purification efficiency of glance coal is lower in subsequent processing, so combine can not be efficient for the two
Purifying pitch cigarette, discharge can cause serious pollution to atmosphere.
Summary of the invention
(1) the technical issues of solving
In view of the deficiencies of the prior art, the present invention provides a kind of controlling devices of atmosphere pollution, solve current pitch
The lower problem of the processing unit efficiency of cigarette.
(2) technical solution
To achieve the above object, the invention provides the following technical scheme: a kind of controlling device of atmosphere pollution, including bottom
Seat, the upper surface of the pedestal are fixedly connected with water tank, and the upper surface of the water tank is plugged with the first appendix and the second gas transmission
Pipe, the upper surface of the pedestal are fixedly connected with aerostatic press, and the output end of the aerostatic press is connected to one end of the first appendix,
The side on the water tank surface is fixedly connected with water inlet pipe, and the other side on the water tank surface is fixedly connected with outlet pipe, described
Heat exchanger is fixedly connected between water inlet pipe and outlet pipe, the heat exchanger is located in water tank, and the upper surface of the pedestal is fixed
It is connected with water pump, the output end of the water pump is connected with one end of water inlet pipe, and the upper surface of the water tank is fixedly connected with note
Water pipe, the lower surface of the water tank are fixedly connected with drainpipe, and one end of second appendix is fixedly connected with moisture absorption case, institute
That states moisture absorption case is internally provided with S-shaped bend, and one end of second appendix is connected with one end of S-shaped bend, the S-shaped
Activated carbon adsorption filling is fixedly connected in bend, the other end of the S-shaped pipeline is fixedly connected with light direct oxidation photocatalysis
Oxidation unit.
The heat exchanger includes connector, and the quantity of the connector is two, two connectors respectively with water inlet pipe and outlet pipe
It is connected, is fixedly connected between two connectors by copper pipe, the quantity of the copper pipe is 6-10, and the copper pipe is equidistant row
Column, the surface of the copper pipe are fixedly connected with by backing, and the diameter of the copper pipe is 1-1.5 centimetres, and the pipe thickness of copper pipe
No more than 2 millimeters, the width by backing is 0.5-1 centimetres, and described by backing every three is one group, and three of every group by
The surface of copper pipe is arranged in backing in the form of annular array.
The smooth direct oxidation photocatalytic oxidation device includes cabinet, and the cabinet is internally provided with filter, ultraviolet
Lamp and photocatalytic plate, the two sides of the cabinet have been respectively fixedly connected with air inlet and air outlet, and the filter is located at cabinet
The side of interior close air inlet, the ultraviolet lamp are equidistantly positioned in cabinet with 5 centimetres for spacing on the right side of filter
Wall, the photocatalytic plate are equidistantly positioned in cabinet close to the side of gas outlet with 5 centimetres for spacing.
Preferably, the pedestal includes supporting plane, and the lower surface of the supporting plane is fixedly connected with support leg, described
The quantity of support leg is four, and the lower surface of pedestal is arranged in four support legs in the form of rectangular array, and the support is flat
The upper surface in face is fixedly connected with support feet, and the quantity of the support feet is four, and four support feets are with rectangular array
Form the upper surface of supporting plane is set, the lower surface of the support feet and water tank is welded.
Preferably, tap water is filled in the water tank, the bottom end of first appendix is located at tap water in water tank
Under liquid level, the bottom end of second appendix is located in water tank on the liquid level of tap water.
Preferably, the input terminal of the aerostatic press is connected with the exhaust end of host computer.
Preferably, shut-off valve is fixedly connected on the water injection pipe and drainpipe.
Preferably, the external tap water water source of the input terminal of the water pump.
Preferably, the region that ultraviolet lamp and photocatalytic plate are arranged jointly in the cabinet is photocatalytic region, in the cabinet
Only the region of ultraviolet lamp is photooxidation area, and the photooxidation area is between filter and photocatalytic region, the photocatalytic region
It is equal with the range in photooxidation area.
Preferably, the bending angle of the S-shaped bend is at least 5.
(3) beneficial effect
The present invention provides a kind of controlling devices of atmosphere pollution.Have it is following the utility model has the advantages that
(1), the present invention, will be upper by aerostatic press by setting water tank, the first appendix, the second appendix and aerostatic press
The discharge gas of machine is pressed into water tank via the first appendix, since the bottom end of the first appendix is located under liquid level, to make
Gas is obtained after the exit because gravity floats, so that some particles contained in flue gas are in water because of self weight sinking
Or by Water Molecular Adsorption, so that the granule foreign in flue gas be filtered, flue gas is arranged out of second appendix after being detached from water body
Out, to achieve the effect that the preliminary purification in water tank.
