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CN101367088A - Garbage treatment method and comprehensive utilization - Google Patents

Garbage treatment method and comprehensive utilization Download PDF

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Publication number
CN101367088A
CN101367088A CNA2008102328195A CN200810232819A CN101367088A CN 101367088 A CN101367088 A CN 101367088A CN A2008102328195 A CNA2008102328195 A CN A2008102328195A CN 200810232819 A CN200810232819 A CN 200810232819A CN 101367088 A CN101367088 A CN 101367088A
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CN
China
Prior art keywords
incinerator
waste
ash
rubbish
biochemical treatment
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
Application number
CNA2008102328195A
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Chinese (zh)
Inventor
袁永扬
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Individual
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Individual
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Filing date
Publication date
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Priority to CNA2008102328195A priority Critical patent/CN101367088A/en
Publication of CN101367088A publication Critical patent/CN101367088A/en
Priority to PCT/CN2009/001090 priority patent/WO2010037268A1/en
Pending legal-status Critical Current

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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
    • F23G5/006—General arrangement of incineration plant, e.g. flow sheets
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2900/00—Special features of, or arrangements for incinerators
    • F23G2900/50208—Biologic treatment before burning, e.g. biogas generation
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2215/00—Preventing emissions
    • F23J2215/20—Sulfur; Compounds thereof
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2215/00—Preventing emissions
    • F23J2215/50—Carbon dioxide
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2900/00—Special arrangements for conducting or purifying combustion fumes; Treatment of fumes or ashes
    • F23J2900/15061—Deep cooling or freezing of flue gas rich of CO2 to deliver CO2-free emissions, or to deliver liquid CO2
    • 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
    • F23L2900/00—Special arrangements for supplying or treating air or oxidant for combustion; Injecting inert gas, water or steam into the combustion chamber
    • F23L2900/07005—Injecting pure oxygen or oxygen enriched air
    • 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
    • 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
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
    • 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
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00—Technologies for solid waste management
    • Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Processing Of Solid Wastes (AREA)
  • Fertilizers (AREA)

Abstract

The invention discloses a method for treating waste and comprehensive utilization thereof. The method adopts a high-temperature incineration technology to greatly reduce a virulent gas in smoke gas dioxin and greatly increase the concentration of a CO2 gas; heat energy, the smoke gas and clinker produced in the incineration process can generate power and produce dry ice, rubber powder, floor tiles, organic compound fertilizer and the like after treatment, thereby realizing no emission, no pollution and no waste in the waste incineration treatment. The waste treatment method comprises the following steps: methane produced in a biochemical treatment pool is conducted to an incinerator and ignites the dry waste in the incinerator; pure oxygen produced in an air separation device is conducted to the incinerator and supports the combustion of the waste to produce the smoke gas containing high-concentration CO2; the temperature in the incinerator is up to over 1,200 DEG C; and the smoke gas is desulphurized and purified to obtain purified CO2. In the method, the smoke gas, the heat energy and the clinker produced by incinerating the waste are matched with liquid nitrogen produced by a liquefier and the air separation device to prepare CO2 liquid, the floor tiles, the rubber powder, the organic compound fertilizer and other useful resources.

