CN109611854A - A kind of organic matter degradation equipment - Google Patents
A kind of organic matter degradation equipment Download PDFInfo
- Publication number
- CN109611854A CN109611854A CN201811507296.0A CN201811507296A CN109611854A CN 109611854 A CN109611854 A CN 109611854A CN 201811507296 A CN201811507296 A CN 201811507296A CN 109611854 A CN109611854 A CN 109611854A
- Authority
- CN
- China
- Prior art keywords
- organic matter
- cavity
- air
- matter degradation
- equipment according
- 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.)
- Pending
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
- F23G5/442—Waste feed arrangements
- F23G5/444—Waste feed arrangements for solid waste
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J1/00—Removing ash, clinker, or slag from combustion chambers
- F23J1/06—Mechanically-operated devices, e.g. clinker pushers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
- F23J15/04—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material using washing fluids
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention belongs to technical field of garbage disposal, more particularly to a kind of organic matter degradation equipment, it includes the internal furnace body with cavity, the feeding port being connected to the cavity, air inlet, exhaust outlet and slag notch are provided on the furnace body, it further include blower and for carrying out magnetized magnetizer to air, the air outlet of the blower is connected to by magnetizer with the air inlet.The equipment is when in use, magnetizer can will enter the intracorporal air of chamber and magnetize, activation energy through the oxygen in magnetized air greatly improves, make a small amount of air that can maintain the burning of material, the device reduces air capacities used when burning material, to reduce the burning gases generated by burning, and then reduce the pollution of burning gases bring.
Description
Technical field
The invention belongs to technical field of garbage disposal, and in particular to a kind of organic matter degradation equipment.
Background technique
Traditional trash processing way mainly has landfill, burning etc., and landfill can occupy a large amount of valuable land resources, simultaneously
It pollutes environment (atmosphere, underground water etc.), thus this simple process mode no longer uses substantially；Compared with landfill disposal, rubbish
Rubbish burning is a kind of preferable processing mode, but rubbish is directly burned and there is problems:
(1) secondary pollution problem；Organic matter in rubbish is in the producing high-molecular containing chlorine for burning the sour gas generated, severe toxicity
Closing object and the flying dust containing Hg, Pb can all pollute the environment；
(2) the problem of burning facility being caused；Chlorine-containing compound forms the corrosive gas such as HCl in furnace in rubbish,
300 DEG C or more i.e. meeting heavy corrosion furnace inner metal component, causes the damage of equipment；Therefore it provides a kind of reduction organic matter is firing
The equipment of the pernicious gas generated during burning, is those skilled in the art's technical problem urgently to be resolved.
Summary of the invention
In order to solve the above problems existing in the present technology, the present invention provides a kind of organic matter degradation equipment, existing to solve
There is the technical issues of secondary pollution caused by directly burning rubbish present in technology.
The present invention implements by the following technical programs:
A kind of organic matter degradation equipment is provided with and the cavity on the furnace body including the internal furnace body with cavity
Feeding port, air inlet, exhaust outlet and the slag notch of connection further include blower and are used to carry out magnetized magnetizer, institute to air
The air outlet for stating blower is connected to by magnetizer with the air inlet.
In order to preferably realize the present invention, make further optimization in said structure, the air inlet setting is useful
In the volume control damper of control air inflow.
In order to preferably realize the present invention, makees further optimization in said structure, be additionally provided with and set in the furnace body
Object platform, the feeding port correspond to the table top setting of the articles holding table, are provided on the table top of the articles holding table to the cavity and push away
Send the material-pulling device of material.
In order to preferably realize the present invention, makees further optimization in said structure, be provided with cooling in the cavity
System, the cooling system include temperature sensor and the first spray equipment, and the temperature sensor and first spray fill
The control switch electrical connection set.
In order to preferably realize the present invention, make further optimization in said structure, which also wraps
Automatic charging device is included, the automatic charging device includes feeding tube and drives the feeding tube to the transmission of feeding port movement
Motor.
In order to preferably realize the present invention, make further optimization in said structure, the automatic charging device also wraps
Sliding rail is included, pulley is provided on the feeding tube, the power output end of the transport motor is connect with the pulley, described to feed intake
Cylinder is slidably arranged on the sliding rail by pulley.
