CN105823050A - Energy-saving type garbage processing system - Google Patents
Energy-saving type garbage processing system Download PDFInfo
- Publication number
- CN105823050A CN105823050A CN201610162149.9A CN201610162149A CN105823050A CN 105823050 A CN105823050 A CN 105823050A CN 201610162149 A CN201610162149 A CN 201610162149A CN 105823050 A CN105823050 A CN 105823050A
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- Prior art keywords
- slag
- energy
- dust
- tail gas
- collection case
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Classifications
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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
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
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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
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- 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
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- 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
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J2700/00—Ash removal, handling and treatment means; Ash and slag handling in pulverulent fuel furnaces; Ash removal means for incinerators
- F23J2700/001—Ash removal, handling and treatment means
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J2700/00—Ash removal, handling and treatment means; Ash and slag handling in pulverulent fuel furnaces; Ash removal means for incinerators
- F23J2700/003—Ash removal means for incinerators
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention discloses an energy-saving type garbage processing system. The energy-saving type garbage processing system comprises a garbage processing furnace, a first induced draft fan, a water filtering device, an air blower, a second induced draft fan, a slag collecting box, a dust collecting machine, a dust dissolving tank and a tail gas purifying mechanism. According to the energy-saving type garbage processing system, furnace ash and slag which are produced in the garbage processing furnace are separated and processed, dust in the slag is separated through tail gas, the separation cost of the dust in the slag is reduced, and processing of smoke dust in the tail gas and processing of the dust in the slag are combined, so that not only is the cost reduced, but also the efficiency is improved.
Description
Technical field
The present invention relates to technical field of waste treatment, particularly relate to a kind of energy-saving refuse disposal system.
Background technology
Rubbish is mankind's daily life and the solid waste produced in producing, and owing to output is big, complicated component is various, and has contaminative, resource and social, as do not dealt carefully with, just pollute the environment, affect environmental health, waste resource, destroys productive life safety, destroys social harmony.Garbage disposal seeks to a rubbish and removes rapidly, and carries out harmless treatment, is the most reasonably utilized.
Along with environmental problem is gradually taken seriously, energy-saving and environmental protection become the development topic of various countries, have begun to provide the chance of industry development into garbage disposal.Whole world rubbish average annual growth is 8.42%, and China's rubbish rate of increase reaches more than 10%.The whole world produces 4.9 hundred million tons of rubbish, only China every year and just produces nearly 1.5 hundred million tons of municipal refuses every year.Municipal Solid Waste in China accumulation volume of cargo in storage has reached 7,000,000,000 tons.Under the hugest rubbish pressure, it is reason to believe that, MSW processing industry can become following domestic star's industry.
At present, garbage disposal mainly uses the mode of burning, and the tail gas and the waste residue that produce in combustion process all include substantial amounts of flue dust and dust, in order to avoid atmospheric pollution, must discharge after processing the flue dust in tail gas and the dust in waste residue, with high costs, structure is complicated.
Summary of the invention
The technical problem existed based on background technology, the present invention proposes a kind of energy-saving refuse disposal system.
