Escaping gas processing cycle uses system and method
Technical field
The present invention relates to escaping gas process field, be specifically related to a kind of escaping gas processing cycle and use system
And method.
Background technology
The escaping gas that industry and life activity produce is one of source polluting environment.Some is known, some
Being unknown, PM2.5 fine dust refers to that aerodynamic diameter is less than the particulate pollutant of 2.5 μm, and it is to cause respiratory tract
The key factor of pathophoresis, these particulate matter long-term suspension do not settle in air, and are easily carried antibacterial and virus, its
80% granule can enter in the alveolar of human body, is the one of the main reasons causing pulmonary disease.
Such as, the harmful substance such as escaping gas that the metal of field of industrial production, plastic moulding process produce, test number
According to showing, the escaping gas and the PM2.5 that produce when plastic shaping and secondary operations are 1%;Make a general survey of whole nation plastic material and consume total
Amount, it is known that therefore China to produce millions of tons escaping gas and PM2.5 every year.In sphere of life, huge numbers of families and restaurant
Culinary art test data shows when oil temperature rises to 155 DEG C-190 DEG C, and the escaping gas of generation and PM2.5 are 1.5%, on the tip of the tongue
China, that makes a general survey of whole nation processing produces tens million of tons of escaping gases and PM2.5 in edible oil total amount consumed year.
Spraying work post is indispensable link in industrial sector chain, and spray painting room can provide painting operation private environment
Closing space, the artificial environment manufactured in coating room, paint application completes by air pressure air-flow, can meet painting operation to environment
Temperature, humidity, illumination, the demand of cleanliness factor etc.;Reach required relative comfort during operation, the working environment of safety.Test
Data show, when construction, have the paint of 1/3 to distribute;Containing harmful volatilizations such as benzene,toluene,xylenes in paint
The property particulate pollutant such as gas and PM2.5.But the actual state that these escaping gases are administered is the project that the most only rests on
Engineering environmental impact assessment and acceptance phase, enterprise usually takes these escaping gases in line.Sticky particle thing in escaping gas without
Method efflorescence, making the activated carbon adsorption that commonly uses process, the material of escaping gas is the most bonding cannot work continuously, causes two
Secondary pollution, treatment cost is high, does not has effective administering method, administers supervision and is easily in uncontrolled state, escaping gas
The most treated just it is directly entered air so that it is become one of reason of forming haze.
Coating room needs to be equipped with paint mist treatment device, can either make to process the coating cloud of the generation of painting operation, protection spray
Coat exempts from secondary pollution, in order to the coating particle that swims produced when making spray-coating can scene from spraying be taken away in time, with
Ensure coating quality, and make its escaping gas processed through paint mist treatment device need to meet discharging standards, with
Prevent from polluting environment.
At present, in escaping gas governance standard, the relevant improvement of PM2.5 is in space state, escaping gas and
PM2.5 produces source improvement to be needed to realize by technology and equipment running, the poisonous and harmful produced during how solving productive life
Gas, is enterprise and a difficult problem of society's facing.Need a kind of escaping gas at present badly and produce the volatility gas in region
Body and PM2.5 processing cycle use system and method to solve current environmental problem.
Summary of the invention
The escaping gas processing cycle that after it is an object of the invention to provide a kind of process, gas can recycle uses
System and method.
For realizing above-mentioned technical purpose, the technical scheme that the present invention provides is: a kind of escaping gas processing cycle uses
System, it is characterised in that: described escaping gas processing cycle uses system to include escaping gas processing means and blower fan;Institute
State escaping gas processing means to be connected with blower fan by pipeline;
Described escaping gas processing cycle uses system also to include, and the escaping gas closed produces region;
Described escaping gas produces region and is provided with air inlet and gas outlet, and described escaping gas processing means sets
It is equipped with air inlet and gas outlet, described blower fan is provided with air inlet and gas outlet;
Described escaping gas produces the gas outlet in region and is connected with the air inlet of described escaping gas processing means;
The gas outlet of described escaping gas processing means is connected with the air inlet of blower fan by pipeline, the gas outlet of described blower fan with
The escaping gas closed produces the air inlet in region and is connected.
Further, described escaping gas processing cycle uses system also to include being arranged at escaping gas processing means
And the gas double purification device between blower fan and drying tower;
Be provided with air inlet and gas outlet on described gas double purification device, described drying tower is provided with air inlet and
Gas outlet;It is provided with particle filtering net at the air inlet of described escaping gas processing means;
The gas outlet of described escaping gas processing means is connected with the air inlet of gas double purification device, described gas
The gas outlet of body double purification device is connected with the air inlet of drying tower;Granule mistake it is provided with at the air inlet of described drying tower
Filter screen, the gas outlet of described drying tower is connected with the air inlet of blower fan.
A kind of escaping gas processing cycle of the present invention uses system, it is characterised in that: described escaping gas processes
Recycling system includes oil-water separation water curtain tower, escaping gas processing means and blower fan;
Described escaping gas processing cycle uses system also to include the food cooking area closed;Described oil-water separation water
It is provided with air inlet and gas outlet on curtain tower, described escaping gas processing means is provided with air inlet and gas outlet, institute
State and on blower fan, be provided with air inlet and gas outlet;
Described food cooking area is provided with air inlet and gas outlet, and described food cooking area is provided with gas outlet and institute
The air inlet stating oil-water separation water curtain tower apparatus is connected, and pipeline is passed through in the gas outlet of described oil-water separation water curtain tower apparatus
Being connected with the air inlet of escaping gas processing means, pipeline and wind are passed through in the gas outlet of described escaping gas processing means
The air inlet of machine is connected, and the gas outlet of described blower fan is connected with the air inlet of food cooking area.
Further, described escaping gas processing cycle uses system also to include being arranged at escaping gas processing means
And the drying tower between blower fan;It is provided with particle filtering net at the air inlet of described escaping gas processing means;
Air inlet and gas outlet it is provided with on described drying tower;The gas outlet of described escaping gas processing means is by pipe
Road is connected with the air inlet of drying tower;
Particle filtering net, the gas outlet of described drying tower and the air inlet of blower fan it is provided with at the air inlet of described drying tower
It is connected.
A kind of escaping gas processing cycle of the present invention uses system, it is characterised in that: described escaping gas processes
Recycling system includes escaping gas processing means and blower fan;
Described escaping gas processing cycle uses system also to include, and metallo-plastic finished product produces region;Described metallo-plastic
Finished product produces and is provided with air inlet and gas outlet on region;It is provided with air inlet in described escaping gas processing means and gives vent to anger
Mouthful, described blower fan is provided with air inlet and gas outlet;
Described metallo-plastic finished product produces the gas outlet air inlet by pipeline with escaping gas processing means in region
Being connected, the gas outlet of described escaping gas processing means is connected with the air inlet of blower fan by pipeline, described blower fan
The air inlet that gas outlet produces region with metallo-plastic finished product is connected.
Further, described metallo-plastic finished product is provided with metallo-plastic finished product production machine and is arranged in producing region
Metallo-plastic finished product produces the air-suction cover on machine,
Being provided with gas outlet on described air-suction cover, metallo-plastic finished product is produced the volatility that machine produces by described air-suction cover
In gas inhalation mask, described gas double purification device is provided with air inlet and gas outlet, described drying tower is provided with into
QI KOU and gas outlet;
The gas outlet of described air-suction cover is connected with the air inlet of escaping gas processing means;At described escaping gas
It is additionally provided with gas double purification device and drying tower, the air inlet of described escaping gas processing means between reason device and blower fan
Particle filtering net it is provided with at Kou;
The gas outlet of described escaping gas processing means is connected with the air inlet of gas double purification device by pipeline
Connecing, the gas outlet of described gas double purification device is connected with the air inlet of drying tower by pipeline;
Particle filtering net, the gas outlet of described drying tower and the air inlet of blower fan it is provided with at the air inlet of described drying tower
It is connected.
Further, the escaping gas of described closing produces region is coating room or food cooking area or metallo-plastic
Finished product produces region;Described escaping gas processing means is low-temperature plasma processing means and photocatalyst processing means or activity
Charcoal adsorbent equipment or vapour phase oxidation process processing means.
Further, state metallo-plastic finished product and produce region for injection machine room or die casting machine room or machine room of casting;Described
It is injection machine or die casting machine or casting machine that metallo-plastic finished product produces machine.
Further, described gas double purification device is water curtain tower or spray column.
Further, it is provided with activated carbon or activated alumina in described drying tower.
Further, honeycomb active carbon filter net or activated alumina filtration net it are provided with in described drying tower.
The escaping gas processing cycle of the present invention uses the method that system carries out escaping gas process, it is characterised in that
Comprise the following steps:
(1) escaping gas produces the gas outlet in region through pipeline by escaping gas by the escaping gas closed
The air inlet of reason device enters in escaping gas processing means and processes;
(2) escaping gas is after escaping gas processing means processes, by giving vent to anger of escaping gas processing means
Mouthful be connected with the air inlet of blower fan by pipeline, described blower fan rely on the mechanical energy raising escaping gas pressure of input by
Escaping gas after reason transfers out;
(3) air inlet that the gas outlet of described blower fan produces region with the escaping gas of closing is connected.
Further, in step (1), it is additionally provided with gas secondary between described escaping gas processing means and blower fan
Purifier and drying tower;The air inlet of described escaping gas processing means is additionally provided with particle filtering net;
Escaping gas giving vent to anger via escaping gas processing means after escaping gas processing means processes
Mouth is connected by the air inlet of pipeline with gas double purification device, enters gas double purification device, described gas secondary
Dust in escaping gas or abnormal flavour or ozone are processed by purifier;
Particle filtering net it is provided with at the air inlet of described drying tower;Volatilization after gas double purification device processes
Property gas, is connected with the air inlet of drying tower by pipeline via the gas outlet of gas double purification device, described drying tower
Escaping gas is processed;
Escaping gas after described process is connected with the air inlet of blower fan via the gas outlet of drying tower.
Further, described gas double purification device is water curtain tower, and described escaping gas is in water curtain tower
The cleaning of solution, the microgranule of the PM2.5 in escaping gas and solubilized composition enter in solution, and described solution is in the mistake of spray
Journey produces aqueous vapor.
Further, in described step (1), escaping gas produces region is coating room, and described escaping gas processes
Device is low-temperature plasma processing means and photocatalyst processing means;
Macromolecular mass, under the splitting action of low-temperature plasma processing means, is decomposed into subset by escaping gas,
It is i.e. carbon dioxide and water by ozone oxidation;
The small organic molecule group not being completely broken down, enters photocatalyst processing means and carries out photodissociation purification, volatility gas
Superoxide anion and hydroxyl free radical that body is produced by photocatalyst processing means are oxidizing to end product carbon dioxide and water;
Described carbon dioxide, water and unnecessary superoxide anion enter water curtain tower, and superoxide anion is by gas secondary purifying
Recirculated water in gasifying device is decomposed into rapidly oxygen;Aqueous escaping gas enters drying tower, the honeycomb being dried in tower activity
Steam is absorbed by carbon drainage screen.
Further, in described step (1), escaping gas produces region is coating room, and described escaping gas processes dress
It is set to vapour phase oxidation process processing means,
In described vapour phase oxidation process processing means escaping gas process solvent be water, be equipped with a certain amount of hydrogen peroxide and
DORC forms composite absorption liquid;
The hydrogen peroxide having Strong oxdiative ability produces chain under the synergism of DORC and passes reaction, and hydrogen peroxide is all cleaved into along weak bond
Two, with unpaired only electronics gene, produce a large amount of strong oxidizing property hydroxyl radical free radicals in working solution high speed, make volatility gas
Organic molecule in body is oxidized to carbon dioxide and water;
Described carbon dioxide, water and unnecessary superoxide anion enter water curtain tower, and superoxide anion is by gas secondary purifying
Recirculated water in gasifying device is decomposed into rapidly the aqueous escaping gas of oxygen and enters drying tower, the honeycomb activated carbon being dried in tower
Steam is absorbed by drainage screen.