(2), the present invention by setting water inlet pipe, outlet pipe, heat exchanger, connector, copper pipe, by backing and water pump, pass through water
Pumping is moved water source and is flowed into from water inlet pipe, flows out of the water outlet pipe after routed through heat exchanger, due to containing amount of heat in flue gas, to make
Separation activity is higher in flue gas, flue gas can transfer heat in water body after being pressed into water tank, by heat exchanger by water
The heat derives of water body in case avoid water body in water tank and boil, while also having achieved the purpose that waste heat recycles, and avoid heat
It distributes discharge in air and causes greenhouse effects.
(3), the present invention is by setting moisture absorption case, S-shaped bend and activated carbon adsorption filling, since flue gas is after flowing through water tank
There is the contact of certain time with water body, so that many hydrones can be contained in flue gas, so that the humidity of flue gas is larger, leads to
It crosses setting activated carbon adsorption and fills and the moisture in flue gas is absorbed, and by setting S-shaped bend, reaching reduction volume
Effect simultaneously, increase the length of aqueous vapor adsorption section, improve the effect of moisture sorption.
(4), the present invention is by setting water injection pipe, drainpipe and shut-off valve, since the water in water tank can ceaselessly absorb cigarette
Dust and particle in gas, so that water pollution, so that the absorbability of water body reaches full after certain duration that works
With to need replacing water source, drainpipe draining is opened by shut-off valve, drainpipe is then shut off and opens water injection pipe again and infused
Water, to achieve the effect that the water body being conveniently replaceable in water tank.
(5), the present invention passes through setting light direct oxidation photocatalytic oxidation device, cabinet, filter, ultraviolet lamp, photocatalysis
Plate, air inlet, gas outlet, photocatalytic region and photooxidation area filter out the dust in flue gas by filter, utilize photooxidation later
Changing the elemental oxygen that area's ultraviolet light and ozone generate has very strong absorbability for the electronics that photocatalyst surface generates, thus
The recombination rate of electrons and holes is greatly reduced, to improve light-catalysed efficiency, and then processing is greatly improved and has
The ability of machine pollutant.
Detailed description of the invention
Fig. 1 is the schematic diagram of the section structure of front view of the present invention；
Fig. 2 is the schematic diagram of the section structure of present invention heat exchanger top view.
In figure: 1 pedestal, 101 supporting planes, 102 support legs, 103 support feets, 2 water tanks, 3 first appendixs, 4 second
Appendix, 5 aerostatic presses, 6 water inlet pipes, 7 outlet pipes, 8 heat exchangers, 801 connectors, 802 copper pipes, 803 are by backing, 9 water pumps, 10 water fillings
Pipe, 11 drainpipes, 12 moisture absorption casees, 13S shape bend, 14 activated carbon adsorptions filling, 15 smooth direct oxidation photocatalytic oxidation devices,
151 cabinets, 152 filters, 153 ultraviolet lamps, 154 photocatalytic plates, 155 air inlets, 156 gas outlets, 157 photocatalytic regions, 158 light
Zoneofoxidation, 16 shut-off valves.
