CN107062240A - The system and method for Thermal generation unit cooperated with consumer waste pyrolysis - Google Patents
The system and method for Thermal generation unit cooperated with consumer waste pyrolysis Download PDFInfo
- Publication number
- CN107062240A CN107062240A CN201710249980.2A CN201710249980A CN107062240A CN 107062240 A CN107062240 A CN 107062240A CN 201710249980 A CN201710249980 A CN 201710249980A CN 107062240 A CN107062240 A CN 107062240A
- Authority
- CN
- China
- Prior art keywords
- pyrolysis
- generation unit
- thermal generation
- combustion
- boiler
- 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
- F23G5/0273—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage using indirect heating
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C1/00—Combustion apparatus specially adapted for combustion of two or more kinds of fuel simultaneously or alternately, at least one kind of fuel being either a fluid fuel or a solid fuel suspended in a carrier gas or air
- F23C1/04—Combustion apparatus specially adapted for combustion of two or more kinds of fuel simultaneously or alternately, at least one kind of fuel being either a fluid fuel or a solid fuel suspended in a carrier gas or air lump and gaseous fuel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C1/00—Combustion apparatus specially adapted for combustion of two or more kinds of fuel simultaneously or alternately, at least one kind of fuel being either a fluid fuel or a solid fuel suspended in a carrier gas or air
- F23C1/12—Combustion apparatus specially adapted for combustion of two or more kinds of fuel simultaneously or alternately, at least one kind of fuel being either a fluid fuel or a solid fuel suspended in a carrier gas or air gaseous and pulverulent fuel
-
- 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
-
- 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
- F23G5/033—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment comminuting or crushing
-
- 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
- F23G5/04—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment drying
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/30—Pyrolysing
- F23G2201/303—Burning pyrogases
-
- 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
- F23G2201/00—Pretreatment
- F23G2201/80—Shredding
-
- 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
- Y02E20/12—Heat utilisation in combustion or incineration of waste
Abstract
The invention discloses a kind of system and method for Thermal generation unit cooperated with consumer waste pyrolysis, the part high-temperature flue gas that extraction Thermal generation unit boiler is produced is sent directly into pyrolysis installation and the house refuse of its inside is pyrolyzed, burner region or its top that combustion gas after pyrolysis is introduced in Thermal generation unit boiler, coal combustion is aided in, steady combustion is realized or fires again.The present invention directly utilizes coal unit existing weaponry and equipment, by superfluous production capacity and domestic garbage resource using organically combining, reduces garbage disposal cost of investment, while solving coal-burning power plant's low-load combustion-stabilizing, combustion retrofit investment, realizes maximizing the benefits.
Description
Technical field
The present invention relates to a kind of system and method for Thermal generation unit cooperated with consumer waste pyrolysis.
Background technology
As economic develops rapidly, the continuous intensification of Development of China's Urbanization, generation sustainable growth house refuse
The soil body is taken, environment is polluted, also has negative effect to the health of people.Generated electricity right and wrong using burning domestic garbage
The processing method usually seen.Part is saved, autonomous region also issues《On further strengthening burning city domestic garbage processing work
Opinion》, it is desirable to the processing of house refuse, in principle without exception from burning (generating) treatment technology.
But, the disposal ability of existing municipal solid waste incinerator is not enough, according to opinion, and various regions need a large amount of build
Incineration plant, invests huge, construction is complicated.Current life refuse processing method, be all house refuse is crushed, sorted,
Desiccation, after, send into special waste incinerator and burnt, above-mentioned technology all has problems with:
(1) a large amount of bioxin are produced, and bioxin is difficult that natural degradation is eliminated in environment, with very strong toxicity, is had
Dioxins concentration in investigation display, waste incineration practitioner's blood is 806pgTEQ/L, is 40 times of left sides of normal population level
It is right;Being discharged into bioxin in atmospheric environment can adsorb on particulate matter, be deposited to water body and soil, then pass through food chain
Enrichment enter human body, endanger the health and environment of people;
(2) substantial amounts of N0 is producedXDeng other pollutants, pollute the environment, and the pollutant process equipment investment of incineration plant
Amount is big, and input cost is high;
(3) large-scale incineration plant is built, it is necessary to put into boiler and its corollary system, input cost is high, take substantial amounts of city
Or urban land, investment is greatly.