In order to preferably realize the present invention, make further optimization in said structure, the bottom of the cavity is provided with
Ash discharging gear, the ash discharging gear include ash discharge motor and auger, and the discharge end of the auger is located at the slag notch, described
The power intake of the power output end of ash discharge motor and the auger is sequentially connected.
In order to preferably realize the present invention, make further optimization in said structure, which also wraps
Primary dust removing device and two-stage dust removal device are included, the primary dust removing device is arranged in the cavity, the two-stage dust removal dress
It installs in the exhaust ports.
In order to preferably realize the present invention, make further optimization in said structure, the primary dust removing device includes
The second spray equipment sprayed water into the cavity, the two-stage dust removal device are high voltage electrostatic dust precipitator, and the high pressure is quiet
The smoke inlet of electrical dust collector device is connected to the exhaust outlet, and the outlet flue of the high voltage electrostatic dust precipitator is provided with smoke exhaust pipe.
In order to preferably realize the present invention, makees further optimization in said structure, be provided in the smoke exhaust pipe useless
Gas device for catalytic treatment.
In conclusion the present invention has following technical effect that
When in use, magnetizer can will enter the intracorporal air of chamber and magnetize the equipment, through in magnetized air
The activation energy of oxygen greatly improves, and makes a small amount of air that can maintain the burning of material, and the device reduces burning materials
When used air capacity, to reduce the burning gases generated by burning, and then reduce the pollution of burning gases bring.
In addition, prioritization scheme of the invention also has following technical effect that
Air inlet is provided with volume control damper, air inflow can be effectively controlled by the volume control damper, to have
The generation of the control burning gases of effect, reduces pollution brought by burning material.
It is provided with material-pulling device in the furnace body, which can be pushed into the material on articles holding table in cavity, thus
The workload for reducing staff, making the equipment, it is more convenient to use.
It is provided with cooling system in the cavity, the pyrolysis temperature of the equipment can be kept by temperature reducing system, to reduce
The generation of dioxin reduces the pollution to air.
The equipment further includes primary dust removing device and two-stage dust removal device, passes through primary dust removing device and two-stage dust removal device
The generation of miscellaneous dirt can effectively be lowered, to reduce the pollution to air.
Detailed description of the invention
In order to more clearly explain the embodiment of the invention or the technical proposal in the existing technology, to embodiment or will show below
There is attached drawing needed in technical description to be briefly described, it should be apparent that, the accompanying drawings in the following description is only this
Some embodiments of invention for those of ordinary skill in the art without creative efforts, can be with
It obtains other drawings based on these drawings.
Fig. 1 is a kind of perspective view of organic matter degradation equipment of the present invention；
Fig. 2 is a kind of lateral side view of the furnace body of organic matter degradation equipment of the present invention；
Fig. 3 is a kind of cross-sectional view of organic matter degradation equipment of the present invention；
Fig. 4 is a kind of rearview of organic matter degradation equipment of the present invention.
Appended drawing reference:
1, furnace body；2, feeding port；3, air inlet；4, exhaust outlet；5, slag notch；6, blower；7, magnetizer；8, Boiler pressure control
Valve；9, articles holding table；10, material-pulling device；11, temperature sensor；12, the first spray equipment；13, feeding tube；14, sliding rail；15, go out
Grey motor；16, auger；17, primary dust removing device；18, two-stage dust removal device；19, exhaust fume catalytic processing unit.
Specific embodiment
To make the object, technical solutions and advantages of the present invention clearer, technical solution of the present invention will be carried out below
Detailed description.Obviously, described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.Base
Embodiment in the present invention, those of ordinary skill in the art are obtained all without making creative work
Other embodiment belongs to the range that the present invention is protected.
Embodiment one:
A kind of organic matter degradation equipment, as shown in Figures 1 to 4 comprising inside has the furnace body 1 of cavity, sets on furnace body 1
Be equipped with the feeding port 2 being connected to cavity, air inlet 3, exhaust outlet 4 and slag notch 5, further include blower 6 and for air carry out
The air outlet of magnetized magnetizer 7, blower 6 is connected to by magnetizer 7 with air inlet 3, and the air intake vent of blower 6 is connected to outside.