Further, in described step (1), escaping gas produces region is coating room, and escaping gas processing means is
Absorbent charcoal adsorber;Described absorbent charcoal adsorber carries out adsorption treatment to escaping gas;
Dust is precipitated by described water curtain tower, absorbs;Described aqueous escaping gas enters drying tower, is dried tower
In honeycomb active carbon filter net steam is absorbed.
The escaping gas processing cycle of the present invention uses the method that system carries out escaping gas process, it is characterised in that
Comprise the following steps:
(1) escaping gas passes through pipeline by the gas outlet of the food cooking area closed and oil-water separation water curtain tower
Air inlet is connected, and enters in oil-water separation water curtain tower and processes, is separated by profit, remove escaping gas simultaneously
In dust or abnormal flavour or ozone;
(2) described escaping gas is processed dress by the gas outlet of oil-water separation water curtain tower with escaping gas by pipeline
The air inlet put is connected, and enters in escaping gas processing means and processes;
(3) escaping gas is after escaping gas processing means processes, by giving vent to anger of escaping gas processing means
Mouthful be connected with the air inlet of blower fan by pipeline, described blower fan rely on the mechanical energy raising escaping gas pressure of input by
Escaping gas after reason transfers out;
(4) gas outlet of described blower fan is connected with the air inlet of the food cooking area of closing.
Further, in step (3), it is additionally provided with drying tower between described escaping gas processing means and blower fan;
It is provided with particle filtering net at the air inlet of described escaping gas processing means;
The gas outlet of described escaping gas processing means is connected with the air inlet of drying tower by pipeline, described dry
Escaping gas is processed by tower;Particle filtering net it is provided with at the air inlet of described drying tower;Volatilization after described process
Property gas is connected with the air inlet of blower fan via the gas outlet of drying tower, and steam is absorbed by drying tower.
The escaping gas processing cycle of the present invention uses the method that system carries out escaping gas process, including following step
Rapid:
(1) escaping gas is produced gas outlet and the escaping gas in region by pipeline by the metallo-plastic finished product closed
The air inlet of processing means is connected, and enters in escaping gas processing means and processes;
(2) escaping gas is after escaping gas processing means processes, by giving vent to anger of escaping gas processing means
Mouthful be connected with the air inlet of blower fan by pipeline, described blower fan rely on the mechanical energy raising escaping gas pressure of input by
Escaping gas after reason transfers out;
(4) air inlet that the gas outlet of described blower fan produces region with the metallo-plastic finished product of closing is connected.
Further, in step (1), between described escaping gas processing means and blower fan, it is additionally provided with gas secondary purifying
Gasifying device and drying tower;It is provided with particle filtering net at the air inlet of described escaping gas processing means;
The gas outlet of described escaping gas processing means is connected with the air inlet of drying tower by pipeline, described dry
Escaping gas is processed by tower;Particle filtering net it is provided with at the air inlet of described drying tower;Volatilization after described process
Property gas is connected with the air inlet of blower fan via the gas outlet of drying tower, and steam is absorbed by drying tower.
Beneficial effect: the escaping gas of the closing of the present invention produces escaping gas processing system and the side thereof in region
Method, simple and easy to do, reasonable in design, energy-conserving and environment-protective.
(1) escaping gas without sticky particle thing enters the low-temperature plasma process dress of escaping gas processing means
Putting and photocatalyst processing means or vapour phase oxidation process processing means or activated carbon adsorption unit, escaping gas molecule is through processing
After obtain carbon dioxide and water, it is ensured that escaping gas purification up to standard, reach discharging standards;
(2) ability of the process of native system and processing method thereof exceedes country's secondary discharge standard, it is to avoid traditional work
Property carbon process the uncontrolled state of secondary pollution;
(3) gas after processing processes via gas double purification device, both can purify PM2.5, again can be clean
Ozone in activating QI body so that gas reaches the requirement that air recycles.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention;
Fig. 2 is the structural representation of first embodiment of the invention;
Fig. 3 is the structural representation of second embodiment of the invention;
Fig. 4 is the structural representation of third embodiment of the invention;
Fig. 5 is the structural representation of fourth embodiment of the invention;
Fig. 6 is the structural representation of fifth embodiment of the invention;
Fig. 7 is the structural representation of sixth embodiment of the invention;
Fig. 8 is the structural representation of seventh embodiment of the invention;
Fig. 9 is low-temperature plasma processing means and the photocatalyst processing means axonometric chart of the present invention;
Figure 10 is low-temperature plasma processing means and the internal structure plane graph of photocatalyst processing means of the present invention;
Figure 11 is low-temperature plasma processing means and the photocatalyst processing means internal structure front elevation of the present invention;
Figure 12 is the structural plan figure of the photocatalyst generator of the present invention;
Figure 13 is the double-dielectric barrier discharge structural representation in the low-temperature plasma generator of the present invention;
Figure 14 is the schematic diagram of the vapour phase oxidation process processing means of the present invention;
Figure 15 is the schematic diagram of the absorbent charcoal adsorber of the present invention;
Figure 16 is the internal framework schematic diagram of the absorbent charcoal adsorber of the present invention;
Figure 17 is the drawer structure schematic diagram of the absorbent charcoal adsorber of the present invention;
Figure 18 is that the labyrinth air-flow of the absorbent charcoal adsorber of the present invention moves towards figure;
Figure 19 is the activated carbon adsorption schematic diagram of the absorbent charcoal adsorber of the present invention;
Wherein: 1 escaping gas processing means;2 exhaust apparatus;3 escaping gases produce region;301 escaping gases
Produce the air inlet in region;302 escaping gases produce the gas outlet in region;4 gas double purification devices;5 drying towers;6 water
Curtain tower;7 spray columns;8 coating rooms;9 food cooking area;10 air-suction covers;11 injection machine rooms;12 depurator casings;1201 ground
Foot;1202 hermatic doors;1203 primary filter net and homogenizing plates;The gas outlet of 1204 depurator casings;1205 depurator casings
Air inlet;13 low-temperature plasma processing meanss;1301 low-temperature plasma generators;1302 plasma pulse power supplys;1303 low temperature
Plasma generator power supply;1304 low-temperature plasma generator guide rails;1305 ground electrodes;1306 block medias;1307 high pressure
Electrode;1308 discharging gaps;14 photocatalyst processing meanss;1401 ultraviolet ray photocatalyst generators;1402 quartz burners;1403
Ultraviolet ray photocatalyst generator power;1404 photocatalyst net power supplys;1405 ultraviolet ray photocatalyst generator guide rails;15 activated carbons are inhaled
Adsorption device;1501 air inlets;1502 gas outlets;1503 activated carbon drawers;1504 quick clips;1505 activated carbons process casing;
1506 intercept net;1507 labyrinth, gas outlet baffle plates;1508 drawer handles;1509 lower margins;1510 maintenance doors;1511 activated carbons;
1512 air inlet labyrinth baffle plates;1513 cross flow proof dividing plates;1514 support keels;1515 drawer rails;1516 cylindrical particle activity
Charcoal;1517 escaping gas molecule and impurity;16 vapour phase oxidation process processing meanss;1601 spray columns;1602 liquid medicine water storage boxes;
1603 circulation fluid outlets;1604 water outlet valves;1605 water pumps;1606 air inlets;1607 circulation fluid pipelines;1608 water inlet valves;
1609 mouth sprays;1610 filler rooms;1611 gas outlets;17 oil-water separation water curtain towers;18 particle filtering nets;19 filters;20
Die casting machine room;21 injection machines;22 die casting machines;23 casting machine rooms;24 casting machines.
Detailed description of the invention
In order to illustrate technical scheme and technical purpose, below in conjunction with the accompanying drawings and detailed description of the invention is to the present invention
It is described further.
Embodiment 1
As depicted in figs. 1 and 2, a kind of escaping gas processing cycle uses system, described escaping gas processing cycle
Use system includes escaping gas processing means 1 and blower fan 2;Described escaping gas processing means is by pipeline and blower fan 2
It is connected;
Described escaping gas processing cycle uses system also to include, and the escaping gas closed produces region 3;
Described escaping gas produces region 3 and is provided with air inlet and gas outlet, in described escaping gas processing means 1
It is provided with air inlet and gas outlet, described blower fan 2 is provided with air inlet and gas outlet;
Described escaping gas produces the gas outlet in region 3 and is connected with the air inlet of described escaping gas processing means 1
Connect;It is provided with particle filtering net 18 at the air inlet of described escaping gas processing means 1;Described escaping gas processing means
The gas outlet of 1 is connected by the air inlet of pipeline with blower fan 2, and the escaping gas of the gas outlet of described blower fan 2 and closing produces
The air inlet in raw region 3 is connected.
Gas double purification device 4 and drying tower 5 it is additionally provided with between described escaping gas processing means 1 and blower fan 2;
It is provided with air inlet and gas outlet on described gas double purification device 4, described drying tower 5 is provided with air inlet
And gas outlet;
The gas outlet of described escaping gas processing means 1 is connected with the air inlet of gas double purification device 4, described
The gas outlet of gas double purification device 4 is connected with the air inlet of drying tower 5;It is provided with at the air inlet of described drying tower 5
Particle filtering net 18, the gas outlet of described drying tower 5 is connected with the air inlet of blower fan 2.
It is coating room 8 that described escaping gas produces region 3.Coating room 8 is to provide the closing of painting operation private environment
Space, the artificial environment manufactured in coating room 8, painting operation can be met to the temperature of environment, humidity, illumination, cleanliness factor etc.
Demand;Relative comfort, the working environment of safety is created for operator;The coating cloud of the generation of painting operation can be processed, protection
Spray exempts from secondary pollution, is that the coating particle that swims in order to produce when making spray-coating can be in time from the on-the-spot band of spraying
Walk, to ensure coating quality.
Described gas double purification device 4 is water curtain tower 6.Water curtain tower 6 is for the float more than PM2.5 particle diameter
Mainly being affected by relative air humidity, when the humidity increases, pollutant rich surface contains steam, by being mutually condensed into bigger
Grain settles;When relative humidity diminishes, pollutant superficial attractive forces is little, is difficult to flocking settling, condenses under wind-force effect
A material can decompose, owing to particle diameter diminishes, being more easy to suspends causes lasting pollution.To air humidification low cost, effective, use
Water spray spray system can effectively administer, with water Xian's air, the atmospheric pollution that city PM2.5 exceeds standard.
Described cascade tower 6 has ozone contained by gas after escaping gas processes simultaneously concurrently and reacts the most double for water after contacting with water
Have in the escaping gas of coating room 8 gas outlet and paint sticky particle through escaping gas process import and export particle filtering process obstruction
During normal work, efflorescence sticky particle thing effect is also after processing order at this moment, the coating room 8 that need to be varied as desired in.
As shown in Fig. 9 to Figure 13, described escaping gas processing means 1 is low-temperature plasma processing means 13 and photocatalyst
Processing means 14.