Description

A kind of waste disposal method and comprehensive utilization thereof
Technical field
The present invention relates to the technology of garbage disposal field, particularly a kind of waste disposal method and comprehensive utilization thereof.
Background technology
Rubbish comprises two kinds of house refuse and industrial refuses, wherein house refuse comprises town dweller's domestic refuse, the domestic refuse of urban street cleaning, the domestic refuse of cities and towns catering trade, the mud of urban life waste water treatment plant, the mud of cleaning is gushed in the river, cities and towns, town dweller's ight soil, junked tire etc.Discarded rubbish " three change " is handled and is meant minimizing, innoxious, changing waste into resources.The application incineration technology will be discarded rubbish and send in the incinerator, by the incineration oxidation reaction, the organic carbon in the rubbish will be converted into CO 2, hydrogen is converted into H 2O makes discarded rubbish become value product, and at high temperature kills virus and bacterium, realizes the processing of minimizing, innoxious and changing waste into resources.
At present, the processing mode of discarded rubbish is mainly contained two kinds of landfill and burning electricity generations.In the existing refuse landfill, it is simple and easy landfill yard that landfill yard more than 50% is arranged approximately, can not accomplish timely covering, not possessing perfect garbage leachate collects, arranges and lead and treatment facility, there is not perfect landfill gas row to lead and treatment facility yet, particularly landfill yard ooze drop liquid because collection that there is no need and concentrated purified treatment, caused the severe contamination of water resource and ambient soil.Because the calorific value of municipal refuse is improving constantly, the recovery energy of rubbish becomes a reality.But all garbage incinerating power plants have all just utilized the heat energy that incineration firing produced, and are still unresolved to the discharging or the recycling of secondary pollution in the waste incineration process.
The conventional garbage incinerator all is to adopt auxiliary fuel-diesel oil or coal, add air-breathing, stove internal combustion temperature has only 800-1000 ℃, garbage organism is difficult to completing combustion in the stove, because stove internal combustion temperature is lower than 1200 ℃, just be easy to generate dioxin toxic and harmful, seriously contaminated environment when causing in the stove garbage organism imperfect combustion.The dioxin of contained severe toxicity is difficult to thoroughly handle totally in the flue gas, and dioxin is contaminated air not only, also can be by accumulation polluted source and plant, and edible contaminated aquatic products or fruit are thin can to influence health.Owing to adopt air-breathing, a large amount of nitrogen is participated in burning and is produced nitrogen oxide, and contaminated air also causes acid rain easily, and simultaneously, also the loss heat reduces the thermal efficiency, and in addition, because in the air, nitrogen accounts for major part, oxygen only accounts for fraction, so CO in the flue gas 2Concentration is lower, is difficult to go to recycle with industrial method.
Summary of the invention
The object of the present invention is to provide a kind of waste disposal method and comprehensive utilization thereof, it adopts the high temperature garbage burning technology, and the hypertoxic gas dioxin in the flue gas that produces in the incinerator can greatly be reduced, and CO 2Gas concentration but greatly increases, thereby has the industrialization recovery value; The heat energy that produces in the high temperature garbage burning process, flue gas and lime-ash after treatment, can generate electricity, can produce liquid CO 2, rubber powder, construction material, compoiste fertilizer, adsorbent and regulus melt down processing, realizes that incineration treatment of garbage do not have discharging, pollution-free, no waste.
Technical solution proposed by the invention is such: a kind of waste disposal method, rubbish is sent into biochemical treatment tank carry out biochemical treatment, send in the incinerator through the rubbish of fume afterheat drying and to burn, produce the generating of steam drive generating set, the incinerator flue gas that produces of burning away the refuse is discharged through desulfurization, the lime-ash collection and treatment that incinerator produces, the biogas that described biochemical treatment tank produces feed the dry rubbish that ignites in the incinerator; Be provided with air-separating plant, this air-separating plant produces pure oxygen and liquid nitrogen, and pure oxygen wherein feeds in the described incinerator, and to the combustion-supporting burning of rubbish, the incineration temperature scope is 1200-1500 ℃ in the stove; Flue gas after the described desulfurization obtains carbon dioxide after purifying.
Carbon dioxide after purifying compressed and liquefied become liquid carbon dioxide, obtain dry ice through puffing again.Regulus and sandstone ash are isolated in lime-ash magnetization after burning in the described incinerator, and regulus returns converter usefulness again, and the sandstone ash adds makes floor tile after adhesive mixes.Junked tire removed add the liquid nitrogen of sending here from air-separating plant behind steel wire and the fiber, make rubber powder, in rubber powder, add the solid sulfur that from the flue gas desulfurization program, obtains then, make rubber through vulcanizing treatment.In described biochemical treatment tank, in the mud of biochemical treatment, add the lightweight ash in ight soil and the described sandstone slag, make compoiste fertilizer.
Compared with prior art, the present invention has following remarkable result:
(1) owing to adopted the pure oxygen burning-aid method in the incinerator, simultaneously, also utilize anaerobic fermentation rubbish to produce the auxiliary incineration firing of biogas, make that incineration temperature reaches 1200 ℃-1500 ℃ in the stove, on the one hand, because of pure oxygen combustion-supporting, CO in the flue gas that incinerator produces 2Four times have been improved during the original air-breathing of concentration ratio, thereby have the industrialization recovery value, simultaneously, because temperature reaches more than 1200 ℃ in the incinerator, the completing combustion that this helps rubbish in the stove can significantly reduce the generation of hypertoxic gas dioxin and sulfide, nitrogen oxide.
