CN205481003U - Processing system is discharged in industrial waste's environmental protection - Google Patents
Processing system is discharged in industrial waste's environmental protection Download PDFInfo
- Publication number
- CN205481003U CN205481003U CN201620094323.6U CN201620094323U CN205481003U CN 205481003 U CN205481003 U CN 205481003U CN 201620094323 U CN201620094323 U CN 201620094323U CN 205481003 U CN205481003 U CN 205481003U
- Authority
- CN
- China
- Prior art keywords
- water
- inlet
- dust
- band
- air
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn - After Issue
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/30—Technologies for a more efficient combustion or heat usage
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model provides a processing system is discharged in industrial waste's environmental protection synthesizes combustion processing solid waste and liquid discarded object to carry out purification treatment to waste gas, the exhaust fume who produces among the combustion processes, finally innoxious completely, the effluent standard that accords with national standard GB18484 -2001 (" dangerous waste incineration pollution control standards "). System's operation is stable, the burning is thorough, the tail gas treatment is innoxious completely, can reduce the running cost by the effective control.
Description
Technical field
This utility model belongs to the environmental protection treatment technical field of trade waste, is specifically related to a kind of Industry Waste
The environment protection emission processing system of gurry.
Background technology
Along with the development of industrial economy, a large amount of industrial refuses cannot be processed in time, and industrial refuse is exhausted
Major part is solid-state castoff and two kinds of forms of liquid garbage, wherein contain substantial amounts of poisonous and harmful substance,
The heavy metals such as arsenic, copper, chromium, hydrargyrum, deal with improperly and will cause periphery soil property environment, atmospheric environment etc. no
Reversible destruction.
Utility model content
For solving above-mentioned technical problem, this utility model provides at the environment protection emission of a kind of trade waste
Reason system, comprehensive combustion processes solid waste, liquid debris, and gives up generation in combustion process
Gas, useless cigarette carry out purified treatment, the most innoxious, to meet GB GB18484-2001 (" dangerous
Incineration of waste Environmental capacity standard ") effluent standard.
For reaching above-mentioned purpose, the technical solution of the utility model is as follows: the environmental protection row of a kind of trade waste
Put processing system, it is characterised in that: include,
At least two pyrolysis gasification furnaces, every pyrolysis gasification furnace be each equipped with charging aperture, the first air inlet,
One water inlet, the first outlet flue and dust-exhausting port, the first air inlet of each pyrolysis gasification furnace is all by band air
The trachea of valve is connected to the first aerator, the first water inlet of each pyrolysis gasification furnace all by band water-supply valve and
The water pipe of water pump is connected to cistern, is provided with ash bucket with the dust-exhausting port of each pyrolysis gasification furnace connects；
Solid waste combustion furnace, it is configured with the first smoke inlet, the second outlet flue, the second air inlet, each described heat
The first outlet flue solving gasification furnace is all connected to the second smoke inlet of described solid waste combustion furnace, institute by pipeline
Stating the second outlet flue and be connected to the first air-introduced machine by the trachea of band air valve, the second air inlet is by band air
The trachea of valve is connected to the second aerator；
Incineration of liquor stove, incineration of liquor stove, it is configured with the 3rd air inlet, the second water inlet, the 3rd smoke
Mouth, the 6th smoke inlet and several inlets, the 6th smoke inlet is connected to by the trachea of band smoke valve
First outlet flue of one of them described pyrolysis gasification furnace, by trachea and the 3rd air inlet of band air cock
Connect is provided with the 3rd aerator, and the second water inlet is connected to described storage by the water pipe of band water valve and water pump
Pond, is provided with the second air-introduced machine, described feed liquor by what the trachea of band smoke valve and the 3rd outlet flue connected
Mouth is arranged in incineration of liquor stove on the sidewall of furnace bottom, and described 3rd outlet flue is arranged in incineration of liquor stove
On the sidewall of furnace roof, corresponding each inlet is each configured with a waste liquid spraying pay-off, institute
State waste liquid spraying pay-off and include fluid reservoir, the sewer pipe of band waste drains pump and ejector, sewer pipe
One end connects fluid reservoir, and its other end is connected with incineration of liquor stove by inlet, and described ejector is arranged
On the sewer pipe stretching into incineration of liquor furnace interior；Each described pyrolysis gasification furnace, solid waste combustion furnace and waste liquid
Burner it is equipped with in combustion furnace；
Flue gas heat-exchange unit, it is configured with the 3rd water inlet, the second smoke inlet, the 4th outlet flue, outlet,
3rd water inlet is connected to water tank by the water pipe of band water valve and water pump, and the second smoke inlet is by band smoke valve
Trachea be connected with the second outlet flue of solid waste combustion furnace, the 4th outlet flue is connected by the trachea of band air valve
To the 3rd air-introduced machine；
In chilling and absorption tower, it is configured with the 3rd smoke inlet, the 4th water inlet, alkali liquor import and the 5th go out
Mouth, the 4th outlet flue of described flue gas heat-exchange unit and the 3rd outlet flue of incineration of liquor stove are all by band cigarette
The trachea of air valve is connected to described 3rd smoke inlet, and the 3rd smoke inlet is arranged in tower body top, the 4th water inlet
Mouthful connect the most described cistern by the water pipe of band water valve and water pump, by the trachea of band smoke valve and the
What five outlet flues connected is provided with the 4th air-introduced machine, is connected with in chilling and absorption tower by the 4th water inlet
Being provided with the cooling water pipe of band spray pump, described cooling water pipe stretches in chilling and is provided with the one end in absorption tower
First high pressure nozzle, the first high pressure nozzle enters the flue dust instantaneous temperature reduction in chilling and in absorption tower after starting
To 200 DEG C, the alkali liquor being provided with band lye pump connected with in chilling and absorption tower by described alkali liquor import
Pipe, described alkali liquor pipe stretches in chilling and is provided with the second high pressure nozzle, the second high pressure with the one end in absorption tower
Nozzle is sprayed onto in chilling after starting and forms alkalescence water film with the alkali liquor moment on the inwall of absorption tower；
Bag-type dust collector, it is configured with dust-removing box, the 4th smoke inlet, ash discharging hole and the 6th outlet flue,
4th smoke inlet is arranged in dust-removing box on the sidewall of position, intermediate portion, and the 4th smoke inlet passes through deacidification
Absorption trachea is connected with the 5th outlet flue in chilling and absorption tower, and the 6th outlet flue is arranged in dust-removing box
Top, be provided with the 5th air-introduced machine by what the trachea of band smoke valve and the 6th outlet flue connected, described remove
Being provided with dedusting filtering bag in dirt casing, part stretches into the oscillating plate that is provided with in dust-removing box, and described oscillating plate is stretched
The position gone out outside dust-removing box is provided with vibrator；
Deacidification adsorbent equipment, it is arranged in chilling and between absorption tower and bag-type dust collector, and it includes disappearing
Calx storage tank, activated carbon storage tank；Slaked lime storage tank is connected with described deacidification absorption trachea by the first pipeline,
Described first pipeline is provided with the first blender, sprays stone by the first blender to deacidification absorption tracheal strips
Ash powder；Activated carbon storage tank is connected with described deacidification absorption trachea by second pipe, described second pipe
It is provided with the second blender, sprays activated carbon powder by the second blender to deacidification absorption tracheal strips；
Water circulation deacidification dedusting washing tower, it is configured with the 5th smoke inlet, clean gas exports, and the 5th smoke inlet is joined
Putting at the bottom of tower, the outlet of clean gas is arranged in tower top, the 5th smoke inlet by trachea and bag-type dust collector the
Six outlet flues connect；
And the chimney of the clean gas outlet with water circulation deacidification dedusting washing tower, it is provided with in described chimney
Line monitoring device, on-Line Monitor Device at least can be monitored in the clean flue gas discharged from chimney in real time
Sulfur dioxide concentration, nitrous oxides concentration, carbonomonoxide concentration, gas concentration lwevel, hydrogen cloride concentration,
Oxygen concentration, flue dust temperature, moisture content, pressure, flow velocity.