Specific embodiment
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation description, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
As shown in Figs. 1-2, the present invention provides a kind of technical solution: a kind of controlling device of atmosphere pollution, including pedestal
(1), pedestal (1) includes supporting plane (101), and the lower surface of supporting plane (101) is fixedly connected with support leg (102), support
The quantity of foot (102) is four, and four support legs (102) are arranged in the lower surface of pedestal (1), branch in the form of rectangular array
The upper surface of support plane (101) is fixedly connected with support feet (103), and the quantity of support feet (103) is four, four supports
Feet (103) is arranged in the upper surface of supporting plane (101) in the form of rectangular array, supports feet (103) and water tank (2)
Lower surface welding, the upper surface of pedestal (1) are fixedly connected with water tank (2), and the upper surface of water tank (2) is plugged with the first appendix
(3) and the second appendix (4) tap water, is filled in water tank (2), it is interior originally that the bottom end of the first appendix (3) is located at water tank (2)
Under the liquid level of water, the bottom end of the second appendix (4) is located on the liquid level of water tank (2) interior tap water, the upper surface of pedestal (1)
It is fixedly connected with aerostatic press (5), the input terminal of aerostatic press (5) is connected with the exhaust end of host computer, the output end of aerostatic press (5)
It is connected to one end of the first appendix (3), the side on water tank (2) surface is fixedly connected with water inlet pipe (6), water tank (2) surface
The other side is fixedly connected with outlet pipe (7), and heat exchanger (8), heat exchanger are fixedly connected between water inlet pipe (6) and outlet pipe (7)
(8) it is located in water tank (2), the upper surface of pedestal (1) is fixedly connected with water pump (9), the output end of water pump (9) and water inlet pipe (6)
One end be connected, the external tap water water source of the input terminal of water pump (9), the upper surface of water tank (2) is fixedly connected with water injection pipe
(10), the lower surface of water tank (2) is fixedly connected with drainpipe (11), is fixedly connected on water injection pipe (10) and drainpipe (11)
Shut-off valve (16), one end of the second appendix (4) are fixedly connected with moisture absorption case (12), and moisture absorption case (12) is internally provided with S-shaped
Bend (13), the bending angle of S-shaped bend (13) are at least 5, one end of one end and S-shaped bend (13) of the second appendix (4)
It is connected, activated carbon adsorption filling (14) is fixedly connected in S-shaped bend (13), the other end of S-shaped pipeline (13) is fixedly connected
There is light direct oxidation photocatalytic oxidation device (15).
Heat exchanger (8) includes connector (801), and the quantity of connector (801) is two, two connectors (801) respectively with water inlet
Pipe (6) is connected with outlet pipe (7), is fixedly connected between two connectors (801) by copper pipe (802), the quantity of copper pipe (802)
It is 6-10, copper pipe (802) is equidistant arrangement, and the surface of copper pipe (802) is fixedly connected with by backing (803), copper pipe (802)
Diameter be 1-1.5 centimetres, and the pipe thickness of copper pipe (802) be no more than 2 millimeters, by backing (803) width be 0.5-1 lis
Rice is one group by backing (803) every three, and three of every group are arranged in the form of annular array in copper pipe by backing (803)
(802) surface.
Light direct oxidation photocatalytic oxidation device (15) includes cabinet (151), and cabinet (151) is internally provided with filter
(152), ultraviolet lamp (153) and photocatalytic plate (154), the two sides of cabinet (151) be respectively fixedly connected with air inlet (155) and
Gas outlet (156), filter (152) are located at the side in cabinet (151) close to air inlet (155), and ultraviolet lamp (153) is filtering
The right side of device (152) is equidistantly positioned the inner wall in cabinet (151) with 5 centimetres for spacing, and photocatalytic plate (154) is in cabinet
(151) be equidistantly positioned in close to the side of gas outlet (156) with 5 centimetres for spacing, cabinet (151) interior ultraviolet lamp (153) and
The region that photocatalytic plate (154) is arranged jointly is photocatalytic region (157), and (151) only have the region of ultraviolet lamp (153) to be in cabinet
Photooxidation area (158), photooxidation area (158) are located between filter (152) and photocatalytic region (157), photocatalytic region (157) with
The range in photooxidation area (158) is equal.
In use, aerostatic press (5) by flue gas from the first appendix (3) indentation water tank (2) in, flue gas by water purification from
Second appendix (4) outflow, water pump (9) are twitched water body and are injected from water inlet pipe (6), and water body flows through in heat exchanger (8) and water tank (2)
Water body heat exchange, heat increases after water body is flowed out from outlet pipe (7), to recycle thermal energy, flue gas is discharged from the second appendix (4)
Enter in moisture absorption case (12) afterwards, after the activated carbon adsorption filling (14) in S-shaped bend (13) is by the Vapor adsorption in flue gas,
Flue gas is passed through in light direct oxidation photocatalytic oxidation device (15) and is purified, and discharges after the completion of purification from gas outlet (156).
It can to sum up obtain, (1), the present invention pass through setting water tank (2), the first appendix (3), the second appendix (4) and air pressure
Machine (5), it is by aerostatic press (5) that the discharge gas of host computer is interior via the first appendix (3) indentation water tank (2), due to first
The bottom end of appendix (3) is located under liquid level, so that gas is after the exit because gravity floats, so that flue gas
In some particles for containing in water because self weight sinks or by Water Molecular Adsorption, thus by the granule foreign mistake in flue gas
Filter, flue gas discharge out of the second appendix (4) after being detached from water body, to achieve the effect that in water tank (2) interior preliminary purification.