The energy-saving refuse disposal system of one that the present invention proposes, including: incineration furnace garbage processes stove, the first air-introduced machine, water treatment plant, aerator, the second air-introduced machine, slag collection case, vacuum cleaner, dust dissolving tank and tail gas clean-up mechanism；
Incineration furnace garbage processes stove and is provided with charging aperture, air inlet, the first gas outlet, the second gas outlet and slag-drip opening；Air inlet distance incineration furnace garbage processes furnace bottom preset distance, and the second gas outlet is arranged on above air inlet, and the first gas outlet is arranged on above the second gas outlet；
First gas outlet is connected with air inlet with water treatment plant by the first air-introduced machine, processes furnace bottom by an ajutage with incineration furnace garbage and connect at blower outlet；
Slag-drip opening is connected with the slag input port of slag collection case by the ground-slag separating mechanism preset, and the second gas outlet is connected with the tail gas input port of slag collection case by the second air-introduced machine；The tail gas delivery outlet of slag collection case connects with the input port of vacuum cleaner, and the equipped at outlet port of vacuum cleaner is provided with dust removing tube, in the liquid that the dust removing tube other end is filled in inserting dust dissolving tank and being submerged in dust dissolving tank；
The gas outlet of dust dissolving tank connects with the input of tail gas clean-up mechanism；
Incineration furnace garbage processes can process stove by rubbish is poured into incineration furnace garbage after furnace bottom lights flame, and aerator processes furnace bottom input oxygen-containing gas to incineration furnace garbage, and rubbish is from base burning；The rubbish that incineration furnace garbage processes in stove is up divided into oxide layer, reducing zone and dry distilling layer according to variations in temperature by burning position；Reducing zone is by the decomposable asymmetric choice net substance decomposition in rubbish, moisture in rubbish is evaporated by dry distilling layer, the mixed gas that the steam of gas and the generation of dry distilling layer that incineration furnace garbage is processed reducing zone generation in stove by the first air-introduced machine is formed is drawn in water treatment plant except importing oxide layer after water, and oxide layer will be as tail gas discharge after the harmful substance high-temperature oxydation in mixed gas；The slag that incineration furnace garbage processes in stove enters slag collection case by slag-drip opening；Tail gas is imported into slag collection case and under vacuum cleaner effect, carries the dust in slag collection case and enters dust dissolving tank, and the pure gaseous state tail gas of dust dissolving tank output discharges after being purified by tail gas clean-up mechanism.
Preferably, water treatment plant includes cooler bin and airway, and airway is arranged in cooler bin, and its first end and the connection of the first gas outlet, its second end connects with air inlet, is filled with cooling medium in cooler bin.
Preferably, airway is serpentine pipe.
Preferably, the second gas outlet is connected with slag collection case by exhaust pipe, and the second air-introduced machine is arranged on exhaust pipe, and exhaust pipe is looped around incineration furnace garbage and processes stove periphery.
Preferably, incineration furnace garbage processes furnace sidewall and is provided with observation window, and observation window processes furnace bottom near incineration furnace garbage and arranges.
Preferably, the slag input port of slag collection case and tail gas delivery outlet are arranged on top, and the tail gas input port of slag collection case is arranged on bottom.
Preferably, also include being provided with on crush box and utility box, crush box and utility box tail gas delivery outlet, and all connect with the input port of vacuum cleaner；Being provided with reducing mechanism in crush box, the slag delivery outlet of slag collection case connects with the input port of crush box, and the delivery outlet of crush box connects with the input port of utility box.
Preferably, the sorting mechanism classified according to diameter through slag it is provided with in utility box.
Preferably, sorting mechanism is helical duct or is obliquely installed and zones of different is distributed the sieve plate of material-dropping hole of different pore size.
Preferably, ajutage is looped around garbage disposal furnace periphery.
The energy-saving refuse disposal system that the present invention proposes, decomposable asymmetric choice net material in rubbish is adequately broken at reducing zone, reduce the intractability of harmful substance in rubbish, the tail gas that garbage processing procedure produces the most have passed through high-temperature oxydation in oxide layer, can avoid including pest confrontation air in tail gas and pollute.
In the present invention, by the ashes produced in garbage disposal furnace and slag separating treatment, and the tail gas that oxide layer exports is imported dust dissolving tank after slag collection case, tail gas in slag collection case with slag collision impact, the dust comprised in slag is kicked up, after then carrying dust, enters dust dissolving tank.Tail gas is because being to discharge from oxide layer, inevitably it is infected with flue dust in oxide layer, in the present invention, utilize this tail gas just carrying a small amount of flue dust that the residual dust comprised in slag is separated, then the tail gas carrying dust being imported dust dissolving tank, disposably dust and flue dust to comprising in tail gas dissolve.
The present invention i.e. make use of tail gas that slag is carried out the dust separation in slag, reduces the cost of dust separation in slag, the process of dust in flue dust in tail gas and slag is united two into one again, both saved cost, be improved efficiency.
Accompanying drawing explanation
Fig. 1 is the one energy-saving refuse disposal system structural representation that the present invention proposes.