(2) adopt this waste disposal method can obtain the carbon dioxide of high concentration, compressed machine supercharging becomes liquid carbon dioxide to store use with the liquefier low-temperature liquefaction, or the liquid carbon dioxide puffing is made dry ice; The liquid nitrogen that utilizes air-separating plant to supply with makes the fragmentation of junked tire superfreeze make rubber powder, adds from the solid sulfur of flue gas desulfurization acquisition the rubber powder vulcanizing treatment is made rubber again; The lime-ash of incinerator is isolated sandstone ash, regulus, lightweight ash, and sandstone are grey and make the building floor tile after the desulfurization slag that desulfurizing agent stays flue gas desulfurization adds the adhesive mixing together; Regulus is sent to steel plant and is melted down, and the lightweight ash can be made adsorbent, can also add in the ight soil mud in rubbish and send into biochemical treatment tank and carry out biochemical treatment, and make compoiste fertilizer.Incineration treatment of garbage zero-emission, pollution-free, changing waste into resources have really been realized.
Description of drawings
Fig. 1 is the waste disposal method of one embodiment of the invention and the process flow diagram of comprehensive utilization thereof.
The specific embodiment
By following embodiment the present invention is further elaborated.
Referring to shown in Figure 1, the present invention provides materials such as a kind of waste disposal method and the flue gas that is produced, heat, lime-ash and fully utilizes in the garbage disposal process, realizes the zero-emission of garbage disposal, the purpose of pollution-free, changing waste into resources.Waste disposal method of the present invention is such: rubbish is sent into biochemical treatment tank, through 3-7 days biochemical processing, produce biogas, send in the incinerator after all the other garbage utilization fume afterheat dryings, the biogas of biochemical treatment tank feeds the dry rubbish that ignites in the incinerator, and the pure oxygen that produces from air-separating plant feeds the combustion-supporting waste incineration of incinerator, owing to adopt pure oxygen to burn, so 1200 ℃-1500 ℃ of incinerator Nei Wenduda, rubbish produces high concentration CO in the combustion-supporting combustion process of pure oxygen 2Flue gas, and hypertoxic gas dioxin greatly reduces, the waste heat that generally contains impurity such as sulfide, nitrogen oxide, water vapour and several Baidu in the flue gas, utilize the waste heat drying of flue gas to go into the preceding rubbish of incinerator, the waste heat of flue gas is reduced to more than 100 below the degree, flue gas precooling separation of water vapor, the flue gas of drying is delivered to desulfurizer the sulfide in the flue gas is separated again, again through the CO in adsorbents such as the activated carbon purification flue gas with desulfurizing agent 2, incinerator also constantly produces lime-ash and a large amount of heat energy in burning process, and these heat energy become the generating of steam rear drive Turbo-generator Set by boiler, and the afterheat steam after these electric weight and the generating is to air-separating plant and CO 2Power devices heat supplies (drying) such as process units, personal back then can be for sale if any electricity more than needed and hot.
Comprehensive utilization situation by the flue gas that produces in this method disposal of refuse process, lime-ash is such:
(1) CO after the purification 2Be pressurized to 4.0Mpa pressure by non-lubricated compressor, make gaseous state CO through the refrigerating plant liquefier then 2Become liquid CO 2, the on-condensible gas through behind the liquefier (-40 ℃ approximately of condensing temperatures) adopts the sudden strain of a muscle crystal method to make on-condensible gas and liquid CO 2Separate pure liquid CO 2Be stored in cryogenic liquid CO 2Storage tank is stored as product.Also can be with liquid CO 2Puffing makes dry ice.
Handling 500 tons of rubbish with day is example, and when adopting prior art, the smoke discharge amount that is produced is 6,480,000 m 3/ day, atmospheric environment is caused severe contamination; When adopting technical solution of the present invention, can withdrawal liquid CO 2Amount is 230 tons/day, and does not have waste gas and discharge to atmosphere.The freezing power consumption of aquatic products is the 260kwh/ ton, and the freezing consumption dry ice of aquatic products amount is the 550kg/ ton.With liquid CO 2Be transformed into dry ice, then can make 115 tons on dry ice every day, but 210 tons of frozen fishes as adopting the freezing 210 tons of aquatic products of refrigeration plant, then need power consumption 54600kwh,, then can save electric weight: 1992.9 ten thousand kwh to calculate in year.
(2) lime-ash that waste incineration process produces adopts magnetization and technique of preparing to isolate sandstone ash, regulus and light slag (ashes), and materials such as sandstone ash (also can add the desulfurization slag that flue gas desulfurization produces) mixed adhesive are made the building ground brick; Regulus can melt down steel-making; The effective fertile element of interpolation was made compoiste fertilizer after nitrogen in the light slag, phosphorus, potassium and ight soil were mixed together biochemical treatment, and the residue in the light slag is made adsorbent or adsorbing agent carrier.
(3) air-separating plant mainly provides pure oxygen, purity nitrogen and straight argon, and it is combustion-supporting and for the production Ozone Water provides oxygen source that pure oxygen is mainly used in waste incineration, surplus capacity liquefaction back export trade liquid oxygen; The full liquefaction of purity nitrogen is mainly used in the fragmentation of junked tire superfreeze and makes rubber powder, becomes the rubber material, and the solid sulfur of utilizing flue gas desulfurization to produce is made rubber with the rubber powder vulcanizing treatment.
Adopt this method to burn away the refuse and its emission just fully utilized and rubbish can be become complete available resource, really realize incineration treatment of garbage zero-emission, pollution-free, no waste.