(2), the present invention by setting water inlet pipe (6), outlet pipe (7), heat exchanger (8), connector (801), copper pipe (802),
By backing (803) and water pump (9), water source is twitched by water pump (9) and is flowed into from water inlet pipe (6), from water outlet after routed through heat exchanger (8)
(7) outflow is managed, due to containing amount of heat in flue gas, activity is higher, and flue gas is being pressed into water so that separating in flue gas
Case can transfer heat in water body after (2), by heat exchanger (8) by the heat derives of water tank (2) interior water body, avoid water tank
(2) interior water body boiling, while also having achieved the purpose that waste heat recycles avoids heat and distributes discharge in air and greenhouse is caused to imitate
It answers.
(3), the present invention is by setting moisture absorption case (12), S-shaped bend (13) and activated carbon adsorption filling (14), due to flue gas
There is the contact of certain time with water body flowing through water tank (2) afterwards, so that many hydrones can be contained in flue gas, so that cigarette
The humidity of gas is larger, fills (14) by setting activated carbon adsorption and absorbs to the moisture in flue gas, and passes through setting S-shaped
Bend (13) is achieving the effect that reduce volume simultaneously, is increasing the length of aqueous vapor adsorption section, improve the effect of moisture sorption
Fruit.
(4), the present invention is by setting water injection pipe (10), drainpipe (11) and shut-off valve (16), due to the water in water tank (2)
The dust and particle in flue gas can be ceaselessly absorbed, so that water pollution, thus after certain duration that works, water body
Absorbability reaches saturation, to need replacing water source, opens drainpipe (11) draining, the row of being then shut off by shut-off valve (16)
Water pipe (11) is opened water injection pipe (10) again and is filled the water, to achieve the effect that the water body being conveniently replaceable in water tank (2).
(5), the present invention by setting light direct oxidation photocatalytic oxidation device (15), cabinet (151), filter (152),
Ultraviolet lamp (153), photocatalytic plate (154), air inlet (155), gas outlet (156), photocatalytic region (157) and photooxidation area
(158), the dust in flue gas is filtered out by filter (152), the original generated later using photooxidation area ultraviolet light and ozone
Sub- oxygen has very strong absorbability for the electronics that photocatalyst surface generates, to greatly reduce electrons and holes
Recombination rate to improve light-catalysed efficiency, and then greatly improves the ability of processing organic pollutant.
It should be noted that, in this document, relational terms such as first and second and the like are used merely to a reality
Body or operation are distinguished with another entity or operation, are deposited without necessarily requiring or implying between these entities or operation
In any actual relationship or order or sequence.Moreover, the terms "include", "comprise" or its any other variant are intended to
Non-exclusive inclusion, so that the process, method, article or equipment including a series of elements is not only wanted including those
Element, but also including other elements that are not explicitly listed, or further include for this process, method, article or equipment
Intrinsic element.In the absence of more restrictions, the element limited by sentence " including a reference structure ", is not arranged
Except there is also other identical elements in the process, method, article or apparatus that includes the element.
It although an embodiment of the present invention has been shown and described, for the ordinary skill in the art, can be with
A variety of variations, modification, replacement can be carried out to these embodiments without departing from the principles and spirit of the present invention by understanding
And modification, the scope of the present invention is defined by the appended.