Detailed description of the invention
With reference to Fig. 1, the energy-saving refuse disposal system of one that the present invention proposes, including: incineration furnace garbage processes stove 1, the first air-introduced machine 2, water treatment plant 3, aerator the 4, second air-introduced machine 5, slag collection case 6, crush box 13, utility box 14, vacuum cleaner 7, dust dissolving tank 8 and tail gas clean-up mechanism A.
Incineration furnace garbage processes stove 1 and is provided with charging aperture, air inlet, the first gas outlet, the second gas outlet and slag-drip opening.Air inlet distance incineration furnace garbage processes has preset distance bottom stove 1, and the second gas outlet is arranged on above air inlet, and the first gas outlet is arranged on above the second gas outlet.
Incineration furnace garbage processes can pour rubbish into incineration furnace garbage process stove 1 by charging aperture after lighting flame bottom stove 1, and the rubbish that incineration furnace garbage processes in stove 1 is up divided into oxide layer, reducing zone and dry distilling layer according to variations in temperature by burning position.Oxide layer temperature is the highest, can be aoxidized by harmful substance, and the decomposable asymmetric choice net material in rubbish is decomposed by reducing zone, and the moisture in rubbish is evaporated forming steam by dry distilling layer.In present embodiment, owing to rubbish directly overlays on flame, so incineration furnace garbage processes the combustion system not havinging fierceness in stove 1, safety is high.Connected bottom incineration furnace garbage process stove 1 by an ajutage 9 at aerator 4 air outlet, aerator 4 processes input oxygen-containing gas bottom stove 1 internal oxidation layer by ajutage 9 to incineration furnace garbage, to ensure that oxide layer rubbish sustained combustion provides high temperature, and ensure that the harmful substance in oxide layer is substantially oxidized.
In present embodiment, ajutage 9 is looped around garbage disposal furnace periphery, in order to oxygen-containing gas enters oxide layer after being preheated by garbage disposal furnace 1 outer wall in ajutage 9, thus avoids oxygen-containing gas low temperature input oxide layer can reduce oxide layer temperature.
First gas outlet is connected with air inlet with water treatment plant 3 by the first air-introduced machine 2.In present embodiment, first gas outlet is positioned at above dry distilling layer, first air-introduced machine 2 is drawn in water treatment plant 3 by the mixed gas of the steam that the decomposition gas comprising reducing zone generation and dry distilling layer are produced by the first gas outlet, mixed gas is imported into oxide layer by air inlet after being filtered out steam in water treatment plant 3, thus the fuel gas in mixed gas burns in oxide layer, to improve the speed of oxide layer incineration firing and abundant degree, the harmful gas in mixed gas is at oxide layer complete oxidation.Tail gas after oxide layer complete oxidation is discharged by the second gas outlet under the second air-introduced machine 5 effect.
Water treatment plant 3 includes cooler bin 301 and airway 302, and airway 302 is arranged in cooler bin 301, and its first end and the connection of the first gas outlet, its second end connects with air inlet, is filled with cooling medium in cooler bin 301.Mixed gas is by after airway 302, and steam therein meets condensation knot, thus is separated.After isolating the mixed gas entrance oxide layer of steam, the too high adverse effect to combustion reaction of water content can be avoided.In present embodiment, in order to improve water rem oval, airway 302 uses serpentine pipe.
In present embodiment, air inlet is corresponding with bottom oxide layer, and the second gas outlet is corresponding with oxide layer temperature highest point such as oxide layer top layer, in order to the tail gas that the second gas outlet is discharged is the most the most oxidized in oxide layer, prevents harmful gas from discharging.
In order to ensure air inlet, the second gas outlet and oxide layer stablizing relative to position, it is necessary to the slag of furnace bottom is discharged in time, it is to avoid move past many in oxide layer.In present embodiment, incineration furnace garbage processes stove 1 sidewall and is provided with observation window, and observation window 12 processes near incineration furnace garbage and arranges bottom stove 1, so, can be observed the accumulation of furnace bottom slag by observation window, thus discharge slag in time.In present embodiment, in order to avoid oxide layer temperature is scattered and disappeared from furnace bottom, it should tiling at the bottom of holding furnace has one layer of slag or ashes to be incubated.