In a preferred embodiment of the present utility model, farther include described solid waste combustion furnace, incineration of liquor
Being equipped with temperature sensor and pressure transducer in stove and each pyrolysis gasification furnace, each waste liquid plastic-blasting feeding fills
It is equipped with effusion meter on the sewer pipe put, controls to connect each temperature sensor, pressure transducer, effusion meter
Be provided with controller, the force value VFC that controller feeds back according to solid waste combustion furnace pressure sensor
First air-introduced machine and the motor speed of the second aerator, controller passes according to incineration of liquor furnace pressure
Force value VFC second air-introduced machine of sensor feedback and the motor speed of the 3rd aerator, control
Device controls its interior burner, controller root according to the temperature value of temperature sensor feedback in solid waste combustion furnace
Controlling its interior burner according to the temperature value of incineration of liquor in-furnace temperature sensor feedback, controller is according to warm
The temperature value solving gasification in-furnace temperature sensor feedback controls its interior burner, and controller is according to effusion meter
The flow value of feedback controls to connect described ejector.
In a preferred embodiment of the present utility model, farther include described incineration of liquor stove and be configured with three
Inlet, corresponding three inlets are configured with three set waste liquid spraying pay-offs, and described pyrolysis gasification furnace is joined
It is equipped with three of independent operating.
In a preferred embodiment of the present utility model, farther include secondary in described solid waste combustion furnace and mend
Filling the 4th aerator that is provided with of air, the outlet of described 4th aerator is connected by the pipeline of band air cock
To the air inlet of solid waste combustion furnace, in described incineration of liquor stove, secondary supplement air is provided with the 5th air blast
Machine, the outlet of described 5th aerator is connected to the air inlet of incineration of liquor stove by the pipeline of band air cock.
In a preferred embodiment of the present utility model, farther include in described chilling and also set in absorption tower
Have atomizing tower body, be sequentially provided with in described aqueous vapor atomisation tower body the first baffle plate, second baffle, the 3rd
Baffle plate, fourth gear plate, fifth gear plate, described first baffle plate, second baffle, third gear plate exist along flue dust
Trend in atomizing tower body sets gradually, and three is all vertically arranged, and the top of the first baffle plate is fixed
On tower body sidewall, arranging at the bottom of the not contact tower of its bottom, the bottom of second baffle is fixed at the bottom of tower, its
Top does not contact tower top and arranges, and the top that third gear plate erects is fixed on tower body, at the bottom of the not contact tower of its bottom
Arranging, fourth gear plate and the equal horizontally set of fifth gear plate, both are separately fixed at two that tower body is oppositely arranged
On individual sidewall, and both other ends the most do not contact tower body and arrange.
In a preferred embodiment of the present utility model, farther include in described chilling and the bottom on absorption tower
Being additionally provided with leakage fluid dram, described leakage fluid dram is connected to a circulating water pool by the drain pipe of band water pump, described in follow
Ring pond is connected to alkali liquor pond by pipeline, and described alkali liquor pond is in alkali liquor to chilling and the alkali liquor on absorption tower
Import.
In a preferred embodiment of the present utility model, farther include the water pipe by band water pump and described storage
What pond connected is provided with a water softener, and the outlet of described water softener is connected with cistern by water pipe.
In a preferred embodiment of the present utility model, farther include described 4th smoke inlet, ash discharging hole and
6th outlet flue is separately positioned on the latter half of dust-removing box side, top and bottom, described dust cleaning case
The internal demarcation strip that is provided with, the space partition in dust-removing box is upper box and lower box by described demarcation strip,
Passage is offered at the center of described demarcation strip, and described dedusting filtering bag is fixed on demarcation strip, and its bag mouth pair
Quasi-passage is arranged, and the bag of described dedusting filtering bag is arranged in stretching into lower box.
In a preferred embodiment of the present utility model, in farther including described upper box, it is fixed on its cover plate
Inner side be provided with an injection tube, evenly spaced in described injection tube be provided with multiple winding-up mouth, described water spray
One end of pipe is stretched out casing and is extended laterally, and be fixed on described dust-removing box is provided with a pressure gas tank,
Described injection tube is stretched out one end that dust-removing box extends laterally and is communicated to pressure gas tank.
In a preferred embodiment of the present utility model, farther include described injection tube and be provided with electromagnetic pulse
Valve, described controller controls to connect electromagnetic impulse valve.
The beneficial effects of the utility model are: garbage environment protection emission system synthesis of the present utility model is burnt
Process solid waste and liquid debris, and the waste gas produced in combustion process, useless cigarette are purified
Process, the most innoxious, meet GB GB18484-2001 (" dangerous waste incineration Environmental capacity
Standard ") effluent standard.System run all right, burning thoroughly, vent gas treatment the most innoxious, energy
Enough effectively control reduces operating cost.
Accompanying drawing explanation
In order to be illustrated more clearly that the technical scheme in this utility model embodiment technology, below will be to enforcement
In the description of example technology, the required accompanying drawing used is briefly described, it should be apparent that, in describing below
Accompanying drawing is only embodiments more of the present utility model, for those of ordinary skill in the art, not
On the premise of paying creative work, it is also possible to obtain other accompanying drawing according to these accompanying drawings.
Fig. 1 is the structural representation of this utility model preferred embodiment；
Fig. 2 is the electrical control schematic of this utility model preferred embodiment.
Wherein, 2-pyrolysis gasification furnace, 21-charging aperture, 22-the first air inlet, 23-the first water inlet, 24-
First outlet flue, 25-dust-exhausting port, 26-the first aerator, 27-water-retention time, 28-temperature sensor, 29-
Pressure transducer, 30-controller, 31-water softener；
4-solid waste combustion furnace, 41-the first smoke inlet, 42-the second outlet flue, 43-the second air inlet, 44-
First air-introduced machine, 45-the second aerator, 46-burner, 47-the 4th aerator；
6-incineration of liquor stove, 61-the 3rd air inlet, 62-the second water inlet, 63-the 3rd outlet flue, 64-
Inlet, 65-the 3rd aerator, 66-the second air-introduced machine, 67-fluid reservoir, 68-ejector, 69-flow
Meter, 70-the 5th aerator, 71-the 6th smoke inlet；
8-flue gas heat-exchange unit, 81-the 3rd water inlet, 82-the second smoke inlet, 83-the 4th outlet flue, 84-
Outlet, 85-the 3rd air-introduced machine；
In 10-chilling and absorption tower, 101-the 3rd smoke inlet, 102-the 4th water inlet, 103-alkali liquor import,
104-the 5th outlet flue, 105-the 4th air-introduced machine, 106-the first high pressure nozzle, 107-the second high pressure nozzle,
108-the first baffle plate, 109-second baffle, 110-third gear plate, 111-fourth gear plate, 112-fifth gear
Plate, 113-leakage fluid dram, 114-circulating water pool, 115-alkali liquor pond；
12-bag-type dust collector, 121-dust-removing box, 121a-upper box, 121b-lower box, 122-
Four smoke inlets, 123-ash discharging hole, 124-the 6th outlet flue, 125-deacidification dust suction trachea, 126-the 5th draws
Blower fan, 127-dedusting filtering bag, 128-oscillating plate, 129-vibrator, 130-demarcation strip, 131-injection tube,
132-jets mouth, 133-pressure gas tank, 134-electromagnetic impulse valve；
14-deacidification adsorbent equipment, 141-slaked lime storage tank, 142-activated carbon storage tank, 143-the first blender,
144-the second blender；
16-water circulation deacidification dedusting washing tower, 161-the 5th smoke inlet, the clean gas of 162-exports；
18-chimney, 20-on-line measuring device.