At the same time, with the economic slowdown in growth of China, electricity consumption is not enough, and production capacity surplus, generating set occurs in coal-burning power plant
Utilize hourage and utilization rate of equipment and installations continuous slide.How to improve utilization rate of equipment and installations and improve economy of power plant and social benefit undoubtedly
It is significant.Simultaneously as unit utilizes the decline of hourage, the boiler of coal-burning power plant is low negative often in underrun
Boiler often combustion instability under lotus.How to ensure that surely combustion is also major issue urgently to be resolved hurrily at present to boiler.In addition, coal-fired electricity
The pollutant disposal system that factory has in itself is very complete and efficient, due to the underrun of unit, and its utilization rate is not enough, difficult
To play optimum efficiency.
If in the newly-built domestic garbage gasification device in existing coal-burning power plant, the high-temperature flue gas gasification produced using boiler of power plant is given birth to
Rubbish living, is not only effectively utilized the waste heat of the high-temperature flue gas of power plant's generation, improves the service efficiency of electric power factory equipment, Er Qiejie
Thermal source and energy expenditure (generally requiring to mix burning coal) and the newly-built pollutant process system of conventional municipal solid waste incinerator are saved
The significant cost of system.In addition, the combustion gas that gasification is produced, which can return to boiler, carries out the steady combustion of burning realization, while taking into account NOXReduction,
Also there is very big benefit for normal run of underload of boiler.Therefore, the gasification of Thermal generation unit cooperated with consumer waste has many
Weight benefit, achieves many things at one stroke.Domestic garbage burning electricity generation can be combined with coal-burning power plant's unit.
The content of the invention
The present invention is in order to solve the above problems, it is proposed that a kind of system of Thermal generation unit cooperated with consumer waste pyrolysis and
Method, the present invention is directly using the existing boiler plant of coal-burning power plant, and the high-temperature flue gas that boiler is produced introduces heat as thermal source
Device is solved, high temperature incineration is carried out for the pyrolysis of house refuse, then by the combustion gas feeding boiler after pyrolysis, suppresses two from source
The precipitation of Evil English, the problem of not only having handled house refuse but also solved boiler low load stable combustion.
To achieve these goals, the present invention is adopted the following technical scheme that:
A kind of system of Thermal generation unit cooperated with consumer waste pyrolysis, extracts the part that Thermal generation unit boiler is produced
High-temperature flue gas is sent directly into pyrolysis installation and the house refuse of its inside is pyrolyzed, and the combustion gas after pyrolysis introduces coal fired power generation machine
Burner region in group boiler, aids in coal combustion, realizes steady combustion.By the way that combustion gas is introduced into combustor section, it can realize
Steady combustion, the problem of solving boiler low load stable combustion.
Further, the combustion gas introduces boiler furnace top by high-temperature fuel gas blower fan, using fractional combustion mode, suppression
NOx generation in stove processed, realizes the low NOx drainage of coal-fired plant boiler.
Further, the gasification installation is pyrolysis oven.
Further, the gasification installation includes drying device, and house refuse is dried into processing.
House refuse first passes through the processing such as sorting, crushing and drying in advance.
A kind of system of Thermal generation unit cooperated with consumer waste pyrolysis, extracts the part that Thermal generation unit boiler is produced
High-temperature flue gas is sent directly into pyrolysis installation and the house refuse of its inside is pyrolyzed, and the combustion gas after pyrolysis introduces coal fired power generation machine
The top of burner region in group boiler, then fired.Denitration, reduction nitrogen oxides are can aid in by again firing
Discharge capacity, realizes energy-saving and environmental protection.
A kind of method of Thermal generation unit cooperated with consumer waste pyrolysis, the part that Thermal generation unit boiler is produced is high
Warm flue gas is sent directly into pyrolysis installation and the house refuse of its inside is pyrolyzed, and will be pyrolyzed in the combustion gas introducing boiler produced
Burner region, aids in coal combustion, realizes steady combustion, the problem of solving low-load combustion-stabilizing.
A kind of method of Thermal generation unit cooperated with consumer waste pyrolysis, the part that Thermal generation unit boiler is produced is high
Warm flue gas feeding pyrolysis installation is pyrolyzed to the house refuse of its inside, will be pyrolyzed the burning in the combustion gas introducing boiler produced
The upper end of device region, then fired.
The temperature of high-temperature flue gas is 600-1000 DEG C.
The introduction volume of high-temperature flue gas confirms and adjusted according to its temperature.