By a kind of organic matter degradation equipment of above structure, when in use, material can be put into cavity by user
And be ignited, blower 6 is capable of providing gas required when rubbish burns in the cavity, and magnetizer 7 can will enter cavity
Interior air is magnetized, and the activation energy through the oxygen in magnetized air greatly improves, and tie up a small amount of air can
The burning of solid waste is held, user can effectively reduce air capacity required when burning material by this way, to subtract
Few exhaust gas generated by burning reduces the pollution of exhaust gas bring.
In addition, the air being magnetized also can indirectly magnetize the intracorporal material of chamber, make the intermolecular of organic matter in material
Poly- power reduces, and makes material that can achieve the effect that pyrolysis at a lower temperature, to reduce the generation of dioxin, reduces
Pollution to air.
Wherein, magnetizer 7 is internally provided at least a pair of magnet, which is permanent magnet, by opposite two magnet
Mutually exclusive magnetic pole is oppositely arranged, and enables the magnet to make to be magnetized by the air of the magnetizer 7, to effectively improve
The activation energy of oxygen in the air being magnetized, the oxygen consumed needed for reducing rubbish during the burning process, and then reduce because of burning
And the combustion exhaust gas generated, reduce the pollution of exhaust gas bring.
Optimization, it is provided with volume control damper 8 at above-mentioned air inlet 3, can effectively be controlled by the volume control damper 8
The air inflow of air processed, so that the generation of more convenient control burning gases, reduces pollution of the burning gases to air.
Optimization, articles holding table 9, the table top setting of the corresponding articles holding table 9 of feeding port 2, to feeding port 2 are additionally provided in furnace body 1
The material of investment can then be fallen on the table top of articles holding table 9；The pusher dress for pushing material is provided on the table top of articles holding table 9
Set 10；When the material in cavity, which is handled, to be completed, user can star material-pulling device 10, and material-pulling device 10 just can will be accumulated
In the material push-in cavity on articles holding table 9, allow what the equipment continued to handle the intracorporal material of chamber.
Preferably, the material-pulling device 10 be hydraulic material-pulling device, by control hydraulic stem elongation, make material-pulling device 10 can
The material on articles holding table 9 to be pushed in cavity.
Optimization, it is additionally provided with cooling system in above-mentioned cavity, which can effectively control in cavity
Temperature avoids generating a large amount of dioxin because ignition temperature is excessively high, to effectively control the generation of dioxin.
Wherein, dioxin is also known as dioxa glutinous rehmannia, is a kind of colorless and odorless, the serious liposoluble substance of toxicity, and dioxin is real
One abbreviation of dioxin on border, what it referred to is not a kind of single substance, but structure and property it is all much like include
The two major classes organic compound of numerous congeners or isomers；In the thermal chemical reaction for burning pyrolysis, dioxin is generated dense
Degree is related with temperature, and when the temperature of pyrolytic reaction is between 350~850 DEG C, the concentration that dioxin generates is maximum.
The device can effectively reduce the temperature inside furnace body 1 by above-mentioned cooling system, make the rubbish inside furnace body 1
Rubbish maintains 300 DEG C or less and is pyrolyzed, and effectively reduces the generation of dioxin, thus the case where reducing environmental pollution hair
It is raw.
Specifically, the cooling system includes temperature sensor 11 and the first spray equipment 12, the temperature sensor 11 and
The control switch of one spray equipment 12 is electrically connected；The temperature sensor 11 is used for the intracorporal temperature of test chamber, when the intracorporal temperature of chamber
When degree is greater than 300 DEG C, which will send a lasting telecommunications to the control switch of the first spray equipment 12
Number, and when control switch receives the lasting electric signal, control switch will start the first spray equipment 12, make the spray
Shower device can spray water into cavity, to play the effect of cooling；When the intracorporal temperature of chamber is lower than 300 DEG C, temperature sensing
Device 11 will stop sending electric signal to control switch, at this point, control switch will close the first spray equipment 12, to make the
One spray equipment 12 stops spraying water into cavity, causes the intracorporal material of chamber can not be into avoid because the intracorporal temperature of chamber is too low
One step carries out the case where being pyrolyzed.