Detailed description of the invention
Below in conjunction with the accompanying drawing in this utility model embodiment, to the technology in this utility model embodiment
Scheme is clearly and completely described, it is clear that described embodiment is only this utility model one
Divide embodiment rather than whole embodiments.Based on the embodiment in this utility model, this area is common
The every other embodiment that technical staff is obtained under not making creative work premise, broadly falls into this
The scope of utility model protection.
Embodiment
As shown in Figure 1, 2, the present embodiment discloses a kind of integrated treatment solid-state industries garbage and liquid
The system of trade waste, the final discharge of harmless environmental protection in a gaseous form after native system processes.
Tail gas clean-up is shared during liquid-state industrial garbage of the present utility model and solid-state industries offal treatment
System.
Process solid-state industries garbage time have pyrolysis gasification furnace 2, solid waste combustion furnace 4, flue gas heat-exchange unit 8,
In chilling and absorption tower 10, deacidification adsorbent equipment 14, bag-type dust collector 12, water circulation deacidification dedusting are washed
Wash tower 16 and chimney 18.
Solid waste first combustion and pyrolysis gasification under anoxia condition in pyrolysis gasification furnace 2, spent useless
The garbage of filling is progressively dried in stove, cracks, burns and after-flame by the heat energy of gurry release,
Final pyrolytic gasification produces fuel gas, in fuel gas enters solid waste combustion furnace 4 subsequently, with the most pre-
The air of heat carries out mixed combustion, by control temperature in solid waste combustion furnace 4 1100 DEG C～1150 DEG C it
Between, it is possible to effectively control the generation of two English；By pyrolysis gasification furnace 2 and the burning of solid waste combustion furnace 4
Coordinate and waste combustion is changed into CO2And various corresponding sour gas, burning is thoroughly；
The waste gas, the flue dust that produce after burning enter flue gas heat-exchange unit 8, exchange radiating and cooling, produce simultaneously and can return
Receive the saturated vapor utilized；
In chilling and absorption tower 10, by controlling the working environment in absorption tower, it is possible to effectively contain two
The synthesis again of English, carries out first once neutralize deacidification, dust removal process to useless cigarette, waste gas simultaneously, it is possible to
Neutralize the sour gas removing 40%～about 50%；
Neutralize the waste gas after deacidification, dust removal process for the first time, useless cigarette enters bag-type dust collector 12 before to it
Carrying out spraying pulverized limestone and activated carbon, on the one hand pulverized limestone carries out second time neutralize deacidification to useless cigarette, waste gas,
Activated carbon carries out the absorption of heavy metal adsorption and PCDDS/PCDFS to useless cigarette, waste gas；The most right
Waste gas, useless tobacco powder networking, deposit on bag wall through bag-type dust collector, form powder net, unreacted
Absorbent continue to neutralize gaseous acid material and Adsorption of Heavy Metals in useless cigarette, waste gas, improve absorption,
Deacidification effect；
Flue dust after absorption and secondary deacidification process enters bag-type dust collector 12, carries out final dusting process,
The flue dust of 85%～90% can be removed；Separately, the bag-type dust collector optimizing design is configured with automatic ash removing function,
The service life of dust removing effects and cloth bag can be improved；
Flue gas after final dusting enters water circulation deacidification dedusting washing tower 16, carries out three deacidifications, removes for three times
Dirt so that the gas of discharge is the most innoxious from chimney, it is (" dangerous to meet GB GB18484-2001
Incineration of waste Environmental capacity standard ") effluent standard；On-Line Monitor Device is directly networked Environmental Protection Agency, real
Time monitoring from chimney, discharge the composition of gas, concentration and flow, temperature etc..
Have in incineration of liquor stove 6, chilling when processing liquid industrial waste gas thing and absorption tower 10, deacidification absorption
Device 14, bag-type dust collector 12, water circulation deacidification dedusting washing tower 16 and chimney 18.
In incineration of liquor stove 6, complete the high-temp combustion of waste liquid, burning with the waste liquid of steam fog shape injection
The flue gas that High Temperature Rotating rises it is fully contacted in stove, the heated evaporation of the moisture in waste liquid, exhausted in waste liquid
Major part poisonous and harmful substance burn the most completely, after-flame generation volume of smoke, CO2 and various
Corresponding sour gas, by adjusting the burning situation in combustor, it is ensured that completely while burning effectively
Control the generation of two English.
Waste gas, flue dust that waste liquid produces after thoroughly burning in incineration of liquor stove 6 enter in chilling and absorb
Tower 10, carries out first once neutralize deacidification, dust removal process to useless cigarette, waste gas, it is possible to neutralizes and removes 40%～50%
The sour gas of left and right；Simultaneously by controlling the working environment in absorption tower, it is possible to effectively contain two
The synthesis again of English, the flue gas owing to producing after incineration of liquor has the high characteristic Han halogen, this utility model
Liquid garbage after burning disposal, do not enter flue gas heat-exchange unit 8 and be directly entered incineration of liquor system
Water heater carries out heat exchange, and the flue gas after heat exchange enters in chilling and absorption tower 10, and in water heater, heat exchange is produced
Raw hot water enters the 3rd water inlet 81 of flue gas heat-exchange unit 8, uses as supplementary hot water, recycles,
Reduce system operation cost.
Flue dust after absorption and secondary deacidification process enters bag-type dust collector 12, carries out at final dusting
Reason, it is possible to remove the flue dust of 85%～90%；Separately, the bag-type dust collector optimizing design is configured with automatic ash removing
Function, it is possible to increase dust removing effects and the service life of cloth bag；
Flue gas after final dusting enters water circulation deacidification dedusting washing tower 8, carries out three deacidifications, removes for three times
Dirt so that the gas of discharge meets (" the dangerous waste incineration pollution of GB GB18484-2001 from chimney
Control standard ") effluent standard；On-Line Monitor Device is directly networked Environmental Protection Agency, and monitoring is from chimney in real time
Composition, concentration and flow, the temperature etc. of middle discharge gas.
Concrete:
One, the combustion process of solid-state castoff: pyrolysis gasification furnace 2 and solid waste combustion furnace 4
Pyrolysis gasification furnace 2 of the present utility model have can three of independent operating, respectively A stove, B stove,
C stove, every pyrolysis gasification furnace 2 be each equipped with charging aperture the 21, first air inlet the 22, first water inlet 23,
First outlet flue 24 and dust-exhausting port 25, the first air inlet 22 of each pyrolysis gasification furnace 2 is all by band air
The trachea of valve is connected to the first aerator 26, and the first water inlet 23 of each pyrolysis gasification furnace 2 is all by bringing
The water pipe of water valve and water pump is connected to cistern 27, with setting that the dust-exhausting port 25 of each pyrolysis gasification furnace 2 connects
There is ash bucket；
Solid waste combustion furnace 4, it is configured with first smoke inlet the 41, second outlet flue the 42, second air inlet 43,
First outlet flue 24 of each described pyrolysis gasification furnace 2 is all connected to described solid waste combustion furnace 4 by pipeline
Second smoke inlet 41, described second outlet flue 42 is connected to the first air-introduced machine 44 by the trachea of band air valve,
Second air inlet 43 is connected to the second aerator 45, each described pyrolysis gasification furnace by the trachea of band air cock
2 and solid waste combustion furnace in be equipped with burner 46.