Described low-temperature plasma processing means 13 and photocatalyst processing means 14 are integrally disposed in depurator casing 12;Institute
Stating and be provided with air inlet and gas outlet on depurator casing 12, described depurator casing 12 passes through pipeline and water curtain tower 6, is dried
Tower 5 is sequentially connected and connects;
Described low-temperature plasma processing means 13 includes that low-temperature plasma generator 1301 and low-temperature plasma generator are led
Rail 1304, described low-temperature plasma generator 1301 is arranged on low-temperature plasma generator guide rail 1304;
Described photocatalyst processing means 14 includes that ultraviolet ray photocatalyst generator 1401 and ultraviolet ray photocatalyst generator are led
Rail 1405, described ultraviolet ray photocatalyst generator 1401 is arranged on ultraviolet ray photocatalyst generator guide rail 1405;
One end of described depurator casing 12 is provided with low-temperature plasma generator power supply 1303 and ultraviolet ray photocatalyst is sent out
Raw device power supply 1403;Described low-temperature plasma generator power supply 1303 is by electric connection line and low-temperature plasma generator 1301 phase
Connect, provide electric energy to low-temperature plasma generator 1301;Described ultraviolet ray photocatalyst generator power 1403 is by electrical connection
Line is connected with ultraviolet ray photocatalyst generator 1401, provides electric energy to ultraviolet ray photocatalyst generator 1401.
Described depurator casing 12 is provided with air inlet, described air inlet near the outside of low-temperature plasma generator 1301
On be provided with primary filter net and homogenizing plate 1203;
Being provided with hermatic door 1202 on described depurator casing 12, the bottom of described depurator casing 12 is equipped with lower margin
1201;
Described depurator casing 12 is provided with gas outlet near the outside of ultraviolet ray photocatalyst generator 1401.
High-field electrode 1307, ground electrode 1305 it is provided with in described low-temperature plasma generator 1301, and equipped with stop
Medium 1306, is provided with discharging gap 1308 between high-field electrode 1307 and ground electrode 1305, high-field electrode 1307 with connect
Ground electrode 1305 is connected with plasma pulse power supply 1302 respectively by wire;
Described ultraviolet ray photocatalyst generator 1401 is provided with quartz burner 1402, sets in quartz burner 1402 periphery
It is equipped with photocatalyst net 1404.
It is provided with activated carbon in described drying tower 5, in described drying tower 5, is provided with honeycomb active carbon filter net.
Described water curtain tower 6 include casing, recycle liquid pump, storage liquid case, recycle liquid pump, distribution box, liquid barrier, clean-up port,
Blowoff valve and fluid infusion mouth.Described box inside rear portion is provided with liquid curtain plate a, liquid curtain plate b;
Described liquid curtain plate a includes that circulation fluid case a and dentation curtain are along a;Described liquid curtain plate a top is provided with circulation fluid case a, follows
Ring liquid case a is provided with overfall a, and the circulation fluid Direct Uniform of overfall a overflow trickles on liquid curtain plate a, and liquid curtain plate a bottom sets
It is equipped with dentation curtain along a, and equipped with deflector a;
Described liquid curtain plate b includes that circulation fluid case b and dentation curtain are along b;Described liquid curtain plate b top is provided with circulation fluid case b, follows
Ring liquid case b is provided with overfall b, and the circulation fluid Direct Uniform of overfall b overflow trickles on liquid curtain plate b;Liquid curtain plate b bottom sets
It is equipped with dentation curtain along b, and equipped with deflector b.
Described lower box is provided with liquid bath, and liquid bath side is provided with liquid bath overfall;It is provided with outside described casing
Storing liquid case, described liquid bath overfall is connected with storing liquid case;Described storage liquid case is provided with inlet and liquid outlet;
Described inlet is used for supplying liquid in storage liquid case, keeps liquid level;Described storage liquid bottom portion, equipped with blowoff valve, uses
In storing liquid case blowdown;Liquid in described storage liquid case is water or oily or anti-icing fluid;Described storage liquid case side is provided with recycle liquid pump,
The inlet of recycle liquid pump is connected with storing liquid case by pipeline;Liquid-controlling valve a, liquid-controlling valve it is respectively provided with on described recycle liquid pump
B, is used for controlling circulation fluid case a and circulation fluid case b liquid inlet volume, in order to keep certain liquid level;
The liquid outlet of recycle liquid pump is connected with circulation fluid case a and circulation fluid case b respectively by circulation fluid pipe;Described follows
Equipped with liquid-controlling valve c in the input duct of ring liquid pump.
The escaping gas processing cycle described in claim 1 that utilizes of the present invention uses system to carry out at escaping gas
The method of reason, comprises the following steps:
(1) gas outlet that escaping gas produces region 3 by the escaping gas closed processes dress with escaping gas
The air inlet put enters in escaping gas processing means 1 and processes;
(2) escaping gas is after escaping gas processing means 1 processes, by going out of escaping gas processing means 1
QI KOU is connected by the air inlet of pipeline with blower fan 2, and described blower fan 2 relies on the mechanical energy of input to improve escaping gas pressure
Escaping gas after processing transfers out;
(3) air inlet that the gas outlet of described blower fan 2 produces region 3 with the escaping gas of closing is connected.
In step (1), described escaping gas produces region 3 is coating room 8.Described escaping gas processing means 1
And it is additionally provided with gas double purification device 4 and drying tower 5 between blower fan 2;
The gas outlet of described escaping gas processing means 1 is entered by the air inlet of pipeline with gas double purification device 4
Entering gas double purification device 4, the dust in escaping gas or abnormal flavour or ozone are carried out by described gas double purification device 4
Process;
Described escaping gas passes through the air inlet of pipeline and drying tower 5 by the gas outlet of gas double purification device 4
Being connected, escaping gas is processed by described drying tower 5;
Escaping gas after described process is connected with the air inlet of blower fan 2 via the gas outlet of drying tower 5.
Described gas double purification device 4 is water curtain tower 6, and described escaping gas is solution in water curtain tower 6
Cleaning, the microgranule of the PM2.5 in escaping gas and solubilized composition enter in solution, and described solution produces during spray
Unboiled water gas.
In described step (1), escaping gas produces region is coating room 8, and described escaping gas processing means 1 is low
Temperature plasma treatment appts 13 and photocatalyst processing means 14;
Macromolecular mass, under the splitting action of low-temperature plasma processing means 13, is decomposed into little molecule by escaping gas
Group, i.e. by ozone oxidation carbon dioxide and water;
The small organic molecule group not being completely broken down, enters photocatalyst processing means 14 and carries out photodissociation cleansing phase, wave
Superoxide anion and hydroxyl free radical that the property sent out gas is produced by photocatalyst processing means 14 are oxidizing to end product carbon dioxide
And water;The ability of the process of native system and processing method thereof exceedes country's secondary discharge standard, it is to avoid at traditional activated carbon
The reason uncontrolled state of secondary pollution.Water curtain tower both can purify PM2.5, can purify again the ozone in gas so that gas
Temperature reach air again with needs.
Described carbon dioxide, water and unnecessary superoxide anion enter water curtain tower 6, and superoxide anion is by gas secondary purifying
Recirculated water in gasifying device 4 is decomposed into rapidly oxygen;Aqueous escaping gas enters drying tower 5.It is dried in tower 5 and is provided with work
Property charcoal and honeycomb active carbon filter net, steam is absorbed by described drying tower 5.
Embodiment 2
As it is shown on figure 3, a kind of escaping gas processing cycle uses system, it is characterised in that: at described escaping gas
Reason recycling system includes absorbent charcoal adsorber 15 and blower fan 2;Described absorbent charcoal adsorber 15 is by pipeline and blower fan 2
It is connected;
Described escaping gas processing cycle uses system also to include the coating room 8 closed;Described absorbent charcoal adsorber
Particle filtering net 18 it is provided with at the air inlet of 15;
Described coating room 8 is provided with air inlet and gas outlet, described absorbent charcoal adsorber 15 is provided with air inlet and
Gas outlet, described blower fan 2 is provided with air inlet and gas outlet;
The gas outlet of described coating room 8 is connected with the air inlet of described absorbent charcoal adsorber 15;Described activated carbon is inhaled
The gas outlet of adsorption device 15 is connected by the air inlet of pipeline with blower fan 2, the gas outlet of described blower fan 2 and the coating room of closing
The air inlet of 8 is connected.
It is additionally provided with water curtain tower 6 between described absorbent charcoal adsorber 15 and blower fan 2;The air inlet of described drying tower 5
Place is provided with particle filtering net 18, described water curtain tower 6 is provided with air inlet and gas outlet, described drying tower 5 is provided with
Air inlet and gas outlet;
The gas outlet of described absorbent charcoal adsorber 15 is connected with the air inlet of water curtain tower 6, described water curtain tower 6
Gas outlet is connected with the air inlet of drying tower 5;The gas outlet of described drying tower 5 is connected with the air inlet of blower fan 2.
It is provided with activated alumina in described drying tower 5.It is provided with activated alumina filtration net in described drying tower 5.
Described water curtain tower includes casing, recycle liquid pump, storage liquid case, recycle liquid pump, distribution box, liquid barrier, clean-up port, row
Dirty valve and fluid infusion mouth.Described box inside rear portion is provided with liquid curtain plate a, liquid curtain plate b;
Described liquid curtain plate a includes that circulation fluid case a and dentation curtain are along a;Described liquid curtain plate a top is provided with circulation fluid case a, follows
Ring liquid case a is provided with overfall a, and the circulation fluid Direct Uniform of overfall a overflow trickles on liquid curtain plate a, and liquid curtain plate a bottom sets
It is equipped with dentation curtain along a, and equipped with deflector a;
Described liquid curtain plate b includes that circulation fluid case b and dentation curtain are along b;Described liquid curtain plate b top is provided with circulation fluid case b, follows
Ring liquid case b is provided with overfall b, and the circulation fluid Direct Uniform of overfall b overflow trickles on liquid curtain plate b;Liquid curtain plate b bottom sets
It is equipped with dentation curtain along b, and equipped with deflector b.
Described lower box is provided with liquid bath, and liquid bath side is provided with liquid bath overfall;It is provided with outside described casing
Storing liquid case, described liquid bath overfall is connected with storing liquid case;Described storage liquid case is provided with inlet and liquid outlet;
Described inlet is used for supplying liquid in storage liquid case, keeps liquid level;Described storage liquid bottom portion, equipped with blowoff valve, uses
In storing liquid case blowdown;Liquid in described storage liquid case is water or oily or anti-icing fluid;Described storage liquid case side is provided with recycle liquid pump,
The inlet of recycle liquid pump is connected with storing liquid case by pipeline;Liquid-controlling valve a, liquid-controlling valve it is respectively provided with on described recycle liquid pump
B, is used for controlling circulation fluid case a and circulation fluid case b liquid inlet volume, in order to keep certain liquid level;
The liquid outlet of recycle liquid pump is connected with circulation fluid case a and circulation fluid case b respectively by circulation fluid pipe;Described follows
Equipped with liquid-controlling valve c in the input duct of ring liquid pump.
The escaping gas processing cycle described in claim 1 that utilizes of the present invention uses system to carry out at escaping gas
The method of reason, comprises the following steps:
(1) escaping gas is entered with the air inlet of absorbent charcoal adsorber 15 by the gas outlet of coating room 8 closed
Absorbent charcoal adsorber 15 processes;
(2) escaping gas is after absorbent charcoal adsorber 15 processes, the gas outlet of absorbent charcoal adsorber 15 lead to
Piping is connected with the air inlet of blower fan 2, and described blower fan 2 relies on the mechanical energy of input to improve escaping gas pressure and will process
After escaping gas transfer out;
(3) gas outlet of described blower fan 2 is connected with the air inlet of the coating room 8 of closing.
In step (1), it is additionally provided with water curtain tower 6 and drying tower between described absorbent charcoal adsorber 15 and blower fan 2
5;
The gas outlet of described absorbent charcoal adsorber 15 enters water curtain tower 6 by the air inlet of pipeline with water curtain tower 6,
Dust in escaping gas or abnormal flavour or ozone are processed by described water curtain tower 6;
Described escaping gas is connected by the air inlet of pipeline with drying tower 5 by the gas outlet of water curtain tower 6, institute
State drying tower 5 escaping gas is processed;
Escaping gas after described process is connected with the air inlet of blower fan 2 via the gas outlet of drying tower 5.