Claims (8)
1. a kind of controlling device of atmosphere pollution, including pedestal (1), it is characterised in that: the upper surface of the pedestal (1) is fixed to be connected
It is connected to water tank (2), the upper surface of the water tank (2) is plugged with the first appendix (3) and the second appendix (4), the pedestal (1)
Upper surface be fixedly connected with aerostatic press (5), the output end of the aerostatic press (5) is connected to one end of the first appendix (3), institute
The side for stating water tank (2) surface is fixedly connected with water inlet pipe (6), and the other side on water tank (2) surface is fixedly connected with water outlet
It manages (7), is fixedly connected with heat exchanger (8) between the water inlet pipe (6) and outlet pipe (7), the heat exchanger (8) is located at water tank
(2) in, the upper surface of the pedestal (1) is fixedly connected with water pump (9), and the one of the output end of the water pump (9) and water inlet pipe (6)
End is connected, and the upper surface of the water tank (2) is fixedly connected with water injection pipe (10), and the lower surface of the water tank (2) is fixedly connected
Have drainpipe (11), one end of second appendix (4) is fixedly connected with moisture absorption case (12), the inside of the moisture absorption case (12)
It is provided with S-shaped bend (13), one end of second appendix (4) is connected with one end of S-shaped bend (13), and the S-shaped is curved
Activated carbon adsorption filling (14) is fixedly connected in road (13), it is direct that the other end of the S-shaped pipeline (13) is fixedly connected with light
It aoxidizes photocatalytic oxidation device (15)；
The heat exchanger (8) includes connector (801), and the quantity of the connector (801) is two, two connectors (801) respectively with
Water inlet pipe (6) is connected with outlet pipe (7), is fixedly connected between two connectors (801) by copper pipe (802), the copper pipe
(802) quantity is 6-10, and the copper pipe (802) is equidistant arrangement, the surface of the copper pipe (802) be fixedly connected with by
Backing (803), the diameter of the copper pipe (802) is 1-1.5 centimetres, and the pipe thickness of copper pipe (802) is no more than 2 millimeters, institute
Stating by the width of backing (803) is 0.5-1 centimetres, and described by backing (803) every three is one group, and three of every group are by backing
(803) it is arranged in the form of annular array on the surface of copper pipe (802)；
The smooth direct oxidation photocatalytic oxidation device (15) includes cabinet (151), and cabinet (151) were internally provided with
The two sides of filter (152), ultraviolet lamp (153) and photocatalytic plate (154), the cabinet (151) have been respectively fixedly connected with air inlet
Mouth (155) and gas outlet (156), the filter (152) is located at the side in cabinet (151) close to air inlet (155), described
Ultraviolet lamp (153) is equidistantly positioned the inner wall in cabinet (151), the light with 5 centimetres on the right side of filter (152) for spacing
Catalytic plate (154) is equidistantly positioned in cabinet (151) close to the side of gas outlet (156) with 5 centimetres for spacing.
2. a kind of controlling device of atmosphere pollution according to claim 1, it is characterised in that: the pedestal (1) includes branch
It supports plane (101), the lower surface of the supporting plane (101) is fixedly connected with support leg (102), the support leg (102)
Quantity is four, and four support legs (102) are arranged in the lower surface of pedestal (1) in the form of rectangular array, and the support is flat
The upper surface in face (101) is fixedly connected with support feet (103), and the quantity of support feet (103) is four, four supports
Feet (103) is arranged in the upper surface of supporting plane (101), the support feet (103) and water tank in the form of rectangular array
(2) lower surface welding.
3. a kind of controlling device of atmosphere pollution according to claim 1, it is characterised in that: filling in the water tank (2)
There is tap water, the bottom end of first appendix (3) is located under the liquid level of water tank (2) interior tap water, second appendix
(4) bottom end is located on the liquid level of water tank (2) interior tap water.
4. a kind of controlling device of atmosphere pollution according to claim 1, it is characterised in that: the aerostatic press (5) it is defeated
Enter end to be connected with the exhaust end of host computer.
5. a kind of controlling device of atmosphere pollution according to claim 1, it is characterised in that: the water injection pipe (10) and row
Shut-off valve (16) are fixedly connected on water pipe (11).
6. a kind of controlling device of atmosphere pollution according to claim 1, it is characterised in that: the input of the water pump (9)
Hold external tap water water source.
7. a kind of controlling device of atmosphere pollution according to claim 1, it is characterised in that: purple in the cabinet (151)
The region that outer lamp (153) and photocatalytic plate (154) are arranged jointly is photocatalytic region (157), and (151) are only ultraviolet in the cabinet
The region of lamp (153) is photooxidation area (158), and the photooxidation area (158) is located at filter (152) and photocatalytic region (157)
Between, the photocatalytic region (157) is equal with the range of photooxidation area (158).
8. a kind of controlling device of atmosphere pollution according to claim 1, it is characterised in that: the S-shaped bend (13)
Bending angle is at least 5.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710718500.2A CN109420392A (en) | 2017-08-21 | 2017-08-21 | A kind of controlling device of atmosphere pollution |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710718500.2A CN109420392A (en) | 2017-08-21 | 2017-08-21 | A kind of controlling device of atmosphere pollution |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109420392A true CN109420392A (en) | 2019-03-05 |
Family
ID=65497932
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710718500.2A Pending CN109420392A (en) | 2017-08-21 | 2017-08-21 | A kind of controlling device of atmosphere pollution |
Country Status (1)
| Country | Link |
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| CN (1) | CN109420392A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN111111362A (en) * | 2019-12-28 | 2020-05-08 | 江苏新中金环保科技股份有限公司 | Flue gas desulfurization and denitrification complete equipment based on efficient catalysis technology |
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