First garbage puts into pyrolysis gasification furnace 2, meanwhile starts the burner 46 in solid waste combustion furnace 4,
The design temperature of 1100 DEG C, the combustion in subsequent start-up pyrolysis gasification furnace 2 will be warming up in solid waste combustion furnace 4
Burner 46, ignition garbage, in pyrolysis gasification furnace 2, only supply oxygen amount by the first aerator 26
Having the air of oxygen amount 20%～30% needed for the stoichiometry of burning, in pyrolysis gasification furnace 2, garbage lacks
The combustion and pyrolysis gasification of oxygen environment, the long strand of various compounds is progressively broken and becomes short molecular chain,
Becoming fuel gas, the Main Ingredients and Appearance of fuel gas is: N2, H2, CH4, C2H6, C6H8, CO and wave
The property sent out sulfur, flammable chlorine etc., in fuel gas enters solid waste combustion furnace 4 subsequently, with the sky preheated in advance
Gas carries out mixed combustion, and burn in the whole combustion process in solid waste combustion furnace 4 is gaseous material,
The flue gas time of staying in solid waste combustion furnace 4 produced is more than 2s, in such a case, and the overwhelming majority
Toxic and harmful is entirely destroyed and changes into CO2 and various corresponding sour gas, such as polyethylene, chlorine
Compound etc..Start in the first air-introduced machine 44 makes solid waste combustion furnace 4 and form tiny structure environment, guide flammable
Gas enters in solid waste combustion furnace 4, and the flue gas produced after burning in solid waste combustion furnace 4 is from the second outlet flue
42 discharge, and send into and discharge after follow-up exhaust gas purification system processes.This utility model is fired by control
Burn the temperature in stove 4 all the time between 1100 DEG C～1150 DEG C, it is possible to effectively control the generation of two English；Logical
Cross the burning of pyrolysis gasification furnace 2 and solid waste combustion furnace 4 to coordinate waste combustion changes into CO2 and various
Corresponding sour gas, burning is thoroughly.
Meanwhile, after three pyrolysis gasification furnaces 2 are set, in system operation, first garbage is put into A
In stove, during the burning of A furnace igniting, garbage is put into B stove, treats that A stove organic matter in garbage tends to
When 1～3%, journey can by color state time, B stove has fed intake complete the most, start igniting, the initial stage, A stove participate in can
In combustion gas body just can make solid waste combustion furnace 4 plus the initial amount of vaporization of B stove, temperature maintains all the time
The combustible gas scale of construction required during the nature of about 1110 DEG C, during the burning of B furnace igniting, throws garbage
Entering C stove, A stove carries out deashing process, with each pyrolysis gasification furnace of this alternate run 2, it is ensured that burning is uninterrupted,
The disposal ability of raising equipment, in controlling solid waste combustion furnace 4, temperature maintains between 1110 DEG C all the time simultaneously,
It is beneficial to contain the generation of two English.
Two, the combustion process of liquid garbage: incineration of liquor stove 6
Incineration of liquor stove 6, its be configured with the 3rd air inlet the 61, second water inlet the 62, the 3rd outlet flue 63,
6th smoke inlet 71 and three inlets 64, the 6th smoke inlet 71 is connected by the trachea of band smoke valve
To the first outlet flue 24 of one of them pyrolysis gasification furnace 2, by trachea and the 3rd air inlet of band air cock
What mouth 61 connected is provided with the 3rd aerator 65, and the second water inlet 62 is by the water pipe of band water valve and water pump even
It is connected to described cistern 27, second is drawn by being provided with of connecting of the trachea of band smoke valve and the 3rd outlet flue 63
Blower fan 66, described inlet 64 is arranged in incineration of liquor stove 6 on the sidewall of furnace bottom, and the described 3rd goes out
Mouth 63 is arranged in incineration of liquor stove 6 on the sidewall of furnace roof, and corresponding each inlet 64 is joined respectively
Being equipped with a waste liquid spraying pay-off, described waste liquid spraying pay-off includes fluid reservoir 67, band waste liquid
The sewer pipe of pump and ejector 68, sewer pipe one end connects fluid reservoir 67, and its other end passes through feed liquor
Mouth 64 connects with incineration of liquor stove 6, and described ejector 68 is arranged on and stretches within incineration of liquor stove 6
On sewer pipe；It is equipped with burner 46 in each pyrolysis gasification furnace 6.
First starting burner 46, heat up preheating incineration of liquor stove 6, when in-furnace temperature rises to 650 DEG C,
Starting waste liquid spraying pay-off, waste liquid is forced with in-furnace temperature time in steam fog shape injection to incineration of liquor stove 6
Nearly about 1150 DEG C, in incineration of liquor stove 6, supplied the change of oxygen amount only burning by the 3rd aerator 65
Learning the air of First Astronautic Research Institute for Measurement and Test's oxygen demand 20%～30%, steam fog shape waste liquid is fully contacted high temperature in incineration of liquor stove 6
Rotate the flue gas risen, the water-sealing high temperature evaporation in waste liquid, the most poisonous and harmful substances in waste liquid
Burning the most completely, after-flame produce volume of smoke, CO2 and various corresponding sour gas,
Discharge from the 3rd outlet flue 63 under the suction of the second air-introduced machine 66 eventually.By reasonable Arrangement inlet
64 and the 3rd position of outlet flue 63, the i.e. the 3rd outlet flue 63 is arranged in incineration of liquor stove 6 near furnace roof
Sidewall, inlet 64 is arranged in the incineration of liquor stove 6 sidewall near furnace bottom, makes the Gas phase Smoke after burning
Flow in incineration of liquor stove 6 with reverse compared with waste liquid, improve the heat utilization efficiency of incineration of liquor stove 6.
Separately, this utility model is by controlling the temperature of the interior burning of incineration of liquor stove 6 all the time at 1100 DEG C～1150 DEG C
Between, it is possible to effectively control the generation of two English, spray by arranging three inlets 64 and supporting waste liquid
Mist pay-off, alternately starts or starts simultaneously waste liquid spraying pay-off, it is ensured that burning is uninterruptedly entered
OK, the disposal ability of system is improved.
Separately, this utility model in order to reduce operating cost, incineration of liquor stove 6 by the 6th smoke inlet 71 with
First outlet flue 24 of one of them pyrolysis gasification furnace 2 connects, and produces in pyrolysis gasification furnace 2 combustion process
High heat flue gas enter in incineration of liquor stove 6, the burning of heating of waste liquid in incineration of liquor stove 6,
Reduce the usage amount of fuel when incineration of liquor stove 6 burns, it is possible to save the fuel cost of 30%～50%.
Three, flue gas heat-exchange unit 8
Flue gas heat-exchange unit 8, its be configured with the 3rd water inlet the 81, second smoke inlet the 82, the 4th outlet flue 83,
Outlet 84, the 3rd water inlet 81 is connected to water tank by the water pipe of band water valve and water pump, the second smoke inlet
82 are connected with the second outlet flue 42 of solid waste combustion furnace 4 by the trachea of band smoke valve, the 4th outlet flue
83 are connected to the 3rd air-introduced machine 85 by the trachea of band air valve.
The flue gas produced after mixed combustion in solid waste combustion furnace 4 enters flue gas heat-exchange unit 8 and swaps heat radiation fall
Temperature, produces the saturated vapor that can recycle, and reduces the thermic load of subsequent technique simultaneously, adjusts in chilling
Technological parameter with absorption tower 10.
Four, in chilling and absorption tower 10
In chilling and absorption tower 10, it is configured with the 3rd smoke inlet the 101, the 4th water inlet 102, alkali liquor enters
Mouth 103 and the 5th outlet flue 104, the 4th outlet flue 83 of described flue gas heat-exchange unit 8 and incineration of liquor stove
3rd outlet flue 63 of 6 is all connected to described 3rd smoke inlet 101 by the trachea of band smoke valve, and the 3rd
Smoke inlet 101 is arranged in tower body top, and the 4th water inlet 102 is connected by the water pipe of band water valve and water pump
The most described cistern 27, is provided with the 4th by what the trachea of band smoke valve and the 5th outlet flue 104 connected
Air-introduced machine 105, is provided with band spray pump by what the 4th water inlet 102 connected with in chilling and absorption tower 10
Cooling water pipe, described cooling water pipe stretches in chilling and one end in absorption tower 10 is provided with the first high pressure spray
Mouth 106, the first high pressure nozzle 106 enters the flue dust instantaneous temperature reduction in chilling and in absorption tower 10 after starting
To 200 DEG C, the alkali liquor being provided with band lye pump connected with in chilling and absorption tower by described alkali liquor import
Pipe, described alkali liquor pipe stretches into and is provided with the second high pressure nozzle 107 in chilling with the one end in absorption tower, and second is high
Pressure nozzle 107 is sprayed onto in chilling after starting and forms alkalescence water film with the alkali liquor moment on the inwall of absorption tower.