In present embodiment, the power of the second air-introduced machine 5 is more than the power of the first air-introduced machine 2, the input flow velocity of oxygen-containing gas under velocity ratio aerator 4 effect is discharged by the tail gas of the second gas outlet big during i.e. incineration furnace garbage processes stove 1, so, keep incineration furnace garbage to process stove 1 internal clock and maintain negative pressure state, avoid incineration furnace garbage to overflow after processing the harmful gas high-temperature expansion in stove 1 and cause atmospheric pollution, and avoid incineration furnace garbage to process explosives burning generation blast in stove 1.
Slag-drip opening is connected with the slag input port of slag collection case 6 by the ground-slag separating mechanism such as cyclone separator preset, and the second gas outlet is connected with the tail gas input port of slag collection case 6 by the second air-introduced machine 5.In garbage disposal furnace 1, producing the ashes of dust-like and the slag of solid granular, ashes and slag after incineration firing and enter ground-slag separating mechanism by slag-drip opening, ashes and slag are separated in ground-slag separating mechanism, ashes are collected separately, and slag enters in slag collection case 6 and carries out subsequent treatment.
The tail gas delivery outlet of slag collection case 6, tail gas delivery outlet all input ports with vacuum cleaner 7 of tail gas delivery outlet and utility box 14 of crush box 13 connect, the equipped at outlet port of vacuum cleaner 7 is provided with dust removing tube 10, in the liquid that dust removing tube 10 other end is filled in inserting dust dissolving tank 8 and being submerged in dust dissolving tank 8.The gas outlet of dust dissolving tank 8 connects with the input of tail gas clean-up mechanism A；
Tail gas is imported into slag collection case 6 and under vacuum cleaner 7 acts on, and carries the i.e. dust of ashes of residual in the slag in slag collection case 6 and enters dust dissolving tank 8, and the pure gaseous state tail gas of dust dissolving tank 8 output discharges after being purified by tail gas clean-up mechanism A.
Being provided with reducing mechanism in crush box 13, the slag delivery outlet of slag collection case 6 connects with the input port of crush box 13, and the delivery outlet of crush box 13 connects with the input port of utility box 14.After most dust separation is gone out in slag collection case 6 by slag, entering in crush box 13, the slag that diameter is big is crushed, and the dust produced in crush box 13 is imported in dust dissolving tank 8 by vacuum cleaner 7 equally.
Being provided with the sorting mechanism classified according to diameter through slag in utility box 14, sorting mechanism can be helical duct, and slag is on spirality channel in rolling process, and the slag of different size diameter is by inertia-responsive impact difference, thus classifies it；Or, sorting mechanism is set to be obliquely installed and zones of different is distributed the sieve plate of material-dropping hole of different pore size, such as the sieve aperture on sieve plate increases the most successively, in order to the slag of different-diameter is at zones of different blanking thus separates.Dust in utility box 14 imports in dust dissolving tank 8 again by vacuum cleaner 7, in order to be sufficiently separated the dust in slag.
Dust is dissolved by the liquid in dust dissolving tank 8, and tail gas overflows into from liquid after tail gas clean-up mechanism A purifies and discharges.Tail gas clean-up mechanism A can use high efficiency particulate air filter, or employing is made up of drying device, adsorbent equipment, acid-base neutralization device etc..
In present embodiment, the slag input port of slag collection case 6 and tail gas delivery outlet are arranged on top, and the tail gas input port of slag collection case 6 is arranged on bottom.So, in slag dropping process, the abundant oxygen of dust, tail gas thus bottom input more dust is impacted, be conducive to strengthen dust separation efficiency.In like manner, the tail gas delivery outlet of crush box 13 and the tail gas delivery outlet of utility box 14 are also arranged at top.
In present embodiment, the second gas outlet is connected with slag collection case 6 by exhaust pipe 11, and the second air-introduced machine 5 is arranged on exhaust pipe 11, and exhaust pipe 11 is looped around incineration furnace garbage and processes stove 1 periphery.So, utilize high-temperature tail gas that incineration furnace garbage is processed stove 1 and be incubated, high temperature utilization rate, beneficially incineration furnace garbage can be improved and process decomposition reaction and the oxidation reaction of oxide layer of furnace reduction layer.