Optimization, it is additionally provided on furnace body 1 convenient for the observation panel of observation 1 inner case of furnace body, and be provided on observation panel
For covering the cover board being located on the observation panel；Staff at work, can directly be checked inside furnace body 1 by observation panel
Situation, in order to carry out the processing of other steps.
Embodiment two:
As advanced optimizing for above-described embodiment, as shown in Figures 1 to 4, which further includes automatic
Charging device, the automatic charging device include feeding tube 13 and transport motor.
Specifically, being provided with sliding rail 14 on above-mentioned furnace body 1, the end of the sliding rail 14 is located at feeding port 2, feeding tube 13
On be provided with pulley, the setting that feeding tube is slided by pulley on sliding rail 14, the power output end of above-mentioned transport motor with
Pulley drive connection, the feeding tube 13 allow feeding tube 13 along sliding rail to feeding intake by transport motor drive pulley rotation
The direction of mouth 2 is mobile；The end of sliding rail 14 is arc-shaped structure, when feeding tube 13 is moved to the end of sliding rail 14, feeding tube
13 can rotate around the arc-shaped sliding rail 14, and the discharge port of feeding tube 13 is made to may correspond to the feeding port 2 of the equipment, thus
Pour into the material in feeding tube 13 smoothly in the equipment.
Preferably, the hopper of taper is provided on the feeding port 2 of the equipment, which can make the material in feeding tube 13
More convenient pours into furnace body 1, can effectively avoid material spilling at feeding port 2 by the hopper, to reduce
The working strength of staff.
Embodiment three:
As shown in Figures 1 to 4, advanced optimizing as embodiment one and embodiment two, the organic matter degradation equipment is also
Including automatic ash discharge, which is arranged in the bottom of cavity；After the completion of the refuse pyrolysis in cavity, ash discharge dress
Setting will convey the dregs of cavity bottom to slag notch 5, collection, processing in order to staff.
Specifically, the ash discharging gear includes ash discharge motor 15 and auger 16, the discharge end of auger 16 is located at slag notch 5,
The power output end of ash discharge motor 15 is connect with auger 16, so that ash discharge motor 15 is able to drive auger 16 and is rotated in cavity；When
After the completion of refuse pyrolysis in cavity, staff can start ash discharge motor 15, and ash discharge motor 15 is made to drive 16 turns of auger
It is dynamic, at this point, the dregs in cavity will be delivered at slag notch 5 by auger 16, in order to which staff is collecting and handling.
Optimization, which further includes primary dust removing device 17 and two-stage dust removal device 18.
Wherein, primary dust removing device 17 is located in cavity, and two-stage dust removal device 18 is located at exhaust outlet 4, organic matter drop
Gas containing smog, dust caused by solution equipment successively passes through primary dust removing device 17 and two-stage dust removal device 18, passes through
Primary dust removing device 17 and two-stage dust removal device 18 can further reduce the dust concentration in gas, thus further
The case where avoiding gas caused by the organic matter degradation equipment from causing secondary pollution to environment generation.
Specifically, primary dust removing device 17 is the second spray equipment, which can spray certainly into cavity
Water, two-stage dust removal device 18 are high voltage electrostatic dust precipitator, which can be in effective adsorbed gas
Suspended particulate；When generating the gas for largely having dust in cavity, staff can start primary dust removing device
17 and two-stage dust removal device 18, and the tap water that primary dust removing device 17 sprays can make in gas biggish granule dust and
Grease stain precipitating, reduces a large amount of particulate matter in gas；Gas after 17 dedusting of primary dust removing device is entered by exhaust outlet 4
When two-stage dust removal device 18, high voltage electrostatic dust precipitator can be with the oil in little particle dust a large amount of in adsorbed gas and smog
Stain, thus the case where gas generated after further preventing material from burning causes secondary pollution to environment generation.
Optimization, it is provided with smoke exhaust pipe at the outlet flue of high voltage electrostatic dust precipitator, by primary dust removing device 17 and two
The gas of grade dust-extraction unit 18 is emitted into atmosphere by smoke exhaust pipe.