The flue dust that high temperature incineration produces can the most synthetically produced two when high temperature is reduced between 250 DEG C～500 DEG C
English, in order to contain the synthesis again of two English, this utility model passes through the first high pressure nozzle 106 to urgency
Injection high-pressure cooling water in cold neutralization absorption tower 10, will enter in chilling and exist with temperature in absorption tower 10
In the flue dust 1S of about 500 DEG C, rapid cooling is to 200 DEG C, can effectively contain two English again with this
Synthesis；Tangentially it is sprayed onto suitable for alkali liquor in chilling and absorption tower by the second high pressure nozzle 107 after rapid cooling
On 10 inwalls, forming the alkaline water film that one layer of rotation flows downward on inwall, alkalescence water film is at stream
Neutralize sour gas during Dong, neutralize deacidification；Grit is separated by centrifugal action simultaneously, throws to
Tower body inwall, is adsorbed by alkalescence water film, flows to bottom with water and discharges, it is achieved waste gas, useless cigarette de-
Acid dedusting.
Flue dust water capacity after chilling, deacidification is high, in order to ensure that flue dust can enter back segment bag-type dust dress
Put 12 and carry out further dedusting, need to after chilling, deacidification flue dust carry out atomization water-removing, this reality
It is additionally provided with atomizing tower body, with to the high humidity after chilling, deacidification with in novel chilling and absorption tower 10
Flue dust carries out atomization water-removing, is sequentially provided with the first baffle plate 108, second baffle in described aqueous vapor atomisation tower body
109, third gear plate 110, fourth gear plate 111, fifth gear plate 112, described first baffle plate 108, second
Baffle plate 109, third gear plate 110 set gradually along flue dust trend in atomizing tower body, and three is equal
Being vertically arranged, the top of the first baffle plate 108 is fixed on tower body sidewall, arranges at the bottom of the not contact tower of its bottom,
The bottom of second baffle 109 is fixed at the bottom of tower, and its top does not contact tower top and arranges, third gear plate 110
Perpendicular top is fixed on tower body, arranges, fourth gear plate 111 and fifth gear plate at the bottom of the not contact tower of its bottom
112 equal horizontally sets, both are separately fixed on two sidewalls that tower body is oppositely arranged, and both another
End does not the most contact tower body and arranges.By arranging baffle plate in tower body, on the one hand it is mingled with the flue gas stream of steam
Colliding on baffle plate, make atomizing by physical impacts, on the other hand being separated by the obstruct of baffle plate will
The little flue gas above of density is discharged, and density is positioned at greatly the grit of lower section, water will not by baffle
With flue gas, further function as dedusting, effect except water.
Five, bag-type dust collector 12
Bag-type dust collector 12, it is configured with dust-removing box 121, the 4th smoke inlet 122, ash discharging hole 123
With the 6th outlet flue 124, the 4th smoke inlet 122 is arranged in the dust-removing box 121 side near position, intermediate portion
On wall, the 4th smoke inlet 122 goes out by the 5th of in deacidification absorption trachea 125 and chilling and absorption tower 10 the
Mouth 104 connects, and the 6th outlet flue 124 is arranged in the top of dust-removing box 121, by band smoke valve
Trachea and the 6th outlet flue 124 connect be provided with the 5th air-introduced machine 126, set in described dust-removing box 121
Having a dedusting filtering bag 127, part stretches into and is provided with oscillating plate 128, described oscillating plate 128 in dust-removing box 121
Stretch out the position outside dust-removing box 121 and be provided with vibrator 129.
Start in the 5th air-introduced machine 126 makes dust-removing box 121 and form subnormal ambient, at band subnormal ambient
In dust-removing box 121, dust and gas enters dedusting filtering bag 127 from the 4th smoke inlet 122, and dedusting filtering bag 127 is to dirt
Gas carry out dirt, edema caused by disorder of QI from, the gas after separation is discharged from the 6th outlet flue 124, enter industrial waste
The back segment operation that thing processes, the dust after separation discharges from ash discharging hole 123, the dedusting of funnel-shaped structure
Casing 121 is beneficial to discharge so that the dust after separating enters ash discharging hole 123, can filter by adjusting dedusting
The mesh number of bag 127 controls to discharge the standard of gas from the 6th outlet flue 124, and of the present utility model the
The specific position design of four smoke inlets 122, ash discharging hole 123 and the 6th outlet flue 124, the i.e. the 6th outlet flue
124 tops being arranged on dust-removing box 121, ash discharging hole 123 is arranged on the lower curtate of dust-removing box 121, the
Four smoke inlets 122 are arranged on the latter half of dust-removing box 121 side so that gas is at dust-removing box 121
Interior stroke is the longest, and the filter dirt effect of gas is more preferable, improves dust removing effects.
Dedusting filtering bag 127 works after a period of time, and dust easily blocks the mesh of dedusting filtering bag 127, mesh
Block and form a barrier to mesh time to a certain degree itself, limit gas and pass, cause dust arrester
Dedusting fault, now Vibration on Start-up device 129, oscillating plate 128 is along with vibration, vibration processes shake dedusting filter
Bag 127, shakes off absorption dust on dedusting filtering bag 127, it is to avoid dust blocking filter opening, forms this since then
The automatic ash removing function of utility model bag-type dust collector 12.
As further improvement of the utility model, in described dust-removing box 121, it is provided with a demarcation strip 130,
Space partition in dust-removing box 121 is upper box 121a and lower box 121b by described demarcation strip 130,
Passage is offered at the center of described demarcation strip 130, and described dedusting filtering bag 127 is fixed on demarcation strip 130,
And its bag mouth alignment passage is arranged, the bag of described dedusting filtering bag 127 stretches in lower box 121b.Increase
Adding after dust-removing box 121 cuts off by demarcation strip 130, the passage on demarcation strip 130 is from the 6th smoke
Mouthfuls 124 discharge must through position, and by dedusting filtering bag 127 be isolated in outer dust be not likely to enter logical
Pore and from the 6th outlet flue 124 discharge, further increase dust removing effects.
In order to further optimize the automatic ash removing function of bag-type dust collector 12, in described upper box 121a
Be fixed on the injection tube 131 that is provided with inside its cover plate, in described injection tube 131 evenly spaced be provided with many
Individual winding-up mouth 132, one end of described injection tube 131 is stretched out dust-removing box 121 and is extended laterally, is fixed on
Being provided with a pressure gas tank 133 on described dust-removing box 121, described injection tube 131 stretches out dust-removing box
121 one end extended laterally are communicated to pressure gas tank 133.By injection tube 131 to dedusting filtering bag 127
Dedusting filtering bag 127 is cleaned by blowing pressurized air, in order to avoid dust arrester is when dedusting filtering bag 127 is long
Between the fault that causes because of dust blocking mesh when working.In the preferred described injection tube 131 of this utility model
Being provided with electromagnetic impulse valve 134, controller 30 controls to connect described electromagnetic impulse valve 134, passes through controller
30 control electromagnetic impulse valves 134 timing or Pulse Width Control is opened, it is achieved dedusting filtering bag 127 automatically clear
Sweeping, it is not necessary to manually participate in, wherein, controller 30 can also adjust pulse width, interpulse by controlling
Every and the mode of period distances control the effect that cleans.
Six, deacidification adsorbent equipment 14
It is arranged in chilling between absorption tower 10 and bag-type dust collector 12, and it includes slaked lime storage tank
141, activated carbon storage tank 142；Slaked lime storage tank 141 adsorbs trachea 125 by the first pipeline with described deacidification
Connecting, described first pipeline is provided with the first blender 143, is adsorbed to deacidification by the first blender 143
Lime powder is sprayed in trachea 125；Activated carbon storage tank 141 is by second pipe and described deacidification adsorbed gas
Pipe 125 connects, and described second pipe is provided with the second blender 144, by the second blender 144 to de-
Activated carbon powder is sprayed in acid absorption trachea 125.