The above; it is only the present invention preferably detailed description of the invention; but protection scope of the present invention is not limited thereto; any those familiar with the art is in the technical scope that the invention discloses; according to technical scheme and inventive concept equivalent or change in addition thereof, all should contain within protection scope of the present invention.
Claims (10)
1. an energy-saving refuse disposal system, it is characterized in that, including: incineration furnace garbage processes stove (1), the first air-introduced machine (2), water treatment plant (3), aerator (4), the second air-introduced machine (5), slag collection case (6), vacuum cleaner (7), dust dissolving tank (8) and tail gas clean-up mechanism (A)；
Incineration furnace garbage processes stove (1) and is provided with charging aperture, air inlet, the first gas outlet, the second gas outlet and slag-drip opening；Air inlet distance incineration furnace garbage processes stove (1) bottom preset distance, and the second gas outlet is arranged on above air inlet, and the first gas outlet is arranged on above the second gas outlet；
First gas outlet is connected with air inlet with water treatment plant (3) by the first air-introduced machine (2), processes stove (1) bottom by an ajutage (9) with incineration furnace garbage and connect at aerator (4) air outlet；
Slag-drip opening is connected with the slag input port of slag collection case (6) by the ground-slag separating mechanism preset, and the second gas outlet is connected with the tail gas input port of slag collection case (6) by the second air-introduced machine (5)；The tail gas delivery outlet of slag collection case (6) connects with the input port of vacuum cleaner (7), the equipped at outlet port of vacuum cleaner (7) is provided with dust removing tube (10), in the liquid that dust removing tube (10) other end is filled in inserting dust dissolving tank (8) and being submerged in dust dissolving tank (8)；
The gas outlet of dust dissolving tank (8) connects with the input of tail gas clean-up mechanism (A).
Energy-saving refuse disposal system the most as claimed in claim 1, it is characterized in that, water treatment plant (3) includes cooler bin (301) and airway (302), airway (302) is arranged in cooler bin (301), its first end and the connection of the first gas outlet, its second end connects with air inlet, and cooler bin is filled with cooling medium in (301).
Energy-saving refuse disposal system the most as claimed in claim 2, it is characterised in that airway (302) is serpentine pipe.
Energy-saving refuse disposal system the most as claimed in claim 1, it is characterized in that, second gas outlet is connected with slag collection case (6) by exhaust pipe (11), second air-introduced machine (5) is arranged on exhaust pipe (11), and exhaust pipe (11) is looped around incineration furnace garbage and processes stove (1) periphery.
Energy-saving refuse disposal system the most as claimed in claim 1, it is characterised in that incineration furnace garbage processes stove (1) sidewall and is provided with observation window, and observation window (12) processes stove (1) bottom near incineration furnace garbage and arranges.
Energy-saving refuse disposal system the most as claimed in claim 1, it is characterised in that the slag input port of slag collection case (6) and tail gas delivery outlet are arranged on top, the tail gas input port of slag collection case (6) is arranged on bottom.
Energy-saving refuse disposal system the most as claimed in claim 1, it is characterized in that, also include crush box (13) and utility box (14), it is provided with tail gas delivery outlet on crush box (13) and utility box (14), and all input ports with vacuum cleaner (7) connect；Crush box is provided with reducing mechanism in (13), the slag delivery outlet of slag collection case (6) connects with the input port of crush box (13), and the delivery outlet of crush box (13) connects with the input port of utility box (14).
Energy-saving refuse disposal system the most as claimed in claim 7, it is characterised in that utility box is provided with, in (14), the sorting mechanism classified through slag according to diameter.
Energy-saving refuse disposal system the most as claimed in claim 8, it is characterised in that sorting mechanism is helical duct or is obliquely installed and zones of different is distributed the sieve plate of material-dropping hole of different pore size.