Described escaping gas is the cleaning of solution in water curtain tower 6, the microgranule of the PM2.5 in escaping gas and can
Solvent components enters in solution, and described solution produces aqueous vapor during spray.
Dust is precipitated by described water curtain tower 6, absorbs;Described aqueous escaping gas enters drying tower 5, is dried
Being provided with activated carbon and honeycomb active carbon filter net in tower 5, steam is absorbed by described drying tower 5.
As shown in Figure 15 to Figure 19, described absorbent charcoal adsorber 15 carries out adsorption treatment to escaping gas;
Described absorbent charcoal adsorber 15 includes that activated carbon processes casing 1505.Described activated carbon processes casing 1505 and includes
Activated carbon drawer 1503, drawer rail 1515, quick clip 1504, drawer handle 1508, activated carbon 1511, intercept net 1506, enter
QI KOU labyrinth baffle plate 1512, labyrinth, gas outlet baffle plate 1507, cross flow proof dividing plate 1513, support keel 1514 and netted collet.
Be provided with activated carbon drawer 1503 on described drawer rail 1515, activated carbon drawer 1503 by quick clip 1504 with
Activated carbon processes casing 1505 and is fixedly connected.Netted collet, activated carbon drawer it is provided with bottom described activated carbon drawer 1503
1503 front portions are provided with drawer handle 1508.It is provided with activated carbon 1511 in described activated carbon drawer 1503.Described activated carbon
1511 is cylindrical particle activated carbon 1516.Described cylindrical particle activated carbon 1516 internal adsorption has escaping gas molecule and impurity
1517.Activated carbon 1511 is a kind of porous carbon containing matter, and it has highly developed hole structure, activated carbon more than 1511
Pore structure is provided for substantial amounts of surface area, can be fully contacted with gaseous impurity, thus it is peculiar to impart activated carbon 1511 institute
Absorption property so that it is be very easy to reach absorb the purpose collecting impurity.As magnetic force, all have between all of molecule
There is attractive interaction.Just because of this, the substantial amounts of molecule on activated carbon 1511 hole wall can produce powerful gravitation, thus reaches
The purpose that harmful impurity is attracted in aperture.
Described activated carbon drawer 1503 is 2 or more than 2.Described activated carbon processes the side of the air inlet of casing 1505
Being provided with obstruct net 1506 and air inlet labyrinth baffle plate 1512, the gas outlet processing casing 1505 at activated carbon is provided with gas outlet
Labyrinth baffle plate 1507.Described activated carbon processes bottom casing 1505 equipped with lower margin 1509;Described activated carbon processes casing
The one side of 1505 is provided with maintenance door 1510.
Embodiment 3
As shown in Fig. 4 and Figure 14, a kind of escaping gas processing cycle uses system, it is characterised in that: described volatility
Gassing cycle uses system to include vapour phase oxidation process processing means 16 and blower fan 2;Described vapour phase oxidation process processing means 16
It is connected with blower fan 2 by pipeline;
Described escaping gas processing cycle uses system also to include the coating room 8 closed;Described vapour phase oxidation process processes
Particle filtering net 18 it is provided with at the air inlet of device 16;
Described escaping gas produces region 3 and is provided with air inlet and gas outlet, described vapour phase oxidation process processing means 16
On be provided with air inlet and gas outlet, described blower fan 2 is provided with air inlet and gas outlet;
Described escaping gas produces the gas outlet in region 3 and is connected with the air inlet of described vapour phase oxidation process processing means 16
Connect;The gas outlet of described vapour phase oxidation process processing means 16 is connected by the air inlet of pipeline with blower fan 2, described blower fan 2
Gas outlet is connected with the air inlet of the coating room 8 of closing.
Spray column 7 and drying tower 5 it is additionally provided with between described vapour phase oxidation process processing means 16 and blower fan 2;
It is provided with air inlet and gas outlet on described spray column 7, described drying tower 5 is provided with air inlet and gas outlet;
It is provided with particle filtering net 18 at the air inlet of described drying tower 5,
The gas outlet of described vapour phase oxidation process processing means 16 is connected with the air inlet of spray column 7, described spray column 7
Gas outlet is connected with the air inlet of drying tower 5;The gas outlet of described drying tower 5 is connected with the air inlet of blower fan 2.
It is provided with activated alumina in described drying tower 5.It is provided with activated alumina filtration net in described drying tower 5.
Described water curtain tower includes casing, recycle liquid pump, storage liquid case, recycle liquid pump, distribution box, liquid barrier, clean-up port, row
Dirty valve and fluid infusion mouth.Described box inside rear portion is provided with liquid curtain plate a, liquid curtain plate b;
Described liquid curtain plate a includes that circulation fluid case a and dentation curtain are along a;Described liquid curtain plate a top is provided with circulation fluid case a, follows
Ring liquid case a is provided with overfall a, and the circulation fluid Direct Uniform of overfall a overflow trickles on liquid curtain plate a, and liquid curtain plate a bottom sets
It is equipped with dentation curtain along a, and equipped with deflector a;
Described liquid curtain plate b includes that circulation fluid case b and dentation curtain are along b;Described liquid curtain plate b top is provided with circulation fluid case b, follows
Ring liquid case b is provided with overfall b, and the circulation fluid Direct Uniform of overfall b overflow trickles on liquid curtain plate b;Liquid curtain plate b bottom sets
It is equipped with dentation curtain along b, and equipped with deflector b.
Described lower box is provided with liquid bath, and liquid bath side is provided with liquid bath overfall;It is provided with outside described casing
Storing liquid case, described liquid bath overfall is connected with storing liquid case;Described storage liquid case is provided with inlet and liquid outlet;
Described inlet is used for supplying liquid in storage liquid case, keeps liquid level;Described storage liquid bottom portion, equipped with blowoff valve, uses
In storing liquid case blowdown;Liquid in described storage liquid case is water or oily or anti-icing fluid;Described storage liquid case side is provided with recycle liquid pump,
The inlet of recycle liquid pump is connected with storing liquid case by pipeline;Liquid-controlling valve a, liquid-controlling valve it is respectively provided with on described recycle liquid pump
B, is used for controlling circulation fluid case a and circulation fluid case b liquid inlet volume, in order to keep certain liquid level;
The liquid outlet of recycle liquid pump is connected with circulation fluid case a and circulation fluid case b respectively by circulation fluid pipe;Described follows
Equipped with liquid-controlling valve c in the input duct of ring liquid pump.
The escaping gas processing cycle described in claim 1 that utilizes of the present invention uses system to carry out at escaping gas
The method of reason, comprises the following steps:
(1) air inlet of escaping gas gas outlet and the vapour phase oxidation process processing means 16 of coating room 8 by closing
Enter in escaping gas processing means 1 and process;
(2) escaping gas is after vapour phase oxidation process processing means 16 processes, by vapour phase oxidation process processing means 16
Gas outlet is connected by the air inlet of pipeline with blower fan 2, and described blower fan 2 relies on the mechanical energy of input to improve escaping gas pressure
Escaping gas after power will process transfers out;
(3) gas outlet of described blower fan 2 is connected with the air inlet of the coating room 8 of closing.
In step (1), it is additionally provided with spray column 7 between described vapour phase oxidation process processing means 16 and blower fan 2 and is dried
Tower 5;
As shown in figure 14, the gas outlet of described vapour phase oxidation process processing means 16 is by the air inlet of pipeline with spray column 7
Entering spray column 7, the dust in escaping gas or abnormal flavour or ozone are processed by described spray column 7;
Described escaping gas is connected by the air inlet of pipeline with drying tower 5 by the gas outlet of spray column 7, described
Escaping gas is processed by drying tower 5;
Escaping gas after described process is connected with the air inlet of blower fan 2 via the gas outlet of drying tower 5.
Described escaping gas is the cleaning of solution in spray column 7, the microgranule of the PM2.5 in escaping gas and solvable
Solving composition and enter in solution, described solution produces aqueous vapor during spray.
The solvent that in described vapour phase oxidation process processing means 16, escaping gas processes is water, is equipped with a certain amount of hydrogen peroxide
Composite absorption liquid is formed with DORC;
The hydrogen peroxide having Strong oxdiative ability produces chain under the synergism of DORC and passes reaction, and hydrogen peroxide is all cleaved into along weak bond
Two, with unpaired only electronics gene, produce a large amount of strong oxidizing property hydroxyl radical free radicals in working solution high speed, make volatility gas
Organic molecule in body is oxidized to carbon dioxide and water;
Described carbon dioxide, water and unnecessary superoxide anion enter spray column 7, and superoxide anion is by gas double purification
Recirculated water in device 4 is decomposed into rapidly the aqueous escaping gas of oxygen and enters drying tower 5, is provided with active oxygen in drying tower 5
Changing aluminum and activated alumina filtration net, steam is absorbed by described drying tower 5.
Be provided with solvent and solution in described vapour phase oxidation process processing means 16, described for escaping gas process molten
Agent is water, and solution is oxydol H2O2The composite absorption liquid formed with DORC.
As shown in figure 14, described vapour phase oxidation process processing means includes spray column 1601, liquid medicine water storage box 1602 and water pump
1605, described water pump 1605 is provided with water inlet and water out.
The side of described spray column 1601 is provided with water pump 1605, and described liquid medicine water storage box 1602 is by pipeline and water pump
1605 water inlets are connected;Described water pump 1605 outlet is connected with spray column 1601 by pipeline, described spray column 1601
It is connected with the liquid medicine water storage box 1602 of its underpart by pipeline.
Described spray column 1601 bottom is provided with air inlet, and spray column 1601 top is provided with gas outlet.
Be provided with mouth spray 1609 on described spray column 1601 interior conduit, water pump 1605 water outlet pipeline is provided with into
Mouth of a river valve 1608.Be provided with bottom described spray column 7 circulation fluid outlet 1603, described circulation fluid outlet 1603 be provided with water outlet
The pipeline of mouth valve 1604 is connected;Described water outlet valve 1604 is connected with liquid medicine water storage box 1602.
Being provided with filler room 1610 in described spray column 1601, filler room 1610 is built with filler.Spray column 1601 bottom
Being provided with air inlet 1606, spray column 1601 top is provided with gas outlet 1606, is connected with clean aiutage by pipeline;In spray
Drench and bottom tower 1601, be provided with circulation fluid outlet 1603, have water outlet valve 1608 by Pipe installing, under spray column 1601 tower body
Portion is provided with liquid medicine water storage box 1602;Circulation fluid outlet 1603 is by water outlet valve 1604, outlet pipe and liquid medicine water storage box 1602
Connection;Water pump 1605 is arranged on spray column 1601 side, and water pump 1605 water inlet is connected with liquid medicine water storage box 1602 by pipeline
Logical, water pump 1605 outlet is connected into spray column 1601 top, the circulation fluid in spray column 1601 by circulation fluid pipeline 1607
It is provided with mouth spray on pipeline 1607, water pump 1605 exit circulation fluid pipeline 1607 is provided with water inlet valve 1608.