Useless cigarette after in chilling and absorption tower 10 processes, waste gas enter before bag-type dust collector 12 based on
It is carried out spraying pulverized limestone and activated carbon by deacidification adsorbent equipment 14, and on the one hand pulverized limestone is to useless cigarette, waste gas
Carrying out second time and neutralize deacidification, activated carbon carries out heavy metal adsorption and PCDDS/PCDFS to useless cigarette, waste gas
Absorption；On the other hand to waste gas, useless tobacco powder networking, heavy on bag wall when bag-type dust collector 12
Long-pending, form powder net, unreacted absorbent continues to neutralize gaseous acid material and suction in useless cigarette, waste gas
Attached heavy metal, improves absorption, deacidification effect.
Seven, water circulation deacidification dedusting washing tower 16
It is configured with the 5th smoke inlet 161, clean gas outlet 162, and the 5th smoke inlet 161 is arranged at the bottom of tower,
Clean gas outlet 162 is arranged in tower top, the 5th smoke inlet 161 by trachea and bag-type dust collector 12 the
Six outlet flues 124 connect.In water circulation deacidification dedusting washing tower 16, flue gas is carried out last water elution
Acid, dust removal process, final clean gas environment protection emission from chimney 18, it is provided with on-line checking dress in chimney 18
Put 20, in real time monitoring from chimney the sulfur dioxide concentration in the clean flue gas of discharge, nitrous oxides concentration,
Carbonomonoxide concentration, gas concentration lwevel, hydrogen cloride concentration, oxygen concentration, flue dust temperature, moisture content,
Pressure, flow velocity.
As further improvement of the utility model, described solid waste combustion furnace 2, incineration of liquor stove 6 and each
Temperature sensor 28 and pressure transducer 29, each waste liquid plastic-blasting pay-off it is equipped with in pyrolysis gasification furnace 2
Sewer pipe on be equipped with effusion meter 69, controller 30 controls to connect each temperature sensor 28, pressure passes
Sensor 29, effusion meter 69, the pressure that controller 30 feeds back according to solid waste combustion furnace 2 pressure sensor 29
The motor speed of both force value VFC the first air-introduced machine 44 and the second aerator 45, controller 30
Force value VFC the second air-introduced machine 66 and the according to incineration of liquor stove 6 pressure sensor 29 feedback
The motor speed of both three aerators 65.Whole system of the present utility model is a normal pressure system, passes through
Controller 30 controls the first air-introduced machine the 44, second aerator the 45, second air-introduced machine 66 and the 3rd aerator
The rotating speed of 65 4 motors controls the air capacity of whole system, it is ensured that system stable operation.
It is interior that controller 30 controls it according to the temperature value of temperature sensor 28 feedback in solid waste combustion furnace 4
Burner 46, controller 30 controls according to the temperature value of temperature sensor 28 feedback in incineration of liquor stove 6
Its interior burner 46, controller 30 is according to the temperature of temperature sensor 28 feedback in pyrolysis gasification furnace 2
Value controls its interior burner 46.The temperature that when system is run, controller 30 feeds back according to temperature sensor 28
Angle value control connection burner 46 guarantees that the ignition temperature in solid waste combustion furnace 4 is all the time at 1100 DEG C
～between 1150 DEG C, effectively controlling the generation of two English, system runs the temperature in time control pyrolysis gasification furnace 2
Degree is all the time between 600 DEG C～800 DEG C, it is ensured that the thorough burning of garbage.Controller 30 when system is run
Control its interior burner 46 according to the temperature value of temperature sensor 28 feedback in incineration of liquor stove 6 to guarantee
Temperature in incineration of liquor stove 6, all the time between 1100 DEG C～1150 DEG C, effectively controls the generation of two English.
Controller 30 controls to connect described ejector 68 according to the flow value that effusion meter 69 feeds back.Waste liquid amount is just
Reason condition bottom sprays into continuously, when the flow value of effusion meter 69 feedback is less or waste liquid does not concentrates, controls
Device 30 controls ejector 68 and is interrupted hydrojet, to maintain stablizing of temperature in incineration of liquor stove 6.
In described solid waste combustion furnace 4, secondary supplement air is provided with the 4th aerator 47, described 4th drum
The outlet of blower fan 47 is connected to the air inlet of solid waste combustion furnace 4 by the pipeline of band air cock, to described useless
In liquid combustion furnace 6, secondary supplement air is provided with the 5th aerator 70, the outlet of described 5th aerator 70
The air inlet of incineration of liquor stove it is connected to by the pipeline of band air cock.It is provided by controller 30 to control
5th aerator 70 of wind supply quantity so that incineration of liquor stove 6 interior-heat right property gas rotating burns, improves cigarette
The gas time of staying, it is ensured that waste liquid thoroughly burns.It is provided by controller 30 and controls the 4th drum of wind supply quantity
Blower fan 47 so that interior-heat right property gas rotating in solid waste combustion furnace 4 burns, improves gas residence time, really
Protect waste liquid thoroughly to burn.
The bottom in described chilling and absorption tower 10 is additionally provided with leakage fluid dram 113, and described leakage fluid dram 113 is by band
The drain pipe of water pump is connected to a circulating water pool 114, and described circulating water pool 114 is connected to alkali liquor by pipeline
Pond 115, described alkali liquor pond 115 is for the alkali liquor import 103 of alkali liquor in chilling and absorption tower 10, in urgency
In cold neutralization absorption tower 10, the unevaporated alkali liquor of part discharges Posterior circle use, reduces equipment operating cost.
In order to avoid the furnace wall fouling of pyrolysis gasification furnace 2, solid waste combustion furnace 4 and incineration of liquor stove 6, and
Avoid in chilling and the tower wall fouling on absorption tower 10, by the water pipe of band water pump with described cistern 27 even
Connect is provided with a water softener 31, and the outlet of described water softener 31 is connected with cistern 27 by water pipe.
Described above to the disclosed embodiments, makes professional and technical personnel in the field be capable of or uses
This utility model.Multiple amendment to these embodiments will be aobvious for those skilled in the art
And be clear to, generic principles defined herein can be without departing from spirit or scope of the present utility model
In the case of, realize in other embodiments.Therefore, this utility model is not intended to be limited to institute herein
These embodiments shown, and it is to fit to consistent with principles disclosed herein and features of novelty the widest
Scope.