Compared with prior art, beneficial effects of the present invention are:
(1) the existing boiler plant in coal-burning power plant is burnt the high-temperature flue gas generated as thermal source by the present invention is used for life rubbish
The pyrolysis of rubbish, then the above-mentioned boiler plant of combustion gas feeding being pyrolyzed after producing is burnt, it is not necessary to multiple incineration plants are set up, just
Disposal of resources efficiently, inexpensive can be carried out to house refuse, domestic and international technological gap is filled up;
(2) recycling of the processing of house refuse and the superfluous resource of Thermal generation unit is combined by the present invention, can profit
With a small amount of high temperature flue-gas from boiler heat, so as to slightly reduce power generating capacity and generating hourage, this and current power plant
Situation matches.
(3) in the cost input of equipment, only only need to additionally increase a pyrolysis oven, without carrying out large-scale equipment
Transformation and research and development, by combustion gas loopback boiler, solve the steady combustion problem under coal-burning power plant's underload, realize maximizing the benefits;
(4) spray boiler implementation fractional combustion is returned in the combustion gas produced using refuse pyrolysis, contributes to reduction to produce tar, N0X
Deng the discharge of pollutant so that boiler is more environmentally friendly.Furthermore, it is not necessary that independent newly-built Pollution in Municipal Solid Waste Incineration processing system, available
Power plant's existing pollutant disposal system in itself, improves the utilization ratio of equipment, integrated cost is substantially reduced.
(5) traditional waste incineration and generating electricity technology, is to be carried out in oxidizing atmosphere, it is to be difficult to avoid that to produce dioxin
's.But in refuse pyrolysis burning process, completely cut off oxygen, the condition element of dioxin generation has been essentially eliminated, so that in rubbish
Dioxin generation is largely avoided on the source that rubbish is burned.Even if pyrolytic process generates a small amount of bioxin, also may be used
Decomposed in boiler by high-temp combustion, it is ensured that the complete decomposition combustion at high temperature of the poisonous organic gas such as dioxin.
Brief description of the drawings
The Figure of description for constituting the part of the application is used for providing further understanding of the present application, and the application's shows
Meaning property embodiment and its illustrate be used for explain the application, do not constitute the improper restriction to the application.
Fig. 1 is the structural representation of the first embodiment of the present invention;
Fig. 2 is the structural representation of second of embodiment of the present invention;
Wherein:1st, drying device, 2, pyrolysis oven, 3, high-temperature fuel gas blower fan, 4, burning boiler, 5, burner, 6, steam turbine,
7th, generator, 8, air preheater, 9, high-temperature flue gas, 10, lime-ash, 11, the flue gas of discharge, 12, the combustion gas after pyrolysis, 13, place
House refuse after reason, 14, flue.
Embodiment:
The invention will be further described with embodiment below in conjunction with the accompanying drawings.
It is noted that described further below is all exemplary, it is intended to provide further instruction to the application.Unless another
Indicate, all technologies used herein and scientific terminology are with usual with the application person of an ordinary skill in the technical field
The identical meanings of understanding.
It should be noted that term used herein above is merely to describe embodiment, and be not intended to restricted root
According to the illustrative embodiments of the application.As used herein, unless the context clearly indicates otherwise, otherwise singulative
It is also intended to include plural form, additionally, it should be understood that, when in this manual using term "comprising" and/or " bag
Include " when, it indicates existing characteristics, step, operation, device, component and/or combinations thereof.
As background technology is introduced, house refuse combustion technology present in prior art is all present can not be from source
Bioxin, and the deficiency that input cost is huge, building renovation is larger are removed, in order to solve technical problem as above, the application
Propose a kind of Thermal generation unit cooperated with consumer waste pyrolysis system and method.
In a kind of typical embodiment of the application, lived as shown in Figure 1 there is provided a kind of collaboration of Thermal generation unit
Refuse pyrolysis system, the part high-temperature flue gas that Thermal generation unit boiler is produced is sent directly into life of the pyrolysis installation to its inside
Rubbish is pyrolyzed, the burner region that the combustion gas after pyrolysis is introduced in Thermal generation unit boiler, aids in coal combustion, real
Now steady combustion.By the way that combustion gas is introduced into combustor section, steady combustion can be realized, the problem of solving boiler low load stable combustion.
Flue in boiler introduces bypass, is sent into pyrolysis installation in high-temperature flue gas, bypass and is provided with control valve, with
Control the conveying capacity of flue gas.
Air preheater is provided with flue simultaneously, flue gas is discharged after passing through air preheater.