Embodiment 4
As it is shown in figure 5, a kind of escaping gas processing cycle uses system, it is characterised in that: at described escaping gas
Reason recycling system includes oil-water separation water curtain tower 17, escaping gas processing means 1 and blower fan 2;
Described escaping gas processing cycle uses system also to include the food cooking area 9 closed;Described oil-water separation
It is provided with air inlet and gas outlet on water curtain tower 17, described escaping gas processing means 1 is provided with air inlet and gives vent to anger
Mouthful, described blower fan 2 is provided with air inlet and gas outlet;
Described food cooking area 9 is provided with air inlet and gas outlet, going out of described oil-water separation water curtain tower apparatus 17
QI KOU is connected by the air inlet of pipeline with escaping gas processing means 1, giving vent to anger of described escaping gas processing means 1
Mouth is connected by the air inlet of pipeline with blower fan 2, and the gas outlet of described blower fan 2 is connected with the air inlet of food cooking area 9
Connect.
Described food cooking area 9 is kitchen.
Described escaping gas processing cycle uses system also to include being arranged at escaping gas processing means 1 and blower fan 2
Between drying tower 5;It is provided with particle filtering net 18 at the air inlet of described escaping gas processing means 1;
Air inlet and gas outlet it is provided with on described drying tower;The gas outlet of described escaping gas processing means 1 is passed through
Pipeline is connected with the air inlet of drying tower 5;
Particle filtering net 18, the gas outlet of described drying tower 5 and blower fan 2 it is provided with at the air inlet of described drying tower 5
Air inlet is connected.
Described oil-water separation water curtain tower 17 includes casing, recycle liquid pump, storage liquid case, recycle liquid pump, distribution box, gear liquid
Plate, clean-up port, blowoff valve and fluid infusion mouth.Described box inside rear portion is provided with liquid curtain plate a, liquid curtain plate b;
Described liquid curtain plate a includes that circulation fluid case a and dentation curtain are along a;Described liquid curtain plate a top is provided with circulation fluid case a, follows
Ring liquid case a is provided with overfall a, and the circulation fluid Direct Uniform of overfall a overflow trickles on liquid curtain plate a, and liquid curtain plate a bottom sets
It is equipped with dentation curtain along a, and equipped with deflector a;
Described liquid curtain plate b includes that circulation fluid case b and dentation curtain are along b;Described liquid curtain plate b top is provided with circulation fluid case b, follows
Ring liquid case b is provided with overfall b, and the circulation fluid Direct Uniform of overfall b overflow trickles on liquid curtain plate b;Liquid curtain plate b bottom sets
It is equipped with dentation curtain along b, and equipped with deflector b.
Described lower box is provided with liquid bath, is provided with fluid groove overfall in liquid bath side;Arrange outside described casing
Having storage liquid case, described fluid groove overfall is connected with storing liquid case;Described storage liquid case is provided with inlet and liquid outlet, liquid outlet
There is oil removal nethike embrane;
Described inlet is used for supplying liquid in storage liquid case, keeps liquid level;Described storage liquid bottom portion, equipped with blowoff valve, uses
In storing liquid case blowdown;Liquid in described storage liquid case is water or oily or anti-icing fluid;Or described in refueling device, store the installation of liquid case side
Having recycle liquid pump, the inlet of recycle liquid pump is connected with storing liquid case by pipeline;It is respectively provided with control on described recycle liquid pump
Liquid valve a, liquid-controlling valve b, be used for controlling circulation fluid case a and circulation fluid case b liquid inlet volume, in order to keep certain liquid level;
The liquid outlet of recycle liquid pump is connected with circulation fluid case a and circulation fluid case b respectively by circulation fluid pipe;Described follows
Equipped with liquid-controlling valve c in the input duct of ring liquid pump.
Escaping gas processing cycle of the present invention uses the method that system carries out escaping gas process, and its feature exists
In comprising the following steps:
(1) escaping gas passes through pipeline by the air inlet of the gas outlet in the kitchen 9 closed Yu oil-water separation water curtain tower 17
Mouth is connected, and enters in oil-water separation water curtain tower 17 and processes, is separated by profit, removes in escaping gas simultaneously
Dust or abnormal flavour or ozone;
(2) described escaping gas is processed with escaping gas by the gas outlet of oil-water separation water curtain tower 17 by pipeline
The air inlet of device 1 is connected, and enters in escaping gas processing means 1 and processes;
(3) escaping gas is after escaping gas processing means 1 processes, by going out of escaping gas processing means 1
QI KOU is connected by the air inlet of pipeline with blower fan 2, and described blower fan 2 relies on the mechanical energy of input to improve escaping gas pressure
Escaping gas after processing transfers out;
(4) gas outlet of described blower fan 2 is connected with the air inlet in the kitchen 9 of closing.
In step (3), it is additionally provided with drying tower 5 between described escaping gas processing means 1 and blower fan 2;Described wave
It is provided with particle filtering net 18 at the air inlet of the property sent out gas treatment equipment 1;
The gas outlet of described escaping gas processing means 1 is connected by the air inlet of pipeline with drying tower 5, described dry
Escaping gas is processed by dry tower 5;It is provided with particle filtering net 18 at the air inlet of described drying tower 5;After described process
Escaping gas be connected with the air inlet of blower fan 2 via the gas outlet of drying tower 5, drying tower 5 is provided with active oxidation
Aluminum and activated alumina filtration net, steam is absorbed by described drying tower 5.
Described escaping gas processing means 1 is vapour phase oxidation process processing means 16, photocatalyst processing means 14, low temperature etc.
One or more in ion manipulation arrangement 13, absorbent charcoal adsorber 15.
As shown in Fig. 9 to Figure 13, described escaping gas processing means 1 is low-temperature plasma processing means 13 and photocatalyst
Processing means 14.
Described low-temperature plasma processing means 13 and photocatalyst processing means 14 are integrally disposed in depurator casing 12;Institute
Stating and be provided with air inlet and gas outlet on depurator casing 12, described depurator casing 12 passes through pipeline and water curtain tower 6, is dried
Tower 5 is sequentially connected and connects;
Described low-temperature plasma processing means 13 includes that low-temperature plasma generator 1301 and low-temperature plasma generator are led
Rail 1304, described low-temperature plasma generator 1301 is arranged on low-temperature plasma generator guide rail 1304;
Described photocatalyst processing means 14 includes that ultraviolet ray photocatalyst generator 1401 and ultraviolet ray photocatalyst generator are led
Rail 1405, described ultraviolet ray photocatalyst generator 1401 is arranged on ultraviolet ray photocatalyst generator guide rail 1405;
One end of described depurator casing 12 is provided with low-temperature plasma generator power supply 1303 and ultraviolet ray photocatalyst is sent out
Raw device power supply 1403;Described low-temperature plasma generator power supply 1303 is by electric connection line and low-temperature plasma generator 1301 phase
Connect, provide electric energy to low-temperature plasma generator 1301;Described ultraviolet ray photocatalyst generator power 1403 is by electrical connection
Line is connected with ultraviolet ray photocatalyst generator 1401, provides electric energy to ultraviolet ray photocatalyst generator 1401.
Described depurator casing 12 is provided with air inlet, described air inlet near the outside of low-temperature plasma generator 1301
On be provided with primary filter net and homogenizing plate 1203;
Being provided with hermatic door 1202 on described depurator casing 12, the bottom of described depurator casing 12 is equipped with lower margin
1201;
Described depurator casing 12 is provided with gas outlet near the outside of ultraviolet ray photocatalyst generator 1401.
High-field electrode 1307, ground electrode 1305 it is provided with in described low-temperature plasma generator 1301, and equipped with stop
Medium 1306, is provided with discharging gap 1308 between high-field electrode 1307 and ground electrode 1305, high-field electrode 1307 with connect
Ground electrode 1305 is connected with plasma pulse power supply 1302 respectively by wire;
Described ultraviolet ray photocatalyst generator 1401 is provided with quartz burner 1402, sets in quartz burner 1402 periphery
It is equipped with photocatalyst net 1404.
As shown in Figure 15 to Figure 19, described absorbent charcoal adsorber 15 carries out adsorption treatment to escaping gas;
Described absorbent charcoal adsorber 15 includes that activated carbon processes casing 1505.Described activated carbon processes casing 1505 and includes
Activated carbon drawer 1503, drawer rail 1515, quick clip 1504, drawer handle 1508, activated carbon 1511, intercept net 1506, enter
QI KOU labyrinth baffle plate 1512, labyrinth, gas outlet baffle plate 1507, cross flow proof dividing plate 1513, support keel 1514 and netted collet.
Be provided with activated carbon drawer 1503 on described drawer rail 1515, activated carbon drawer 1503 by quick clip 1504 with
Activated carbon processes casing 1505 and is fixedly connected.Netted collet, activated carbon drawer it is provided with bottom described activated carbon drawer 1503
1503 front portions are provided with drawer handle 1508.It is provided with activated carbon 1511 in described activated carbon drawer 1503.Described activated carbon
1511 is cylindrical particle activated carbon 1516.Activated carbon 1511 is a kind of porous carbon containing matter, and it has highly developed hole
Gap constructs, and the loose structure of activated carbon 1511 is provided for substantial amounts of surface area, can be fully contacted with gaseous impurity, thus compose
Give absorption property specific to activated carbon 1511 so that it is be very easy to reach to absorb the purpose collecting impurity.Such as magnetic force one
Sample, all has attractive interaction between all of molecule.Just because of this, the substantial amounts of molecule on activated carbon 1511 hole wall can produce
Raw powerful gravitation, thus reach the purpose being attracted in aperture by harmful impurity.
Described activated carbon drawer 1503 is 2 or more than 2.Described activated carbon processes the side of the air inlet of casing 1505
Being provided with obstruct net 1506 and air inlet labyrinth baffle plate 1512, the gas outlet processing casing 1505 at activated carbon is provided with gas outlet
Labyrinth baffle plate 1507.Described activated carbon processes bottom casing 1505 equipped with lower margin 1509;Described activated carbon processes casing
The one side of 1505 is provided with maintenance door 1510.
As shown in figure 14, described vapour phase oxidation process processing means includes spray column 1601, liquid medicine water storage box 1602 and water pump
1605, described water pump 1605 is provided with water inlet and water out.
The side of described spray column 1601 is provided with water pump 1605, and described liquid medicine water storage box 1602 is by pipeline and water pump
1605 water inlets are connected;Described water pump 1605 outlet is connected with spray column 1601 by pipeline, described spray column 1601
It is connected with the liquid medicine water storage box 1602 of its underpart by pipeline.
Described spray column 1601 bottom is provided with air inlet, and spray column 1601 top is provided with gas outlet.
Be provided with mouth spray 1609 on described spray column 1601 interior conduit, water pump 1605 water outlet pipeline is provided with into
Mouth of a river valve 1608.Be provided with bottom described spray column 7 circulation fluid outlet 1603, described circulation fluid outlet 1603 be provided with water outlet
The pipeline of mouth valve 1604 is connected;Described water outlet valve 1604 is connected with liquid medicine water storage box 1602.
Being provided with filler room 1610 in described spray column 1601, filler room 1610 is built with filler.Spray column 1601 bottom
Being provided with air inlet 1606, spray column 1601 top is provided with gas outlet 1606, is connected with clean aiutage by pipeline;In spray
Drench and bottom tower 1601, be provided with circulation fluid outlet 1603, have water outlet valve 1608 by Pipe installing, under spray column 1601 tower body
Portion is provided with liquid medicine water storage box 1602;Circulation fluid outlet 1603 is by water outlet valve 1604, outlet pipe and liquid medicine water storage box 1602
Connection;Water pump 1605 is arranged on spray column 1601 side, and water pump 1605 water inlet is connected with liquid medicine water storage box 1602 by pipeline
Logical, water pump 1605 outlet is connected into spray column 1601 top, the circulation fluid in spray column 1601 by circulation fluid pipeline 1607
It is provided with mouth spray on pipeline 1607, water pump 1605 exit circulation fluid pipeline 1607 is provided with water inlet valve 1608.