Claims (10)
1. the environment protection emission processing system of a trade waste, it is characterised in that: include,
At least two pyrolysis gasification furnaces, every pyrolysis gasification furnace is each equipped with charging aperture, the first air inlet, the first water inlet, the first outlet flue and dust-exhausting port, first air inlet of each pyrolysis gasification furnace is all connected to the first aerator by the trachea of band air cock, first water inlet of each pyrolysis gasification furnace is all connected to cistern by the water pipe of band water-supply valve and water pump, is provided with ash bucket with the dust-exhausting port of each pyrolysis gasification furnace connects；
Solid waste combustion furnace, it is configured with the first smoke inlet, the second outlet flue, the second air inlet, first outlet flue of each described pyrolysis gasification furnace is all connected to the second smoke inlet of described solid waste combustion furnace by pipeline, described second outlet flue is connected to the first air-introduced machine by the trachea of band air valve, and the second air inlet is connected to the second aerator by the trachea of band air cock；
nullIncineration of liquor stove，It is configured with the 3rd air inlet、Second water inlet、3rd outlet flue、6th smoke inlet and several inlets，6th smoke inlet is connected to the first outlet flue of one of them described pyrolysis gasification furnace by the trachea of band smoke valve，It is provided with the 3rd aerator by what the trachea of band air cock and the 3rd air inlet connected，Second water inlet is connected to described cistern by the water pipe of band water valve and water pump，It is provided with the second air-introduced machine by what the trachea of band smoke valve and the 3rd outlet flue connected，Described inlet is arranged in incineration of liquor stove on the sidewall of furnace bottom，Described 3rd outlet flue is arranged in incineration of liquor stove on the sidewall of furnace roof，Corresponding each inlet is each configured with a waste liquid spraying pay-off，Described waste liquid spraying pay-off includes fluid reservoir、Sewer pipe with waste drains pump、And ejector，Sewer pipe one end connects fluid reservoir，Its other end is connected with incineration of liquor stove by inlet，Described ejector is arranged on the sewer pipe stretching into incineration of liquor furnace interior；It is equipped with burner in each described pyrolysis gasification furnace, solid waste combustion furnace and incineration of liquor stove；
Flue gas heat-exchange unit, it is configured with the 3rd water inlet, the second smoke inlet, the 4th outlet flue, outlet, 3rd water inlet is connected to water tank by the water pipe of band water valve and water pump, second smoke inlet is connected with the second outlet flue of solid waste combustion furnace by the trachea of band smoke valve, and the 4th outlet flue is connected to the 3rd air-introduced machine by the trachea of band air valve；
nullIn chilling and absorption tower，It is configured with the 3rd smoke inlet、4th water inlet、Alkali liquor import and the 5th outlet flue，4th outlet flue of described flue gas heat-exchange unit and the 3rd outlet flue of incineration of liquor stove are all connected to described 3rd smoke inlet by the trachea of band smoke valve，3rd smoke inlet is arranged in tower body top，4th water inlet connects the most described cistern by the water pipe of band water valve and water pump，It is provided with the 4th air-introduced machine by what the trachea of band smoke valve and the 5th outlet flue connected，The cooling water pipe being provided with band spray pump connected with in chilling and absorption tower by the 4th water inlet，Described cooling water pipe stretches in chilling and is provided with the first high pressure nozzle with the one end in absorption tower，First high pressure nozzle enters the flue dust instantaneous temperature reduction in chilling and in absorption tower to 200 DEG C after starting，The alkali liquor pipe being provided with band lye pump connected with in chilling and absorption tower by described alkali liquor import，Described alkali liquor pipe stretches in chilling and is provided with the second high pressure nozzle with the one end in absorption tower，Second high pressure nozzle is sprayed onto in chilling after starting and forms alkalescence water film with the alkali liquor moment on the inwall of absorption tower；
Bag-type dust collector, it is configured with dust-removing box, 4th smoke inlet, ash discharging hole and the 6th outlet flue, 4th smoke inlet is arranged in dust-removing box on the sidewall of position, intermediate portion, 4th smoke inlet is connected with the 5th outlet flue in chilling and absorption tower by deacidification absorption trachea, 6th outlet flue is arranged in the top of dust-removing box, it is provided with the 5th air-introduced machine by what the trachea of band smoke valve and the 6th outlet flue connected, it is provided with dedusting filtering bag in described dust-removing box, part stretches into and is provided with oscillating plate in dust-removing box, the position that described oscillating plate stretches out outside dust-removing box is provided with vibrator；
Deacidification adsorbent equipment, it is arranged in chilling and between absorption tower and bag-type dust collector, and it includes slaked lime storage tank, activated carbon storage tank；Slaked lime storage tank is connected with described deacidification absorption trachea by the first pipeline, and described first pipeline is provided with the first blender, sprays lime powder by the first blender to deacidification absorption tracheal strips；Activated carbon storage tank is connected with described deacidification absorption trachea by second pipe, and described second pipe is provided with the second blender, sprays activated carbon powder by the second blender to deacidification absorption tracheal strips；
Water circulation deacidification dedusting washing tower, it is configured with the 5th smoke inlet, clean gas exports, and the 5th smoke inlet is arranged at the bottom of tower, and the outlet of clean gas is arranged in tower top, and the 5th smoke inlet is connected with the 6th outlet flue of bag-type dust collector by trachea；
And the chimney of the clean gas outlet with water circulation deacidification dedusting washing tower, being provided with on-Line Monitor Device in described chimney, on-Line Monitor Device at least can monitor the sulfur dioxide concentration in the clean flue gas discharged from chimney, nitrous oxides concentration, carbonomonoxide concentration, gas concentration lwevel, hydrogen cloride concentration, oxygen concentration, flue dust temperature, moisture content, pressure, flow velocity in real time.
nullThe environment protection emission processing system of trade waste the most according to claim 1，It is characterized in that: described solid waste combustion furnace、It is equipped with temperature sensor and pressure transducer in incineration of liquor stove and each pyrolysis gasification furnace，It is equipped with effusion meter on the sewer pipe of each waste liquid plastic-blasting pay-off，Control to connect each temperature sensor、Pressure transducer、Effusion meter be provided with controller，Force value VFC the first air-introduced machine that controller feeds back according to solid waste combustion furnace pressure sensor and the motor speed of the second aerator，Controller is according to force value VFC second air-introduced machine of incineration of liquor furnace pressure sensor feedback and the motor speed of the 3rd aerator，Controller controls its interior burner according to the temperature value of temperature sensor feedback in solid waste combustion furnace，Controller controls its interior burner according to the temperature value of incineration of liquor in-furnace temperature sensor feedback，Controller controls its interior burner according to the temperature value of temperature sensor feedback in pyrolysis gasification furnace，Controller controls to connect described ejector according to the flow value that effusion meter feeds back.
The environment protection emission processing system of trade waste the most according to claim 1, it is characterized in that: described incineration of liquor stove is configured with three inlets, corresponding three inlets are configured with three set waste liquid spraying pay-offs, and described pyrolysis gasification furnace is configured with three of independent operating.
The environment protection emission processing system of trade waste the most according to claim 1, it is characterized in that: in described solid waste combustion furnace, secondary supplement air is provided with the 4th aerator, the outlet of described 4th aerator is connected to the air inlet of solid waste combustion furnace by the pipeline of band air cock, in described incineration of liquor stove secondary supplement air be provided with the 5th aerator, the outlet of described 5th aerator is connected to the air inlet of incineration of liquor stove by the pipeline of band air cock.
nullThe environment protection emission processing system of trade waste the most according to claim 1 and 2，It is characterized in that: in described chilling and be additionally provided with atomizing tower body in absorption tower，It is sequentially provided with the first baffle plate in described atomizing tower body、Second baffle、Third gear plate、Fourth gear plate、Fifth gear plate，Described first baffle plate、Second baffle、Third gear plate sets gradually along flue dust trend in atomizing tower body，And three is all vertically arranged，The top of the first baffle plate is fixed on tower body sidewall，Arrange at the bottom of the not contact tower of its bottom，The bottom of second baffle is fixed at the bottom of tower，Its top does not contact tower top and arranges，The top that third gear plate erects is fixed on tower body，Arrange at the bottom of the not contact tower of its bottom，Fourth gear plate and the equal horizontally set of fifth gear plate，Both are separately fixed on two sidewalls that tower body is oppositely arranged，And both other ends the most do not contact tower body and arrange.
The environment protection emission processing system of trade waste the most according to claim 5, it is characterized in that: the bottom in described chilling and absorption tower is additionally provided with leakage fluid dram, described leakage fluid dram is connected to a circulating water pool by the drain pipe of band water pump, described circulating water pool is connected to alkali liquor pond by pipeline, and described alkali liquor pond is in alkali liquor to chilling and the alkali liquor import on absorption tower.
The environment protection emission processing system of trade waste the most according to claim 6, it is characterised in that: being provided with a water softener by what the water pipe of band water pump was connected with described cistern, the outlet of described water softener is connected with cistern by water pipe.
The environment protection emission processing system of trade waste the most according to claim 2, it is characterized in that: described 4th smoke inlet, ash discharging hole and the 6th outlet flue are separately positioned on the latter half of dust-removing box side, top and bottom, a demarcation strip it is provided with in described dust-removing box, space partition in dust-removing box is upper box and lower box by described demarcation strip, passage is offered at the center of described demarcation strip, described dedusting filtering bag is fixed on demarcation strip, and its bag mouth alignment passage is arranged, the bag of described dedusting filtering bag is arranged in stretching into lower box.
