CN110397923A - A kind of comprehensive cyclic processing device of waste - Google Patents
A kind of comprehensive cyclic processing device of waste Download PDFInfo
- Publication number
- CN110397923A CN110397923A CN201910681091.2A CN201910681091A CN110397923A CN 110397923 A CN110397923 A CN 110397923A CN 201910681091 A CN201910681091 A CN 201910681091A CN 110397923 A CN110397923 A CN 110397923A
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- Prior art keywords
- incinerator
- waste
- powder
- gas
- dust collector
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Classifications
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/20—Combinations of devices covered by groups B01D45/00 and B01D46/00
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- 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
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- 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
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- 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
- F23G5/46—Recuperation of heat
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
- F23G7/061—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K3/00—Feeding or distributing of lump or pulverulent fuel to combustion apparatus
- F23K3/02—Pneumatic feeding arrangements, i.e. by air blast
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
- F23L15/00—Heating of air supplied for combustion
- F23L15/04—Arrangements of recuperators
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
- F23L7/00—Supplying non-combustible liquids or gases, other than air, to the fire, e.g. oxygen, steam
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/60—Separating
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2205/00—Waste feed arrangements
- F23G2205/20—Waste feed arrangements using airblast or pneumatic feeding
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2206/00—Waste heat recuperation
- F23G2206/10—Waste heat recuperation reintroducing the heat in the same process, e.g. for predrying
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2209/00—Specific waste
- F23G2209/14—Gaseous waste or fumes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K2203/00—Feeding arrangements
- F23K2203/20—Feeding/conveying devices
- F23K2203/201—Feeding/conveying devices using pneumatic means
-
- 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
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
Abstract
The present invention relates to changing rejected material to useful resource comprehensive utilization technique and devices, disclose a kind of comprehensive cyclic processing device of waste, it includes incinerator (1), it further include interconnected the pre-heat treatment device (2) and multistage rotary dust collector (3), the high-temperature flue gas that burning generates in incinerator (1) flows into the pre-heat treatment device (2) and carries out heat exchange processing to waste to be processed, treated that waste to be processed enters in multistage rotary dust collector (3) and is separated into powder and gas liquid mixture for heat exchange, multistage rotary dust collector (3), which is connected to incinerator (1) and powder is introduced into incinerator (1), to burn.Combustor of the invention can be using heavy oil as fuel, the treatment of wastes with processes of wastes against one another, the discharge of pollutant can be reduced to the greatest extent, it is burned by the exhaust gas that processing generates by incinerator by the waste containing organic liquid, generate heat, it can be used to preheated air and powder granule, reduce the consumption of the energy.
Description
Technical field
The present invention relates to changing rejected material to useful resource comprehensive utilization technique and device, more particularly to a kind of comprehensive circulation of waste
Processing unit.
Background technique
According to statistics, the whole world generates about more than 400,000,000 tons hazardous wastes every year, and the inappropriate disposition of hazardous waste will be good for human body
Health and environment cause serious influence.Since the processing of China's hazardous waste is still within the primary stage, to relation technological researching
It starts late, collection is less with treatment facility, and the quantity of hazardous waste is increasing sharply.It is especially right recently as country
The raising of environmental requirement proposes higher standard to the disposing task of hazardous waste.Due to it is domestic at present to dangerous powder with
And organic liquid waste comprehensive utilization of resources technical research is less.The present invention is intended to provide a kind of danger powder and organic
Liquid debris comprehensive utilization of resources technology and a kind of associated apparatus.
Currently, patent name be a kind for the treatment of method changing rejected material to useful resource, the patent of invention of Patent No. 95106313.8,
Solve the problems, such as that such as damaged tire, printed circuit board waste material, plastic waste or scrap rubber, greasy filth and sludge are handled, but there is also
The defect of hazardous waste can not be handled.
Summary of the invention
The present invention provides at a kind of comprehensive circulation of waste for the shortcomings that can not handling hazardous waste in the prior art
Manage device.