Embodiment 5
As shown in Figure 6, a kind of escaping gas processing cycle uses system, it is characterised in that: at described escaping gas
Reason recycling system includes escaping gas processing means 1 and blower fan 2;
Described escaping gas processing cycle uses system also to include being molded machine room 11;It is provided with on described injection machine room 11
Air inlet and gas outlet;It is provided with air inlet and gas outlet in described escaping gas processing means 1, described blower fan 2 is arranged
There are air inlet and gas outlet;
The gas outlet of described injection machine room 11 is connected by the air inlet of pipeline with escaping gas processing means 1, institute
The gas outlet stating escaping gas processing means 1 is connected by the air inlet of pipeline with blower fan 2, the gas outlet of described blower fan 2
It is connected with the air inlet of injection machine room 11.
Injection machine 21 and the air-suction cover 10 being arranged on injection machine 21 it is provided with in described injection machine room 11,
Being provided with gas outlet on described air-suction cover 10, the escaping gas that injection machine 21 is produced by described air-suction cover 10 sucks
In cover 10, described gas double purification device 4 is provided with air inlet and gas outlet, described drying tower 5 is provided with air inlet
And gas outlet;
The gas outlet of described air-suction cover 10 is connected with the air inlet of escaping gas processing means 1;Described volatility gas
Being additionally provided with gas double purification device 4 and drying tower 5 between body processing means 1 and blower fan 2, described escaping gas processes dress
Put and at the air inlet of 1, be provided with particle filtering net 18;
The gas outlet of described escaping gas processing means 1 is by the air inlet phase of pipeline with gas double purification device 4
Connecting, the gas outlet of described gas double purification device 4 is connected by the air inlet of pipeline with drying tower 5;
Particle filtering net 18, the gas outlet of described drying tower 5 and blower fan 2 it is provided with at the air inlet of described drying tower 5
Air inlet is connected.
Escaping gas processing cycle of the present invention uses the method that system carries out escaping gas process, and its feature exists
In comprising the following steps:
(1) escaping gas passes through pipeline by the gas outlet being molded machine room 11 closed and escaping gas processing means 1
Air inlet be connected, enter in escaping gas processing means 1 and process;
(2) escaping gas is after escaping gas processing means 1 processes, by going out of escaping gas processing means 1
QI KOU is connected by the air inlet of pipeline with blower fan 2, and described blower fan 2 relies on the mechanical energy of input to improve escaping gas pressure
Escaping gas after processing transfers out;
(4) gas outlet of described blower fan is connected with the air inlet of the injection machine room 11 of closing.
In step (1), it is additionally provided with double purification device between described escaping gas processing means and blower fan and is dried
Tower;It is provided with particle filtering net 18 at the air inlet of described escaping gas processing means 1;
The gas outlet of described escaping gas processing means 1 is connected by the air inlet of pipeline with drying tower 5, described dry
Escaping gas is processed by dry tower 5;It is provided with particle filtering net 18 at the air inlet of described drying tower 5;After described process
Escaping gas be connected with the air inlet of blower fan 2 via the gas outlet of drying tower 5, steam is absorbed by drying tower 5.
Described escaping gas processing means 1 includes that filter 19, low-temperature plasma processing means 13, photocatalyst process dress
Put 14, absorbent charcoal adsorber 15, vapour phase oxidation process processing means 16;Described filter 19, low-temperature plasma processing means 13,
Photocatalyst processing means 14, absorbent charcoal adsorber 15, vapour phase oxidation process processing means 16 are sequentially connected and connect;
The gas outlet of described air-suction cover 25 is connected with filter 19;
Impurity in escaping gas is stopped by described filter 19;
Escaping gas after described filter 19 filters enters described low-temperature plasma processing means 13, described low temperature etc.
Escaping gas is cracked by ion manipulation arrangement 13, under splitting action, macromolecular mass is decomposed into subset, i.e. by
Ozone oxidation carbon dioxide and water;
Described escaping gas after low-temperature plasma processing means 13 enters photocatalyst processing means 14, and described light touches
Matchmaker's processing means 14 carries out photodissociation cleansing phase to escaping gas, and escaping gas is by surpassing that photocatalyst processing means 14 produces
Negative oxygen ion and hydroxyl free radical are oxidizing to end product carbon dioxide and water;
As shown in Fig. 9 to Figure 13, described escaping gas processing means 1 is low-temperature plasma processing means 13 and photocatalyst
Processing means 14.
Described low-temperature plasma processing means 13 and photocatalyst processing means 14 are integrally disposed in depurator casing 12;Institute
Stating and be provided with air inlet and gas outlet on depurator casing 12, described depurator casing 12 passes through pipeline and water curtain tower 6, is dried
Tower 5 is sequentially connected and connects;
Described low-temperature plasma processing means 13 includes that low-temperature plasma generator 1301 and low-temperature plasma generator are led
Rail 1304, described low-temperature plasma generator 1301 is arranged on low-temperature plasma generator guide rail 1304;
Described photocatalyst processing means 14 includes that ultraviolet ray photocatalyst generator 1401 and ultraviolet ray photocatalyst generator are led
Rail 1405, described ultraviolet ray photocatalyst generator 1401 is arranged on ultraviolet ray photocatalyst generator guide rail 1405;
One end of described depurator casing 12 is provided with low-temperature plasma generator power supply 1303 and ultraviolet ray photocatalyst is sent out
Raw device power supply 1403;Described low-temperature plasma generator power supply 1303 is by electric connection line and low-temperature plasma generator 1301 phase
Connect, provide electric energy to low-temperature plasma generator 1301;Described ultraviolet ray photocatalyst generator power 1403 is by electrical connection
Line is connected with ultraviolet ray photocatalyst generator 1401, provides electric energy to ultraviolet ray photocatalyst generator 1401.
Described depurator casing 12 is provided with air inlet, described air inlet near the outside of low-temperature plasma generator 1301
On be provided with primary filter net and homogenizing plate 1203;
Being provided with hermatic door 1202 on described depurator casing 12, the bottom of described depurator casing 12 is equipped with lower margin
1201;
Described depurator casing 12 is provided with gas outlet near the outside of ultraviolet ray photocatalyst generator 1401.
High-field electrode 1307, ground electrode 1305 it is provided with in described low-temperature plasma generator 1301, and equipped with stop
Medium 1306, is provided with discharging gap 1308 between high-field electrode 1307 and ground electrode 1305, high-field electrode 1307 with connect
Ground electrode 1305 is connected with plasma pulse power supply 1302 respectively by wire;
Described ultraviolet ray photocatalyst generator 1401 is provided with quartz burner 1402, sets in quartz burner 1402 periphery
It is equipped with photocatalyst net 1404.
Described escaping gas after photocatalyst processing means 14 enters absorbent charcoal adsorber 15, and described activated carbon is inhaled
Adsorption device 15 carries out adsorption treatment to escaping gas;
As shown in Figure 15 to Figure 19, described absorbent charcoal adsorber 15 carries out adsorption treatment to escaping gas;
Described absorbent charcoal adsorber 15 includes that activated carbon processes casing 1505.Described activated carbon processes casing 1505 and includes
Activated carbon drawer 1503, drawer rail 1515, quick clip 1504, drawer handle 1508, activated carbon 1511, intercept net 1506, enter
QI KOU labyrinth baffle plate 1512, labyrinth, gas outlet baffle plate 1507, cross flow proof dividing plate 1513, support keel 1514 and netted collet.
Be provided with activated carbon drawer 1503 on described drawer rail 1515, activated carbon drawer 1503 by quick clip 1504 with
Activated carbon processes casing 1505 and is fixedly connected.Netted collet, activated carbon drawer it is provided with bottom described activated carbon drawer 1503
1503 front portions are provided with drawer handle 1508.It is provided with activated carbon 1511 in described activated carbon drawer 1503.Described activated carbon
1511 is cylindrical particle activated carbon 1516.Activated carbon 1511 is a kind of porous carbon containing matter, and it has highly developed hole
Gap constructs, and the loose structure of activated carbon 1511 is provided for substantial amounts of surface area, can be fully contacted with gaseous impurity, thus compose
Give absorption property specific to activated carbon 1511 so that it is be very easy to reach to absorb the purpose collecting impurity.Such as magnetic force one
Sample, all has attractive interaction between all of molecule.Just because of this, the substantial amounts of molecule on activated carbon 1511 hole wall can produce
Raw powerful gravitation, thus reach the purpose being attracted in aperture by harmful impurity.
Described activated carbon drawer 1503 is 2 or more than 2.Described activated carbon processes the side of the air inlet of casing 1505
Being provided with obstruct net 1506 and air inlet labyrinth baffle plate 1512, the gas outlet processing casing 1505 at activated carbon is provided with gas outlet
Labyrinth baffle plate 1507.Described activated carbon processes bottom casing 1505 equipped with lower margin 1509;Described activated carbon processes casing
The one side of 1505 is provided with maintenance door 1510.
Described escaping gas after absorbent charcoal adsorber 15 enters vapour phase oxidation process processing means 16, by volatility
Organic molecule in gas is oxidized to carbon dioxide and water;
As shown in figure 14, described vapour phase oxidation process processing means includes spray column 1601, liquid medicine water storage box 1602 and water pump
1605, described water pump 1605 is provided with water inlet and water out.
The side of described spray column 1601 is provided with water pump 1605, and described liquid medicine water storage box 1602 is by pipeline and water pump
1605 water inlets are connected;Described water pump 1605 outlet is connected with spray column 1601 by pipeline, described spray column 1601
It is connected with the liquid medicine water storage box 1602 of its underpart by pipeline.
Described spray column 1601 bottom is provided with air inlet, and spray column 1601 top is provided with gas outlet.
Be provided with mouth spray 1609 on described spray column 1601 interior conduit, water pump 1605 water outlet pipeline is provided with into
Mouth of a river valve 1608.Be provided with bottom described spray column 7 circulation fluid outlet 1603, described circulation fluid outlet 1603 be provided with water outlet
The pipeline of mouth valve 1604 is connected;Described water outlet valve 1604 is connected with liquid medicine water storage box 1602.
Being provided with filler room 1610 in described spray column 1601, filler room 1610 is built with filler.Spray column 1601 bottom
Being provided with air inlet 1606, spray column 1601 top is provided with gas outlet 1606, is connected with clean aiutage by pipeline;In spray
Drench and bottom tower 1601, be provided with circulation fluid outlet 1603, have water outlet valve 1608 by Pipe installing, under spray column 1601 tower body
Portion is provided with liquid medicine water storage box 1602;Circulation fluid outlet 1603 is by water outlet valve 1604, outlet pipe and liquid medicine water storage box 1602
Connection;Water pump 1605 is arranged on spray column 1601 side, and water pump 1605 water inlet is connected with liquid medicine water storage box 1602 by pipeline
Logical, water pump 1605 outlet is connected into spray column 1601 top, the circulation fluid in spray column 1601 by circulation fluid pipeline 1607
It is provided with mouth spray on pipeline 1607, water pump 1605 exit circulation fluid pipeline 1607 is provided with water inlet valve 1608.
Dust in escaping gas is absorbed by described water curtain tower 6, and superoxide anion is decomposed into rapidly oxygen;
Described aqueous escaping gas enters drying tower 5, is dried in tower 5 and is provided with activated carbon and honeycomb active carbon filter net, described
Steam is absorbed by drying tower.