The environment protection emission processing system of trade waste the most according to claim 8, it is characterized in that: be fixed in described upper box and be provided with an injection tube inside its cover plate, evenly spaced in described injection tube it is provided with multiple winding-up mouth, one end of described injection tube is stretched out casing and is extended laterally, be fixed on described dust-removing box is provided with a pressure gas tank, and described injection tube is stretched out one end that dust-removing box extends laterally and is communicated to pressure gas tank.
The environment protection emission processing system of trade waste the most according to claim 9, it is characterised in that: described injection tube is provided with electromagnetic impulse valve, and described controller controls to connect electromagnetic impulse valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620094323.6U CN205481003U (en) | 2016-01-29 | 2016-01-29 | Processing system is discharged in industrial waste's environmental protection |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620094323.6U CN205481003U (en) | 2016-01-29 | 2016-01-29 | Processing system is discharged in industrial waste's environmental protection |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205481003U true CN205481003U (en) | 2016-08-17 |
Family
ID=56671695
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620094323.6U Withdrawn - After Issue CN205481003U (en) | 2016-01-29 | 2016-01-29 | Processing system is discharged in industrial waste's environmental protection |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205481003U (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105465790A (en) * | 2016-01-29 | 2016-04-06 | 苏州新区环保服务中心有限公司 | Environment-friendly discharge treatment system for industrial waste |
| CN106545879A (en) * | 2016-12-20 | 2017-03-29 | 青岛极致节能环保有限公司 | A kind of negative pressure is ignited separator |
| CN106833694A (en) * | 2017-03-29 | 2017-06-13 | 攀枝花市银江金勇工贸有限责任公司 | A kind of town and country lightweight discarded object destructive distillation carbonization treatment system |
| CN107255288A (en) * | 2017-07-27 | 2017-10-17 | 江苏久朗高科技股份有限公司 | A kind of high concentration salty organic waste liquid incineration tail gas embrane method processing system and technique |
| CN107442554A (en) * | 2017-08-09 | 2017-12-08 | 爱土工程环境科技有限公司 | Pollute discarded object integrated treatment unit and pollution discarded object detection means |
| CN108434864A (en) * | 2018-06-12 | 2018-08-24 | 王鹏 | A kind of desulfurizing industrial fume denitration dust removal system |
| CN108826307A (en) * | 2018-07-13 | 2018-11-16 | 芜湖若科自动化科技有限公司 | A kind of energy-saving and environment-friendly waste incineration case |
| CN117682592A (en) * | 2024-02-02 | 2024-03-12 | 南京宇清环境科技有限公司 | Device and method for simultaneously treating high-salt-content high-COD industrial wastewater and industrial solid waste salt |
| CN117682592B (en) * | 2024-02-02 | 2024-06-11 | 南京宇清环境科技有限公司 | Device and method for simultaneously treating high-salt-content high-COD industrial wastewater and industrial solid waste salt |
-
2016
- 2016-01-29 CN CN201620094323.6U patent/CN205481003U/en not_active Withdrawn - After Issue
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105465790A (en) * | 2016-01-29 | 2016-04-06 | 苏州新区环保服务中心有限公司 | Environment-friendly discharge treatment system for industrial waste |
| CN106545879A (en) * | 2016-12-20 | 2017-03-29 | 青岛极致节能环保有限公司 | A kind of negative pressure is ignited separator |
| CN106833694A (en) * | 2017-03-29 | 2017-06-13 | 攀枝花市银江金勇工贸有限责任公司 | A kind of town and country lightweight discarded object destructive distillation carbonization treatment system |
| WO2019019759A1 (en) * | 2017-07-27 | 2019-01-31 | 江苏久朗高科技股份有限公司 | Membrane method processing system and process for high-concentration salt-containing organic waste liquid incineration exhaust gas |
| CN107255288A (en) * | 2017-07-27 | 2017-10-17 | 江苏久朗高科技股份有限公司 | A kind of high concentration salty organic waste liquid incineration tail gas embrane method processing system and technique |
| CN107255288B (en) * | 2017-07-27 | 2019-05-21 | 江苏久朗高科技股份有限公司 | A kind of high concentration salty organic waste liquid incineration tail gas embrane method processing system and technique |
| CN107442554B (en) * | 2017-08-09 | 2019-06-14 | 爱土工程环境科技有限公司 | Pollute waste integrated treatment unit and pollution waste detection device |
| CN107442554A (en) * | 2017-08-09 | 2017-12-08 | 爱土工程环境科技有限公司 | Pollute discarded object integrated treatment unit and pollution discarded object detection means |
| CN108434864A (en) * | 2018-06-12 | 2018-08-24 | 王鹏 | A kind of desulfurizing industrial fume denitration dust removal system |
| CN108826307A (en) * | 2018-07-13 | 2018-11-16 | 芜湖若科自动化科技有限公司 | A kind of energy-saving and environment-friendly waste incineration case |
| CN108826307B (en) * | 2018-07-13 | 2020-03-13 | 云南博曦环保设备有限公司 | Energy-concerving and environment-protective rubbish burns case |
| CN117682592A (en) * | 2024-02-02 | 2024-03-12 | 南京宇清环境科技有限公司 | Device and method for simultaneously treating high-salt-content high-COD industrial wastewater and industrial solid waste salt |
| CN117682592B (en) * | 2024-02-02 | 2024-06-11 | 南京宇清环境科技有限公司 | Device and method for simultaneously treating high-salt-content high-COD industrial wastewater and industrial solid waste salt |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205481003U (en) | Processing system is discharged in industrial waste's environmental protection | |
| CN105465790B (en) | The environment protection emission processing system of trade waste | |
| CN205388313U (en) | Processing system is discharged in industry solid waste's environmental protection | |
| CN105546545B (en) | The environment protection emission processing system of industrial solid castoff | |
| CN206652386U (en) | A kind of minimum discharge purifier of burning city domestic garbage flue gas | |
| CN105090997B (en) | A kind of highly concentrated brine waste, waste residue low-cost processes method and its device | |
| CN108636098A (en) | A kind of the minimum discharge purifier and its method of burning city domestic garbage flue gas | |
| CN106621754A (en) | Garbage incineration fume ultralow emission purifying system | |
| CN106178892A (en) | Exhaust gas treating method and system are reclaimed in a kind of enamel-covered wire pyrolysis | |
| CN205517237U (en) | Smoke and dust purification treatment system that industrial waste handled | |
| CN109751607A (en) | A kind of sacrificial offerings incinerator with flue gas purification system | |
| CN205965479U (en) | Vent gas treatment system in is retrieved in enameled wire pyrolysis | |
| CN108014591A (en) | A kind of boiler waste gas treating device | |
| CN209672342U (en) | A kind of sacrificial offerings incinerator with flue gas purification system | |
| CN111928263A (en) | System for utilize rotary kiln to burn burning furnace and handle hazardous waste | |
| CN116262198A (en) | Two-stage dry desulfurization deacidification dust removal process for waste incineration flue gas | |
| CN105509068B (en) | The environment protection emission processing system of industrial waste liquid | |
| CN104165364A (en) | Environment-friendly energy-saving waste incineration disposal device | |
| CN205388315U (en) | Processing system is discharged in industry waste liquid's environmental protection | |
| CN206478649U (en) | A kind of useless solid combustion processing unit | |
| CN109453642A (en) | Chemical laboratory rubbish processing to be harmless system | |
| CN204853508U (en) | High enriched salt waste water, low -cost processing apparatus of waste residue of containing | |
| CN217698537U (en) | Hot clean stove depainting exhaust treatment device | |
| CN206478656U (en) | A kind of liquid waste incinerator and a kind of liquid waste treating apparatus | |
| CN206330283U (en) | A kind of Industrial Boiler environment protection energy-saving equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20160817 Effective date of abandoning: 20170912 |