Optimization, exhaust fume catalytic processing unit 19 is provided in the smoke exhaust pipe, setting in the exhaust fume catalytic processing unit 19
There is adsorbent equipment, the particulate matter which can be a small amount of in further adsorbed gas is arranged to meet country to dust
The standard put.
Preferably, which is platinum adsorbent equipment, and cellular hole is provided on platinum adsorbent equipment, with
Increase the adsorption area of the adsorbent equipment, to improve the adsorption criteria of the adsorbent equipment.
Wherein, platinum adsorbent equipment can also use the precious metals such as palladium commonly used in the prior art and beryllium to replace.
The above description is merely a specific embodiment, but scope of protection of the present invention is not limited thereto, any
Those familiar with the art in the technical scope disclosed by the present invention, can easily think of the change or the replacement, and should all contain
Lid is within protection scope of the present invention.
Claims (10)
1. a kind of organic matter degradation equipment, it is characterised in that: including the internal furnace body (1) with cavity, set on the furnace body (1)
It is equipped with the feeding port (2) being connected to the cavity, air inlet (3), exhaust outlet (4) and slag notch (5)；Further include blower (6) and
For carrying out magnetized magnetizer (7) to air, the air outlet of the blower (6) passes through magnetizer (7) and the air inlet (3)
Connection.
2. organic matter degradation equipment according to claim 1, it is characterised in that: be provided with and be used at the air inlet (3)
Control the volume control damper (8) of air inflow.
3. organic matter degradation equipment according to claim 2, it is characterised in that: be additionally provided with glove in the furnace body (1)
Platform (9), the table top setting of the corresponding articles holding table (9) of the feeding port (2), be provided on the table top of the articles holding table (9) to
The material-pulling device (10) of the cavity push material.
4. organic matter degradation equipment according to claim 3, it is characterised in that: it is provided with cooling system in the cavity,
The cooling system includes temperature sensor (11) and the first spray equipment (12), the temperature sensor (11) and described first
The control switch of spray equipment (12) is electrically connected.
5. organic matter degradation equipment according to any one of claim 1 to 4, it is characterised in that: further include automatic charging
Device, the automatic charging device include feeding tube (13) and drive the feeding tube (13) to the biography of feeding port (2) movement
Power transmission machine.
6. organic matter degradation equipment according to claim 5, it is characterised in that: the automatic charging device further includes sliding rail
(14), it is provided with pulley on the feeding tube (13), the power output end of the transport motor is connect with the pulley, the throwing
Barrel (13) is slidably arranged on the sliding rail by pulley.
7. organic matter degradation equipment according to any one of claim 2 to 4, it is characterised in that: the bottom of the cavity
It is provided with ash discharging gear, the ash discharging gear includes ash discharge motor (15) and auger (16), the discharge end position of the auger (16)
At the slag notch (5), the power output end of the ash discharge motor (15) and the power intake of the auger (16) are driven
Connection.
8. organic matter degradation equipment according to claim 7, it is characterised in that: further include primary dust removing device (17) and two
Grade dust-extraction unit (18), the primary dust removing device (17) are arranged in the cavity, two-stage dust removal device (18) setting
At the exhaust outlet (4).
9. organic matter degradation equipment according to claim 8, it is characterised in that: the primary dust removing device (17) include to
The second spray equipment sprayed water in the cavity, the two-stage dust removal device (18) are high voltage electrostatic dust precipitator, the high pressure
The smoke inlet of electrostatic precipitator is connected to the exhaust outlet (4), and the outlet flue of the high voltage electrostatic dust precipitator is provided with row
Smoke pipe.