In order to solve the above-mentioned technical problem, the present invention is addressed by following technical proposals:
A kind of comprehensive cyclic processing device of waste, including incinerator further include interconnected the pre-heat treatment device with
Multistage rotary dust collector, the high-temperature flue gas that the interior burning of incinerator generates are flowed into the pre-heat treatment device and are changed waste to be processed
Heat treatment, treated that waste to be processed enters in multistage rotary dust collector and be separated into powder and gas liquid mixture for heat exchange, multistage
Deduster, which is connected to incinerator and powder is introduced into incinerator, to burn.
Preferably, further including by the sequentially connected blower of pipeline, air preheater and powder injector, blower is to sky
Dispatch air in air preheater, air preheater are connect and by the high-temperature flue gas of incinerator generation to the sky in it with incinerator
Gas is preheated, and the air after preheating is connected to simultaneously by pipeline with the powder outlet end of multistage rotary dust collector by air preheater
Powder is pushed in powder injector, further includes injection pipe, powder injector is by the air driven powder after heating by spraying
Pipeline is penetrated to spray into oxygen-enriched combusting machine and incinerator.
Preferably, further including gas-liquid separator, gas-liquid separator is connected to multistage rotary dust collector and divides multistage rotary dust collector
The gas liquid mixture separated out carries out gas-liquid separation, and gas-liquid separator is connected to injection pipe and is discharged into the organic gas after separating
In injection pipe, gas-liquid separator separates go out liquid by sewage-treatment plant and fluid organic material processing unit at
Reason.
Preferably, further including crusher, waste to be processed passes through the break process of crusher and enters the pre-heat treatment
It exchanges heat in device.
Preferably, multistage rotary dust collector includes primary dust removing device and secondary ash collector, the outlet side of secondary ash collector and gas
Liquid/gas separator connection, the inlet communication for going out dirt end and primary dust removing device of secondary ash collector, powder go out dirt by primary dust removing device
End discharge, primary dust removing device are cyclone dust collectors, and secondary ash collector is electric precipitator or bag filter.
Preferably, further including air valve, air valve is mounted between level-one multistage rotary dust collector and the pre-heat treatment device.
Preferably, further including flue gas processing device, the high-temperature flue gas discharge of flue gas processing device and the pre-heat treatment device
End is connected to and handles high-temperature flue gas.
Preferably, the lower end of incinerator is equipped with cooling device, cooling device is useless to the powder after burning in incinerator
Slag is cooled down and generates glassy state waste material.
Preferably, cooling device includes pond, cooling tower, moisture separator, pump, the lower part of incinerator is immersed in pond
In, cooling tower is equipped with the upper tube being connected to respectively with incinerator lower part and the lower tube being connected to pond, upper tube and lower tube
On be mounted on pump, the outlet side of cooling tower is connected to moisture separator with the outlet side of incinerator, moisture separator go out
Water end (W.E.) is connected to lower tube.
Preferably, further including screw conveyor and holding vessel, after screw conveyor is located at below incinerator and will burn
The glassy state waste material transportation of formation is to holding vessel.
The present invention is due to using above technical scheme, with significant technical effect: combustor of the present invention uses special
There is combustor can be using heavy oil as fuel, the treatment of wastes with processes of wastes against one another can reduce to the greatest extent the discharge of pollutant, for example contain
The waste of organic liquid is burned by the exhaust gas that processing generates by incinerator, generates heat, can be used to preheated air with
Powder granule, reduces the consumption of the energy, and mixing material then can be solid waste such as cullet etc.；Pass through proprietary combustor
Oxygen-enriched combusting, ignition temperature can achieve 2000 ° or more, effectively reduce dangerous powder and contain organic liquid waste
The generation of object dioxin in combustion, it is therefore prevented that secondary pollution；The present invention can with scale make various dangerous powders with
And the waste containing organic liquid formed white or transparent coloured glaze state substance, coloured glaze state substance can recycle uses, reduction
Operating cost；By multistage bootstrap system, smoke heat energy is made full use of, improves the efficiency of heating- utilization of fuel, is handled
Efficiency is obviously improved, and can carry out integrated treatment benefit to dangerous powder and organic liquid waste on a large scale since its is low in cost
With.
Detailed description of the invention
Fig. 1 is structural schematic diagram of the invention.
Fig. 2 is the partial enlarged view I of Fig. 1.