Claims (5)

1. waste disposal method, rubbish is sent into biochemical treatment tank carry out biochemical treatment, send in the incinerator through the rubbish of fume afterheat drying and to burn, produce the generating of steam drive generating set, the incinerator flue gas that produces of burning away the refuse is discharged through desulfurization, the lime-ash collection and treatment that incinerator produces is characterized in that: the biogas that described biochemical treatment tank produces feeds the dry rubbish that ignites in the incinerator; Be provided with air-separating plant, this air-separating plant produces pure oxygen and liquid nitrogen, and pure oxygen wherein feeds in the described incinerator, and to the combustion-supporting burning of rubbish, the incineration temperature scope is 1200-1500 ℃ in the stove; Flue gas after the described desulfurization obtains carbon dioxide after purifying.
2. the carbon dioxide that utilizes the described waste disposal method of claim 1 to be obtained is made dry ice, and it is characterized in that: the carbon dioxide after will purifying compresses and liquefies and becomes liquid carbon dioxide, obtains dry ice through puffing again.
3. the lime-ash that utilizes the described waste disposal method of claim 1 to be obtained is produced floor tile, it is characterized in that: regulus and sandstone ash are isolated in the lime-ash magnetization after burning in the described incinerator, regulus returns converter usefulness again, and the sandstone ash adds makes floor tile after adhesive mixes.
4. the sulphur and the liquid nitrogen that utilize the described waste disposal method of claim 1 to be obtained are made rubber, it is characterized in that: add the liquid nitrogen of sending here from air-separating plant after junked tire is removed steel wire and fiber, make rubber powder, in rubber powder, add the solid sulfur that from the flue gas desulfurization program, obtains then, make rubber through vulcanizing treatment.
5. the biochemical treatment thing that utilizes the described waste disposal method of claim 1 to be obtained is made compoiste fertilizer, it is characterized in that: add the lightweight ash in ight soil and the described sandstone slag in described biochemical treatment tank, make compoiste fertilizer in the mud of biochemical treatment.
CNA2008102328195A 2008-09-27 2008-09-27 Garbage treatment method and comprehensive utilization Pending CN101367088A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
CNA2008102328195A CN101367088A (en) 2008-09-27 2008-09-27 Garbage treatment method and comprehensive utilization
PCT/CN2009/001090 WO2010037268A1 (en) 2008-09-27 2009-09-27 Method for processing garbage and comprehensive treatment technology thereof