Energy-saving refuse disposal system the most as claimed in claim 1, it is characterised in that ajutage (9) is looped around garbage disposal furnace periphery.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610162149.9A CN105823050B (en) | 2016-03-21 | 2016-03-21 | A kind of energy-saving refuse disposal system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610162149.9A CN105823050B (en) | 2016-03-21 | 2016-03-21 | A kind of energy-saving refuse disposal system |
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| CN105823050A true CN105823050A (en) | 2016-08-03 |
| CN105823050B CN105823050B (en) | 2018-05-08 |
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| CN201610162149.9A Active CN105823050B (en) | 2016-03-21 | 2016-03-21 | A kind of energy-saving refuse disposal system |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106693598A (en) * | 2017-01-13 | 2017-05-24 | 安徽未名鼎和环保有限公司 | Device for treating tail gas of combustion furnace |
| CN108502425A (en) * | 2018-03-07 | 2018-09-07 | 广州利萨智能化科技有限公司 | A kind of follow-on Intelligent traffic management systems |
| CN108593809A (en) * | 2018-06-29 | 2018-09-28 | 莱茵技术（上海）有限公司 | A kind of detection device and method burned for organic matter |
| CN106247346B (en) * | 2016-10-12 | 2018-09-28 | 桃江县博强再生资源有限公司 | One kind is for clinker recovery and processing system after consumer waste incineration |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1769397A (en) * | 2005-10-19 | 2006-05-10 | 天津大学 | Device and method for suppressing refuse end gas injurant using pyrolysis and aerification technology |
| JP2007078197A (en) * | 2005-09-12 | 2007-03-29 | Shoei:Kk | Incinerator and incinerating method of waste |
| CN102506439A (en) * | 2011-09-30 | 2012-06-20 | 智胜化工股份有限公司 | Method for blowing soot for waste heat boiler by using waste |
| CN203099861U (en) * | 2013-01-30 | 2013-07-31 | 浙江富春江环保热电股份有限公司 | Boiler slag hole dust-removing device |
| CN203784971U (en) * | 2014-04-08 | 2014-08-20 | 广州东凌粮油股份有限公司 | Boiler soot blower for grease machining |
| CN104456579A (en) * | 2014-12-10 | 2015-03-25 | 唐厚胜 | Environment-friendly garbage disposal device |
-
2016
- 2016-03-21 CN CN201610162149.9A patent/CN105823050B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007078197A (en) * | 2005-09-12 | 2007-03-29 | Shoei:Kk | Incinerator and incinerating method of waste |
| CN1769397A (en) * | 2005-10-19 | 2006-05-10 | 天津大学 | Device and method for suppressing refuse end gas injurant using pyrolysis and aerification technology |
| CN102506439A (en) * | 2011-09-30 | 2012-06-20 | 智胜化工股份有限公司 | Method for blowing soot for waste heat boiler by using waste |
| CN203099861U (en) * | 2013-01-30 | 2013-07-31 | 浙江富春江环保热电股份有限公司 | Boiler slag hole dust-removing device |
| CN203784971U (en) * | 2014-04-08 | 2014-08-20 | 广州东凌粮油股份有限公司 | Boiler soot blower for grease machining |
| CN104456579A (en) * | 2014-12-10 | 2015-03-25 | 唐厚胜 | Environment-friendly garbage disposal device |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106247346B (en) * | 2016-10-12 | 2018-09-28 | 桃江县博强再生资源有限公司 | One kind is for clinker recovery and processing system after consumer waste incineration |
| CN106693598A (en) * | 2017-01-13 | 2017-05-24 | 安徽未名鼎和环保有限公司 | Device for treating tail gas of combustion furnace |
| CN108502425A (en) * | 2018-03-07 | 2018-09-07 | 广州利萨智能化科技有限公司 | A kind of follow-on Intelligent traffic management systems |
| CN108593809A (en) * | 2018-06-29 | 2018-09-28 | 莱茵技术（上海）有限公司 | A kind of detection device and method burned for organic matter |
| CN108593809B (en) * | 2018-06-29 | 2023-12-26 | 莱茵技术（上海）有限公司 | Detection device and method for organic matter incineration |
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| Publication number | Publication date |
|---|---|
| CN105823050B (en) | 2018-05-08 |
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