Fig. 3 is the partial enlarged view II of Fig. 1.
The toponym that each number designation is referred in attached drawing is as follows: 1-incinerator, 2-the pre-heat treatment devices, more than 3-
Grade deduster, 4-cooling devices, 5-screw conveyors, 6-holding vessels, 7-oxygen-enriched combusting machines, 8-blowers, 9-air are pre-
Hot device, 10-powder injectors, 11-crushers, 12-air valves, 13-gas-liquid separators, 14-injection pipes, 15-cigarettes
Flash Gas Compression Skid System, 31-primary dust removing devices, 32-secondary ash collectors, 41-ponds, 42-cooling towers, 43-moisture separators,
44-pumps, 421-upper tubes, 422-lower tubes, 131-sewage-treatment plants, 132-fluid organic material processing units.
Specific embodiment
Present invention is further described in detail with embodiment with reference to the accompanying drawing.
Embodiment 1
A kind of comprehensive cyclic processing device of waste, as shown, further including interconnected preheating including incinerator 1
Processing unit 2 and multistage rotary dust collector 3, the high-temperature flue gas that the interior burning of incinerator 1 generates flow into the pre-heat treatment device 2 and treat place
Reason waste carries out heat exchange processing, heat exchange treated waste to be processed enters in multistage rotary dust collector 3 and be separated into powder and
Gas liquid mixture, multistage rotary dust collector 3, which is connected to incinerator 1 and powder is introduced into incinerator 1, to burn.
It further include pre- to air by the sequentially connected blower 8 of pipeline, air preheater 9 and powder injector 10, blower 8
Dispatch air in hot device 9, air preheater 9 is connect with incinerator 1 and the high-temperature flue gas that is generated by incinerator 1 is to the sky in it
Gas is preheated, and the air after preheating is connected to by pipeline with the powder outlet end of multistage rotary dust collector 3 by air preheater 9
And push to powder in powder injector 10, it further include injection pipe 14, powder injector 10 is by the air driven after heating
Powder is sprayed into oxygen-enriched combusting machine 7 and incinerator 1 by injection pipe 14.Oxygen-enriched combusting machine 7 is located at 1 top of incinerator, oxygen-enriched combustion
Burning machine 7 is connected with air compressor machine and making oxygen by air separation machine, and oxygen-enriched combusting machine 7 is burnt by the combination of oxygen and powder.
It further include gas-liquid separator 13, gas-liquid separator 13 is connected to multistage rotary dust collector 3 and isolates multistage rotary dust collector 3
Gas liquid mixture carry out gas-liquid separation, the organic gas after separating simultaneously is discharged by the connection of gas-liquid separator 13 and injection pipe 14
In injection pipe 14, the liquid that gas-liquid separator 13 is isolated passes through sewage-treatment plant 131 and fluid organic material processing unit
132 are handled.
It further include crusher 11, waste to be processed passes through the break process of crusher 11 and enters the pre-heat treatment device 2
In exchange heat.
Multistage rotary dust collector 3 includes primary dust removing device 31 and secondary ash collector 32, the outlet side of secondary ash collector 32 and gas-liquid
Separator 13 is connected to, and the outlet side of secondary ash collector 32 is connected to gas-liquid separator 13, and secondary ash collector 32 goes out dirt end and one
The inlet communication of grade deduster 31, powder are discharged by the dirt end that goes out of primary dust removing device 31, and powder goes out dirt by primary dust removing device 31
End discharge, primary dust removing device 31 are cyclone dust collectors, and secondary ash collector 32 is electric precipitator or bag filter.
It further include air valve 12, air valve 12 is mounted between level-one multistage rotary dust collector 31 and the pre-heat treatment device 2.Lock wind
Valve action: first is that the hot wind in truncation junior's air hose enters higher level's cyclone cylinder by expects pipe, air flow shortcircuit is prevented；On the other hand,
Guarantee that material can pass through expects pipe and enter junior's air hose to exchange heat, realizes Conveyance.
It further include flue gas processing device 15, the high-temperature flue gas outlet side company of flue gas processing device 15 and the pre-heat treatment device 2
Lead to and high-temperature flue gas is handled.