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Application Number Priority Date Filing Date Title
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WO (1) WO2010037268A1 (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010037268A1 (en) * 2008-09-27 2010-04-08 Yuan Yongyang Method for processing garbage and comprehensive treatment technology thereof
CN102705832A (en) * 2012-05-11 2012-10-03 袁永扬 Solid waste incinerator without emission of flue gas
CN103742918A (en) * 2013-12-05 2014-04-23 谢华原 Waste incineration treatment process
CN108224450A (en) * 2016-12-22 2018-06-29 内蒙古大学 Fully closed garbage incineration method and its device
CN108315081A (en) * 2018-04-08 2018-07-24 源创环境科技有限公司 The RDF production systems of aging rubbish are dried using the landfill gas of refuse landfill
CN109373324A (en) * 2018-11-27 2019-02-22 中国中元国际工程有限公司 A kind of garbage disposal association system and method
CN110822437A (en) * 2019-11-07 2020-02-21 光大环保技术研究院（南京）有限公司 Waste incineration power generation system and method
CN111360022A (en) * 2020-03-17 2020-07-03 江苏和合环保集团有限公司 Landfill method beneficial to comprehensive treatment of household garbage
CN112871964A (en) * 2021-01-08 2021-06-01 光大环保（中国）有限公司 Meal kitchen and burn integration and deal with device in coordination

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CN108045862B (en) * 2018-01-18 2024-02-13 洛阳理工学院 Garbage discharging valve for suspension combustion furnace
CN108204592A (en) * 2018-02-08 2018-06-26 吴永勇 A kind of waste incineration cleaning system
CN111018300A (en) * 2019-11-27 2020-04-17 中建科技有限公司 Excrement treatment method and system
CN112443846B (en) * 2020-11-24 2024-10-22 上海市安装工程集团有限公司 Garbage storage warehouse
CN115477455A (en) * 2022-05-12 2022-12-16 杭州坤灵环境技术有限公司 Sludge and leachate synergistic full recycling method based on catalytic pyrohydrolysis technology

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US6935251B2 (en) * 2002-02-15 2005-08-30 American Air Liquide, Inc. Steam-generating combustion system and method for emission control using oxygen enhancement
CN1282849C (en) * 2004-11-09 2006-11-01 滕清华 Domestic garbage continuous incinerator
CN1850370A (en) * 2006-05-15 2006-10-25 滕清华 Life-garbage comprehensive treatment technology
CN100523614C (en) * 2007-03-12 2009-08-05 刘春� Oxygen-enriched combustion and heat-transferring system and its applied method
CN101367088A (en) * 2008-09-27 2009-02-18 袁永扬 Garbage treatment method and comprehensive utilization
CN101367519A (en) * 2008-09-27 2009-02-18 袁永扬 Apparatus for preparing carbonic anhydride with high temperature garbage burning

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010037268A1 (en) * 2008-09-27 2010-04-08 Yuan Yongyang Method for processing garbage and comprehensive treatment technology thereof
CN102705832A (en) * 2012-05-11 2012-10-03 袁永扬 Solid waste incinerator without emission of flue gas
CN102705832B (en) * 2012-05-11 2013-07-10 袁永扬 Solid waste incinerator without emission of flue gas
CN103742918A (en) * 2013-12-05 2014-04-23 谢华原 Waste incineration treatment process
CN103742918B (en) * 2013-12-05 2016-04-20 谢华原 Incineration treatment of garbage technique
CN108224450B (en) * 2016-12-22 2021-02-05 内蒙古大学 Full-closed refuse burning method and device
CN108224450A (en) * 2016-12-22 2018-06-29 内蒙古大学 Fully closed garbage incineration method and its device
CN108315081A (en) * 2018-04-08 2018-07-24 源创环境科技有限公司 The RDF production systems of aging rubbish are dried using the landfill gas of refuse landfill
CN108315081B (en) * 2018-04-08 2023-11-28 源创环境科技有限公司 RDF production system for drying stale garbage by using landfill gas of garbage landfill
CN109373324A (en) * 2018-11-27 2019-02-22 中国中元国际工程有限公司 A kind of garbage disposal association system and method
CN110822437A (en) * 2019-11-07 2020-02-21 光大环保技术研究院（南京）有限公司 Waste incineration power generation system and method
CN111360022A (en) * 2020-03-17 2020-07-03 江苏和合环保集团有限公司 Landfill method beneficial to comprehensive treatment of household garbage
CN112871964A (en) * 2021-01-08 2021-06-01 光大环保（中国）有限公司 Meal kitchen and burn integration and deal with device in coordination

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