Embodiment 6
As it is shown in fig. 7, a kind of escaping gas processing cycle uses system, it is characterised in that: at described escaping gas
Reason recycling system includes escaping gas processing means 1 and blower fan 2;
Described escaping gas processing cycle uses system also to include die casting machine room 20;It is provided with on described die casting machine room 20
Air inlet and gas outlet;It is provided with air inlet and gas outlet in described escaping gas processing means 1, described blower fan 2 is arranged
There are air inlet and gas outlet;
The gas outlet of described die casting machine room 20 is connected by the air inlet of pipeline with escaping gas processing means 1, institute
The gas outlet stating escaping gas processing means 1 is connected by the air inlet of pipeline with blower fan 2, the gas outlet of described blower fan 2
It is connected with the air inlet of die casting machine room 20.
Injection machine 13 and the air-suction cover 10 being arranged on die casting machine 22 it is provided with in described die casting machine room 20,
Being provided with gas outlet on described air-suction cover 10, the escaping gas that die casting machine 22 is produced by described air-suction cover 10 sucks
In cover 10, described gas double purification device 4 is provided with air inlet and gas outlet, described drying tower 5 is provided with air inlet
And gas outlet;
The gas outlet of described air-suction cover 10 is connected with the air inlet of escaping gas processing means 1;Described volatility gas
Being additionally provided with gas double purification device 4 and drying tower 5 between body processing means 1 and blower fan 2, described escaping gas processes dress
Put and at the air inlet of 1, be provided with particle filtering net 18;
The gas outlet of described escaping gas processing means 1 is by the air inlet phase of pipeline with gas double purification device 4
Connecting, the gas outlet of described gas double purification device 4 is connected by the air inlet of pipeline with drying tower 5;
Particle filtering net 18, the gas outlet of described drying tower 5 and blower fan 2 it is provided with at the air inlet of described drying tower 5
Air inlet is connected.
Escaping gas processing cycle of the present invention uses the method that system carries out escaping gas process, and its feature exists
In comprising the following steps:
(1) escaping gas passes through pipeline by the gas outlet of the die casting machine room 20 closed and escaping gas processing means 1
Air inlet be connected, enter in escaping gas processing means 1 and process;
(2) escaping gas is after escaping gas processing means 1 processes, by going out of escaping gas processing means 1
QI KOU is connected by the air inlet of pipeline with blower fan 2, and described blower fan 2 relies on the mechanical energy of input to improve escaping gas pressure
Escaping gas after processing transfers out;
(4) gas outlet of described blower fan is connected with the air inlet of the die casting machine room 20 of closing.
In step (1), between described escaping gas processing means 1 and blower fan 2, it is additionally provided with gas double purification device 4
With drying tower 5;It is provided with particle filtering net 18 at the air inlet of described escaping gas processing means 1;
The gas outlet of described escaping gas processing means 1 is connected by the air inlet of pipeline with drying tower 5, described dry
Escaping gas is processed by dry tower 5;It is provided with particle filtering net 18 at the air inlet of described drying tower 5;After described process
Escaping gas be connected with the air inlet of blower fan 2 via the gas outlet of drying tower 5, steam is absorbed by drying tower 5.
Described escaping gas processing means 1 includes that filter 19, low-temperature plasma processing means 13, photocatalyst process dress
Put 14, absorbent charcoal adsorber 15, vapour phase oxidation process processing means 16;Described filter 19, low-temperature plasma processing means 13,
Photocatalyst processing means 14, absorbent charcoal adsorber 15, vapour phase oxidation process processing means 16 are sequentially connected and connect;
The gas outlet of described air-suction cover 10 is connected with filter 19;
Impurity in escaping gas is stopped by described filter 19;
Escaping gas after described filter 19 filters enters described low-temperature plasma processing means 13, described low temperature etc.
Escaping gas is cracked by ion manipulation arrangement 13, under splitting action, macromolecular mass is decomposed into subset, i.e. by
Ozone oxidation carbon dioxide and water;
Described escaping gas after low-temperature plasma processing means 13 enters photocatalyst processing means 14, and described light touches
Matchmaker's processing means 14 carries out photodissociation cleansing phase to escaping gas, and escaping gas is by surpassing that photocatalyst processing means 14 produces
Negative oxygen ion and hydroxyl free radical are oxidizing to end product carbon dioxide and water;
As shown in Fig. 9 to Figure 13, described low-temperature plasma processing means 13 and photocatalyst processing means 14 integrally disposed in
In depurator casing 12;Being provided with air inlet and gas outlet on described depurator casing 12, described depurator casing 12 is by pipe
Road is sequentially connected connects with water curtain tower 6, drying tower 5;
Described low-temperature plasma processing means 13 includes that low-temperature plasma generator 1301 and low-temperature plasma generator are led
Rail 1304, described low-temperature plasma generator 1301 is arranged on low-temperature plasma generator guide rail 1304;
Described photocatalyst processing means 14 includes that ultraviolet ray photocatalyst generator 1401 and ultraviolet ray photocatalyst generator are led
Rail 1405, described ultraviolet ray photocatalyst generator 1401 is arranged on ultraviolet ray photocatalyst generator guide rail 1405;
One end of described depurator casing 12 is provided with low-temperature plasma generator power supply 1303 and ultraviolet ray photocatalyst is sent out
Raw device power supply 1403;Described low-temperature plasma generator power supply 1303 is by electric connection line and low-temperature plasma generator 1301 phase
Connect, provide electric energy to low-temperature plasma generator 1301;Described ultraviolet ray photocatalyst generator power 1403 is by electrical connection
Line is connected with ultraviolet ray photocatalyst generator 1401, provides electric energy to ultraviolet ray photocatalyst generator 1401.
Described depurator casing 12 is provided with air inlet, described air inlet near the outside of low-temperature plasma generator 1301
On be provided with primary filter net and homogenizing plate 1203;
Being provided with hermatic door 1202 on described depurator casing 12, the bottom of described depurator casing 12 is equipped with lower margin
1201;
Described depurator casing 12 is provided with gas outlet near the outside of ultraviolet ray photocatalyst generator 1401.
High-field electrode 1307, ground electrode 1305 it is provided with in described low-temperature plasma generator 1301, and equipped with stop
Medium 1306, is provided with discharging gap 1308 between high-field electrode 1307 and ground electrode 1305, high-field electrode 1307 with connect
Ground electrode 1305 is connected with plasma pulse power supply 1302 respectively by wire;
Described ultraviolet ray photocatalyst generator 1401 is provided with quartz burner 1402, sets in quartz burner 1402 periphery
It is equipped with photocatalyst net 1404.
Described escaping gas after photocatalyst processing means 14 enters absorbent charcoal adsorber 15, and described activated carbon is inhaled
Adsorption device 15 carries out adsorption treatment to escaping gas;
As shown in Figure 15 to Figure 19, described absorbent charcoal adsorber 15 carries out adsorption treatment to escaping gas;
Described absorbent charcoal adsorber 15 includes that activated carbon processes casing 1505.Described activated carbon processes casing 1505 and includes
Activated carbon drawer 1503, drawer rail 1515, quick clip 1504, drawer handle 1508, activated carbon 1511, intercept net 1506, enter
QI KOU labyrinth baffle plate 1512, labyrinth, gas outlet baffle plate 1507, cross flow proof dividing plate 1513, support keel 1514 and netted collet.
Be provided with activated carbon drawer 1503 on described drawer rail 1515, activated carbon drawer 1503 by quick clip 1504 with
Activated carbon processes casing 1505 and is fixedly connected.Netted collet, activated carbon drawer it is provided with bottom described activated carbon drawer 1503
1503 front portions are provided with drawer handle 1508.It is provided with activated carbon 1511 in described activated carbon drawer 1503.Described activated carbon
1511 is cylindrical particle activated carbon 1516.Activated carbon 1511 is a kind of porous carbon containing matter, and it has highly developed hole
Gap constructs, and the loose structure of activated carbon 1511 is provided for substantial amounts of surface area, can be fully contacted with gaseous impurity, thus compose
Give absorption property specific to activated carbon 1511 so that it is be very easy to reach to absorb the purpose collecting impurity.Such as magnetic force one
Sample, all has attractive interaction between all of molecule.Just because of this, the substantial amounts of molecule on activated carbon 1511 hole wall can produce
Raw powerful gravitation, thus reach the purpose being attracted in aperture by harmful impurity.
Described activated carbon drawer 1503 is 2 or more than 2.Described activated carbon processes the side of the air inlet of casing 1505
Being provided with obstruct net 1506 and air inlet labyrinth baffle plate 1512, the gas outlet processing casing 1505 at activated carbon is provided with gas outlet
Labyrinth baffle plate 1507.Described activated carbon processes bottom casing 1505 equipped with lower margin 1509;Described activated carbon processes casing
The one side of 1505 is provided with maintenance door 1510.
Described escaping gas after absorbent charcoal adsorber 15 enters vapour phase oxidation process processing means 16, by volatility
Organic molecule in gas is oxidized to carbon dioxide and water;
As shown in figure 14, described vapour phase oxidation process processing means includes spray column 1601, liquid medicine water storage box 1602 and water pump
1605, described water pump 1605 is provided with water inlet and water out.
The side of described spray column 1601 is provided with water pump 1605, and described liquid medicine water storage box 1602 is by pipeline and water pump
1605 water inlets are connected;Described water pump 1605 outlet is connected with spray column 1601 by pipeline, described spray column 1601
It is connected with the liquid medicine water storage box 1602 of its underpart by pipeline.
Described spray column 1601 bottom is provided with air inlet, and spray column 1601 top is provided with gas outlet.
Be provided with mouth spray 1609 on described spray column 1601 interior conduit, water pump 1605 water outlet pipeline is provided with into
Mouth of a river valve 1608.Be provided with bottom described spray column 7 circulation fluid outlet 1603, described circulation fluid outlet 1603 be provided with water outlet
The pipeline of mouth valve 1604 is connected;Described water outlet valve 1604 is connected with liquid medicine water storage box 1602.
Being provided with filler room 1610 in described spray column 1601, filler room 1610 is built with filler.Spray column 1601 bottom
Being provided with air inlet 1606, spray column 1601 top is provided with gas outlet 1606, is connected with clean aiutage by pipeline;In spray
Drench and bottom tower 1601, be provided with circulation fluid outlet 1603, have water outlet valve 1608 by Pipe installing, under spray column 1601 tower body
Portion is provided with liquid medicine water storage box 1602;Circulation fluid outlet 1603 is by water outlet valve 1604, outlet pipe and liquid medicine water storage box 1602
Connection;Water pump 1605 is arranged on spray column 1601 side, and water pump 1605 water inlet is connected with liquid medicine water storage box 1602 by pipeline
Logical, water pump 1605 outlet is connected into spray column 1601 top, the circulation fluid in spray column 1601 by circulation fluid pipeline 1607
It is provided with mouth spray on pipeline 1607, water pump 1605 exit circulation fluid pipeline 1607 is provided with water inlet valve 1608.
Dust in escaping gas is absorbed by described spray column 7, and superoxide anion is decomposed into rapidly oxygen;Institute
State aqueous escaping gas and enter drying tower 5, be dried in tower 5 and be provided with activated alumina and activated alumina filtration net, institute
State drying tower to be absorbed by steam.
Embodiment 7
As shown in Figure 8, a kind of escaping gas processing cycle uses system, it is characterised in that: at described escaping gas
Reason recycling system includes escaping gas processing means 1 and blower fan 2;
Described escaping gas processing cycle uses system also to include machine room 23 of casting;It is provided with on described casting machine room 23
Air inlet and gas outlet;It is provided with air inlet and gas outlet in described escaping gas processing means 1, described blower fan 2 is arranged
There are air inlet and gas outlet;
The gas outlet of described casting machine room 23 is connected by the air inlet of pipeline with escaping gas processing means 1, institute
The gas outlet stating escaping gas processing means 1 is connected by the air inlet of pipeline with blower fan 2, the gas outlet of described blower fan 2
It is connected with the air inlet of casting machine room 23.