Embodiment 2
Same as Example 1, the difference is that the lower end of incinerator 1 is equipped with cooling device 4, cooling device 4 is to incinerator 1
Powder waste residue after interior burning is cooled down and generates glassy state waste material.
Cooling device 4 includes pond 41, cooling tower 42, moisture separator 43, pump 44, and the lower part of incinerator 1 is immersed in water
In pond 41, cooling tower 42 is equipped with the upper tube 421 being connected to respectively with incinerator lower part and the lower tube 422 being connected to pond 41,
It is mounted on pump 44 on upper tube 421 and lower tube 422, the outlet side of the outlet side of cooling tower 42 and incinerator 1 is and aqueous vapor
Separator 43 is connected to, and the water outlet of moisture separator 43 is connected to lower tube 422.
Water is transported in cooling tower 42 by the lower tube 422 that acts through of pump 44 in pond 42, by under fan action
The relatively low air of temperature and cooling tower 42 in filler water carry out heat exchange, to have the function that reduce water temperature.At this time
42 top of cooling tower can generate high temperature air, and 1 lower part of incinerator is immersed in pond 41, and high temperature melt substance is fallen down, meeting
Steam is generated, the high temperature air and steam generated in cooling tower 41 reaches gas-liquid separator 43 under differential pressure action, by gas-liquid
The effect of separator 43, gas are separated with liquid, and liquid enters cooling tower 42, and gas discharge, cooling water passes through after heat exchange
Pump 44 enters in pond 41 by upper tube 421, to be recycled.
Embodiment 3
It is same as Example 1, the difference is that further including screw conveyor 5 and holding vessel 6, screw conveyor 5, which is located at, to be burned
The lower section of furnace 1 and by the glassy state waste material transportation formed after burning to holding vessel 6.
In short, the foregoing is merely presently preferred embodiments of the present invention, it is all according to equalization made by scope of the present invention patent
Variation and modification, shall all be covered by the patent of the invention.
Claims (9)
1. a kind of comprehensive cyclic processing device of waste, including incinerator (1), it is characterised in that: further include interconnected pre-
Annealing device (2) and multistage rotary dust collector (3), the high-temperature flue gas that the interior burning of incinerator (1) generates flow into the pre-heat treatment device (2)
In and heat exchange processing carried out to waste to be processed, treated that waste to be processed enters in multistage rotary dust collector (3) simultaneously for heat exchange
Be separated into powder and gas liquid mixture, multistage rotary dust collector (3) be connected to incinerator (1) and by powder be introduced into incinerator (1) into
Row burning；It further include flue gas processing device (15), the high-temperature flue gas discharge of flue gas processing device (15) and the pre-heat treatment device (2)
End is connected to and handles high-temperature flue gas.
2. the comprehensive cyclic processing device of a kind of waste according to claim 1, it is characterised in that: further include passing through pipeline
Sequentially connected blower (8), air preheater (9) and powder injector (10), blower (8) is to air preheater (9) interior dispatch
Air, air preheater (9) connect with incinerator (1) and the high-temperature flue gas that is generated by incinerator (1) to the air in it into
Air after preheating is connected to by pipeline with the powder outlet end of multistage rotary dust collector (3) by row preheating, air preheater (9)
And push to powder in powder injector (10), powder injector (10) is connected to the powder outlet end of multistage rotary dust collector (3),
It further include injection pipe (14), the air driven powder after heating is sprayed by injection pipe (14) and burned by powder injector (10)
In furnace (1).
3. the comprehensive cyclic processing device of a kind of waste according to claim 2, it is characterised in that: further include gas-liquid separation
Device (13), gas-liquid separator (13) be connected to multistage rotary dust collector (3) and the gas liquid mixture of isolating multistage rotary dust collector (3) into
Row gas-liquid separation, gas-liquid separator (13) are connected to injection pipe (14) and the organic gas after separating are discharged into injection pipe
(14) in, the liquid that gas-liquid separator (13) is isolated passes through sewage-treatment plant (131) and fluid organic material processing unit
(132) it is handled.
4. the comprehensive cyclic processing device of a kind of waste according to claim 1, it is characterised in that: further include crusher
(11), waste to be processed passes through the break process of crusher (11) and enters in the pre-heat treatment device (2) and exchanges heat.