10. organic matter degradation equipment according to claim 9, it is characterised in that: be provided with exhaust gas in the smoke exhaust pipe and urge
Change processing unit (19).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811507296.0A CN109611854A (en) | 2018-12-10 | 2018-12-10 | A kind of organic matter degradation equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811507296.0A CN109611854A (en) | 2018-12-10 | 2018-12-10 | A kind of organic matter degradation equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109611854A true CN109611854A (en) | 2019-04-12 |
Family
ID=66006992
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811507296.0A Pending CN109611854A (en) | 2018-12-10 | 2018-12-10 | A kind of organic matter degradation equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109611854A (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1293234A (en) * | 1969-08-29 | 1972-10-18 | Metallgesellschaft Ag | Refuse incinerating plant |
| CN200958091Y (en) * | 2006-09-30 | 2007-10-10 | 武汉川岛重工机械设备制造有限公司 | Fast high-heat-value carbonizing furnace |
| CN105020716A (en) * | 2015-07-01 | 2015-11-04 | 上海煜工环保科技有限公司 | Midline slag fall type smoke wind pyrolyzing furnace |
| CN204943497U (en) * | 2015-09-15 | 2016-01-06 | 鑫源昊（北京）环保能源科技有限公司 | Magnetization cracking device |
| CN206234828U (en) * | 2016-12-07 | 2017-06-09 | 上海楷都智能科技有限公司 | Novel absorbent charcoal desulfurization of flue gas by adsorption technology system |
-
2018
- 2018-12-10 CN CN201811507296.0A patent/CN109611854A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1293234A (en) * | 1969-08-29 | 1972-10-18 | Metallgesellschaft Ag | Refuse incinerating plant |
| CN200958091Y (en) * | 2006-09-30 | 2007-10-10 | 武汉川岛重工机械设备制造有限公司 | Fast high-heat-value carbonizing furnace |
| CN105020716A (en) * | 2015-07-01 | 2015-11-04 | 上海煜工环保科技有限公司 | Midline slag fall type smoke wind pyrolyzing furnace |
| CN204943497U (en) * | 2015-09-15 | 2016-01-06 | 鑫源昊（北京）环保能源科技有限公司 | Magnetization cracking device |
| CN206234828U (en) * | 2016-12-07 | 2017-06-09 | 上海楷都智能科技有限公司 | Novel absorbent charcoal desulfurization of flue gas by adsorption technology system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103363531B (en) | A kind of dangerous waste incinerator complexes | |
| CN101201167B (en) | Apparatus and method for gasification of refuse and hyperthermia melt processing of flying ash | |
| CN1884912A (en) | Medical refuse incineration process and system equipment therefor | |
| CN101112669A (en) | Multilevel purifier for disacidifying using dry and wet method and for removing dust by using cloth bag | |
| CN207999834U (en) | A kind of medical waste pyrolysis gasification furnace incinerator | |
| CN203757724U (en) | Garbage incinerator | |
| CN202224433U (en) | Refuse treatment system unit capable of effectively restraining dioxin | |
| CN205619341U (en) | Environment -friendly refuse treatment burns burning furnace convenient to wash | |
| CN209263040U (en) | A kind of active carbon discharge rate automatic control system of waste incineration | |
| CN205351332U (en) | Burning furnace is burnt in domestic waste environmental protection | |
| CN109611854A (en) | A kind of organic matter degradation equipment | |
| CN106753474A (en) | A kind of domestic garbage pyrolysis processing system and low temperature, high temperature pyrolysis processing method | |
| CN204987023U (en) | Waste incinerator and gas cleaning integrated device | |
| CN206553459U (en) | A kind of domestic garbage pyrolysis processing system | |
| CN202105553U (en) | Integrated device for removing tar oil and dust in smoke of biomass fuel heat supply device | |
| CN211290074U (en) | Kiln tail accumulated slag cleaning device for incineration treatment of hazardous waste rotary kiln | |
| CN210740424U (en) | Environment-friendly dust removal incinerator | |
| CN208090679U (en) | A kind of solid waste multi-cycle coupling collaboration processing unit | |
| CN107013921B (en) | A kind of administering method of absorption VOCs exhaust gas solid waste | |
| CN217329847U (en) | Flue gas purification treatment device of garbage incinerator | |
| CN215411894U (en) | Industrial waste incineration waste treatment system | |
| CN108613195A (en) | A kind of rubbish, solid waste burning purifier | |
| CN217274156U (en) | Burn burning furnace convenient to deashing | |
| CN212299015U (en) | Heat accumulating type incinerator | |
| CN109780553A (en) | Novel environment friendly waste incinerator |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20190412 |