Casting machine 24 and the air-suction cover 10 being arranged on casting machine 24 it is provided with in described casting machine room 23,
Being provided with gas outlet on described air-suction cover 10, the escaping gas that casting machine 24 is produced by described air-suction cover 10 sucks
In cover 10, described gas double purification device 4 is provided with air inlet and gas outlet, described drying tower 5 is provided with air inlet
And gas outlet;
The gas outlet of described air-suction cover 10 is connected with the air inlet of escaping gas processing means 1;Described volatility gas
Being additionally provided with gas double purification device 4 and drying tower 5 between body processing means 1 and blower fan 2, described escaping gas processes dress
Put and at the air inlet of 1, be provided with particle filtering net 18;
The gas outlet of described escaping gas processing means 1 is by the air inlet phase of pipeline with gas double purification device 4
Connecting, the gas outlet of described gas double purification device 4 is connected by the air inlet of pipeline with drying tower 5;
Particle filtering net 18, the gas outlet of described drying tower 5 and blower fan 2 it is provided with at the air inlet of described drying tower 5
Air inlet is connected.
Escaping gas processing cycle of the present invention uses the method that system carries out escaping gas process, and its feature exists
In comprising the following steps:
(1) escaping gas by pipeline by gas outlet and the escaping gas processing means 1 of the casting machine room 23 closed
Air inlet be connected, enter in escaping gas processing means 1 and process;
(2) escaping gas is after escaping gas processing means 1 processes, by going out of escaping gas processing means 1
QI KOU is connected by the air inlet of pipeline with blower fan 2, and described blower fan 2 relies on the mechanical energy of input to improve escaping gas pressure
Escaping gas after processing transfers out;
(4) gas outlet of described blower fan is connected with the air inlet of the casting machine room 23 of closing.
In step (1), between described escaping gas processing means 1 and blower fan 2, it is additionally provided with gas double purification device 4
With drying tower 5;It is provided with particle filtering net 18 at the air inlet of described escaping gas processing means 1;
The gas outlet of described escaping gas processing means 1 is connected by the air inlet of pipeline with drying tower 5, described dry
Escaping gas is processed by dry tower 5;It is provided with particle filtering net 18 at the air inlet of described drying tower 5;After described process
Escaping gas be connected with the air inlet of blower fan 2 via the gas outlet of drying tower 5, steam is absorbed by drying tower 5.
Described escaping gas processing means 1 includes that filter 19, low-temperature plasma processing means 13, photocatalyst process dress
Put 14, absorbent charcoal adsorber 15, vapour phase oxidation process processing means 16;Described filter 19, low-temperature plasma processing means 13,
Photocatalyst processing means 14, absorbent charcoal adsorber 15, vapour phase oxidation process processing means 16 are sequentially connected and connect;
The gas outlet of described air-suction cover 10 is connected with filter 19;
Impurity in escaping gas is stopped by described filter 19;
Escaping gas after described filter 19 filters enters described low-temperature plasma processing means 13, described low temperature etc.
Escaping gas is cracked by ion manipulation arrangement 13, under splitting action, macromolecular mass is decomposed into subset, i.e. by
Ozone oxidation carbon dioxide and water;
Described escaping gas after low-temperature plasma processing means 13 enters photocatalyst processing means 14, and described light touches
Matchmaker's processing means 14 carries out photodissociation cleansing phase to escaping gas, and escaping gas is by surpassing that photocatalyst processing means 14 produces
Negative oxygen ion and hydroxyl free radical are oxidizing to end product carbon dioxide and water;
As shown in Fig. 9 to Figure 13, described low-temperature plasma processing means 13 and photocatalyst processing means 14 integrally disposed in
In depurator casing 12;Being provided with air inlet and gas outlet on described depurator casing 12, described depurator casing 12 is by pipe
Road is sequentially connected connects with water curtain tower 6, drying tower 5;
Described low-temperature plasma processing means 13 includes that low-temperature plasma generator 1301 and low-temperature plasma generator are led
Rail 1304, described low-temperature plasma generator 1301 is arranged on low-temperature plasma generator guide rail 1304;
Described photocatalyst processing means 14 includes that ultraviolet ray photocatalyst generator 1401 and ultraviolet ray photocatalyst generator are led
Rail 1405, described ultraviolet ray photocatalyst generator 1401 is arranged on ultraviolet ray photocatalyst generator guide rail 1405;
One end of described depurator casing 12 is provided with low-temperature plasma generator power supply 1303 and ultraviolet ray photocatalyst is sent out
Raw device power supply 1403;Described low-temperature plasma generator power supply 1303 is by electric connection line and low-temperature plasma generator 1301 phase
Connect, provide electric energy to low-temperature plasma generator 1301;Described ultraviolet ray photocatalyst generator power 1403 is by electrical connection
Line is connected with ultraviolet ray photocatalyst generator 1401, provides electric energy to ultraviolet ray photocatalyst generator 1401.
Described depurator casing 12 is provided with air inlet, described air inlet near the outside of low-temperature plasma generator 1301
On be provided with primary filter net and homogenizing plate 1203;
Being provided with hermatic door 1202 on described depurator casing 12, the bottom of described depurator casing 12 is equipped with lower margin
1201;
Described depurator casing 12 is provided with gas outlet near the outside of ultraviolet ray photocatalyst generator 1401.
High-field electrode 1307, ground electrode 1305 it is provided with in described low-temperature plasma generator 1301, and equipped with stop
Medium 1306, is provided with discharging gap 1308 between high-field electrode 1307 and ground electrode 1305, high-field electrode 1307 with connect
Ground electrode 1305 is connected with plasma pulse power supply 1302 respectively by wire;
Described ultraviolet ray photocatalyst generator 1401 is provided with quartz burner 1402, sets in quartz burner 1402 periphery
It is equipped with photocatalyst net 1404.
Described escaping gas after photocatalyst processing means 14 enters absorbent charcoal adsorber 15, and described activated carbon is inhaled
Adsorption device 15 carries out adsorption treatment to escaping gas;
As shown in Figure 15 to Figure 19, described absorbent charcoal adsorber 15 carries out adsorption treatment to escaping gas;
Described absorbent charcoal adsorber 15 includes that activated carbon processes casing 1505.Described activated carbon processes casing 1505 and includes
Activated carbon drawer 1503, drawer rail 1515, quick clip 1504, drawer handle 1508, activated carbon 1511, intercept net 1506, enter
QI KOU labyrinth baffle plate 1512, labyrinth, gas outlet baffle plate 1507, cross flow proof dividing plate 1513, support keel 1514 and netted collet.
Be provided with activated carbon drawer 1503 on described drawer rail 1515, activated carbon drawer 1503 by quick clip 1504 with
Activated carbon processes casing 1505 and is fixedly connected.Netted collet, activated carbon drawer it is provided with bottom described activated carbon drawer 1503
1503 front portions are provided with drawer handle 1508.It is provided with activated carbon 1511 in described activated carbon drawer 1503.Described activated carbon
1511 is cylindrical particle activated carbon 1516.Activated carbon 1511 is a kind of porous carbon containing matter, and it has highly developed hole
Gap constructs, and the loose structure of activated carbon 1511 is provided for substantial amounts of surface area, can be fully contacted with gaseous impurity, thus compose
Give absorption property specific to activated carbon 1511 so that it is be very easy to reach to absorb the purpose collecting impurity.Such as magnetic force one
Sample, all has attractive interaction between all of molecule.Just because of this, the substantial amounts of molecule on activated carbon 1511 hole wall can produce
Raw powerful gravitation, thus reach the purpose being attracted in aperture by harmful impurity.
Described activated carbon drawer 1503 is 2 or more than 2.Described activated carbon processes the side of the air inlet of casing 1505
Being provided with obstruct net 1506 and air inlet labyrinth baffle plate 1512, the gas outlet processing casing 1505 at activated carbon is provided with gas outlet
Labyrinth baffle plate 1507.Described activated carbon processes bottom casing 1505 equipped with lower margin 1509;Described activated carbon processes casing
The one side of 1505 is provided with maintenance door 1510.
Described escaping gas after absorbent charcoal adsorber 15 enters vapour phase oxidation process processing means 16, by volatility
Organic molecule in gas is oxidized to carbon dioxide and water;
As shown in figure 14, described vapour phase oxidation process processing means includes spray column 1601, liquid medicine water storage box 1602 and water pump
1605, described water pump 1605 is provided with water inlet and water out.
The side of described spray column 1601 is provided with water pump 1605, and described liquid medicine water storage box 1602 is by pipeline and water pump
1605 water inlets are connected;Described water pump 1605 outlet is connected with spray column 1601 by pipeline, described spray column 1601
It is connected with the liquid medicine water storage box 1602 of its underpart by pipeline.
Described spray column 1601 bottom is provided with air inlet, and spray column 1601 top is provided with gas outlet.
Be provided with mouth spray 1609 on described spray column 1601 interior conduit, water pump 1605 water outlet pipeline is provided with into
Mouth of a river valve 1608.Be provided with bottom described spray column 7 circulation fluid outlet 1603, described circulation fluid outlet 1603 be provided with water outlet
The pipeline of mouth valve 1604 is connected;Described water outlet valve 1604 is connected with liquid medicine water storage box 1602.
Being provided with filler room 1610 in described spray column 1601, filler room 1610 is built with filler.Spray column 1601 bottom
Being provided with air inlet 1606, spray column 1601 top is provided with gas outlet 1606, is connected with clean aiutage by pipeline;In spray
Drench and bottom tower 1601, be provided with circulation fluid outlet 1603, have water outlet valve 1608 by Pipe installing, under spray column 1601 tower body
Portion is provided with liquid medicine water storage box 1602;Circulation fluid outlet 1603 is by water outlet valve 1604, outlet pipe and liquid medicine water storage box 1602
Connection;Water pump 1605 is arranged on spray column 1601 side, and water pump 1605 water inlet is connected with liquid medicine water storage box 1602 by pipeline
Logical, water pump 1605 outlet is connected into spray column 1601 top, the circulation fluid in spray column 1601 by circulation fluid pipeline 1607
It is provided with mouth spray on pipeline 1607, water pump 1605 exit circulation fluid pipeline 1607 is provided with water inlet valve 1608.
Dust in escaping gas is absorbed by described spray column 7, and superoxide anion is decomposed into rapidly oxygen;Institute
Stating aqueous escaping gas and enter drying tower 5, steam is absorbed by the honeycomb active carbon filter net being dried in tower 5.
The escaping gas of the closing of the present invention produces escaping gas processing system and the method thereof in region 3, easy to be easy
OK, reasonable in design, energy-conserving and environment-protective.
(1) escaping gas without sticky particle thing enters the low-temperature plasma process of escaping gas processing means 1
Device 13 and photocatalyst processing means 14 or vapour phase oxidation process processing means 16 or activated carbon adsorption unit 15, escaping gas divides
Son obtains carbon dioxide and water after treatment, it is ensured that escaping gas purification up to standard, reaches discharging standards;
(2) ability of the process of native system and processing method thereof exceedes country's secondary discharge standard, it is to avoid traditional work
Property carbon process the uncontrolled state of secondary pollution;
(3) gas after processing processes via gas double purification device 4, both can purify PM2.5, again can be clean
Ozone in activating QI body so that gas reaches the requirement that air recycles.
The ultimate principle of the present invention, principal character and advantages of the present invention have more than been shown and described.The technology of the industry
Personnel, it should be appreciated that the present invention is not restricted to the described embodiments, simply illustrating this described in above-described embodiment and description
The principle of invention, without departing from the spirit and scope of the present invention, the present invention also has various changes and modifications, the present invention
Claimed scope is defined by appending claims, description and equivalent thereof.