5. the comprehensive cyclic processing device of a kind of waste according to claim 3, it is characterised in that: multistage rotary dust collector (3)
Including primary dust removing device (31) and secondary ash collector (32), the outlet side and gas-liquid separator (13) of secondary ash collector (32) are even
Logical, the inlet communication for going out dirt end and primary dust removing device (31) of secondary ash collector (32), powder is gone out by primary dust removing device (31)
The discharge of dirt end, primary dust removing device (31) are cyclone dust collectors, and secondary ash collector (32) is electric precipitator or bag filter.
6. the comprehensive cyclic processing device of a kind of waste according to claim 5, it is characterised in that: further include air valve
(12), air valve (12) is mounted between level-one multistage rotary dust collector (31) and the pre-heat treatment device (2).
7. the comprehensive cyclic processing device of a kind of waste according to claim 1, it is characterised in that: under incinerator (1)
End is equipped with cooling device (4), and cooling device (4) cools down the powder waste residue after burning in incinerator (1) and generates glass
Glass state waste material.
8. the comprehensive cyclic processing device of a kind of waste according to claim 7, it is characterised in that: cooling device (4) packet
Pond (41), cooling tower (42), moisture separator (43), pump (44) are included, the lower part of incinerator (1) is immersed in pond (41),
Cooling tower (42) is equipped with the upper tube (421) being connected to respectively with incinerator lower part and the lower tube (422) being connected to pond (41),
It is mounted on pump (44) in upper tube (421) and lower tube (422), the outlet side of cooling tower (42) and the outlet of incinerator (1)
End is connected to moisture separator (43), and the water outlet of moisture separator (43) is connected to lower tube (422).
9. the comprehensive cyclic processing device of a kind of waste according to claim 1, it is characterised in that: further include helical feed
Machine (5) and holding vessel (6), screw conveyor (5) are located at the glassy state waste material transportation that will be formed below incinerator (1) and after burning
To holding vessel (6).
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| Application Number | Priority Date | Filing Date | Title |
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| CN201910681091.2A CN110397923A (en) | 2019-07-26 | 2019-07-26 | A kind of comprehensive cyclic processing device of waste |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201910681091.2A CN110397923A (en) | 2019-07-26 | 2019-07-26 | A kind of comprehensive cyclic processing device of waste |
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Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2563442Y (en) * | 2002-07-23 | 2003-07-30 | 洪文虎 | Waste material incinerator |
| CN102476129A (en) * | 2010-11-29 | 2012-05-30 | 周仁福 | Integrated converting and utilizing co-production method for agricultural waste |
| CN102583945A (en) * | 2012-01-13 | 2012-07-18 | 哈尔滨工业大学 | Sludge multi-stage drying device, fluidized bed combustion treatment device and fluidized bed combustion treatment method |
| CN207391044U (en) * | 2017-09-07 | 2018-05-22 | 上海晟兰石化工程技术有限公司 | A kind of acrylic nitrile waste water processing system |
| CN108176703A (en) * | 2018-02-11 | 2018-06-19 | 武汉凯迪工程技术研究总院有限公司 | Polynary waste method for innocent treatment and its system |
-
2019
- 2019-07-26 CN CN201910681091.2A patent/CN110397923A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2563442Y (en) * | 2002-07-23 | 2003-07-30 | 洪文虎 | Waste material incinerator |
| CN102476129A (en) * | 2010-11-29 | 2012-05-30 | 周仁福 | Integrated converting and utilizing co-production method for agricultural waste |
| CN102583945A (en) * | 2012-01-13 | 2012-07-18 | 哈尔滨工业大学 | Sludge multi-stage drying device, fluidized bed combustion treatment device and fluidized bed combustion treatment method |
| CN207391044U (en) * | 2017-09-07 | 2018-05-22 | 上海晟兰石化工程技术有限公司 | A kind of acrylic nitrile waste water processing system |
| CN108176703A (en) * | 2018-02-11 | 2018-06-19 | 武汉凯迪工程技术研究总院有限公司 | Polynary waste method for innocent treatment and its system |
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Application publication date: 20191101 |