Combustion gas is introduced in boiler by high-temperature fuel gas blower fan.
Pyrolysis installation is pyrolysis oven.
Pyrolysis installation includes lifting device, and house refuse is sent into its processing region.
House refuse first passes through the processing such as sorting, crushing and drying in advance.
The steam produced after firing again is sent into steam turbine by the existing equipment of coal-burning power plant and generated electricity.
A kind of Thermal generation unit cooperated with consumer waste method for pyrolysis, the part high temperature that Thermal generation unit boiler is produced
Flue gas is sent directly into pyrolysis installation and the house refuse of its inside is pyrolyzed, and will be pyrolyzed the combustion in the combustion gas introducing boiler produced
Burner region, aids in coal combustion, realizes steady combustion, the problem of solving low-load combustion-stabilizing.
The temperature of high-temperature flue gas is 600-1000 DEG C.
The introduction volume of high-temperature flue gas confirms and adjusted according to its temperature.
Pyrolysis installation has deslagging part.
Wherein, pyrolysis installation, air preheater, high-temperature fuel gas blower fan etc. use existing device.
As described in Figure 2, there is provided a kind of Thermal generation unit cooperated with consumer waste for second of exemplary embodiment of the invention
Pyrolysis system, the part high-temperature flue gas that Thermal generation unit boiler is produced is sent directly into house refuse of the pyrolysis installation to its inside
It is pyrolyzed, the burner region top that the combustion gas after pyrolysis is introduced in Thermal generation unit boiler is surely fired.
Simultaneously there is provided a kind of Thermal generation unit cooperated with consumer waste method for pyrolysis, Thermal generation unit boiler is produced
Part high-temperature flue gas be sent directly into pyrolysis installation the house refuse of its inside be pyrolyzed, the combustion gas produced will be pyrolyzed and introduced
The top of burner region in boiler, then fired.By fire again can aid in denitration, reduce nitrogen oxides row
High-volume, energy-saving and environmental protection are realized.
The temperature of high-temperature flue gas is 600-1000 DEG C.
The introduction volume of high-temperature flue gas confirms and adjusted according to its temperature.
The preferred embodiment of the application is the foregoing is only, the application is not limited to, for the skill of this area
For art personnel, the application can have various modifications and variations.It is all within spirit herein and principle, made any repair
Change, equivalent substitution, improvement etc., should be included within the protection domain of the application.
Although above-mentioned the embodiment of the present invention is described with reference to accompanying drawing, not to present invention protection model
The limitation enclosed, one of ordinary skill in the art should be understood that on the basis of technical scheme those skilled in the art are not
Need to pay various modifications or deform still within protection scope of the present invention that creative work can make.
Claims (10)
1. a kind of Thermal generation unit cooperated with consumer waste pyrolysis system, it is characterized in that:The portion that Thermal generation unit boiler is produced
Divide high-temperature flue gas to be sent directly into pyrolysis installation to be pyrolyzed the house refuse of its inside, the combustion gas after pyrolysis introduces coal fired power generation
Burner region in unit boiler, aids in coal combustion, realizes steady combustion.
2. a kind of Thermal generation unit cooperated with consumer waste pyrolysis system as claimed in claim 1, it is characterized in that:The combustion gas
Introduced by high-temperature fuel gas blower fan in boiler.
3. a kind of Thermal generation unit cooperated with consumer waste pyrolysis system as claimed in claim 1, it is characterized in that:The pyrolysis
Device is pyrolysis oven.
4. a kind of Thermal generation unit cooperated with consumer waste pyrolysis system as claimed in claim 1, it is characterized in that:The gasification
Device includes drying device, and house refuse is dried into processing.
5. a kind of Thermal generation unit cooperated with consumer waste pyrolysis system, it is characterized in that:The portion that Thermal generation unit boiler is produced
Divide high-temperature flue gas to be sent directly into pyrolysis installation to be pyrolyzed the house refuse of its inside, the combustion gas after pyrolysis introduces coal fired power generation
The top of burner region in unit boiler, then fired.
6. a kind of Thermal generation unit cooperated with consumer waste method for pyrolysis, it is characterized in that:Thermal generation unit boiler is produced
Part high-temperature flue gas is sent directly into pyrolysis installation and the house refuse of its inside is pyrolyzed, and the combustion gas for being pyrolyzed generation is introduced into pot
Burner region in stove, aids in coal combustion, realizes steady combustion, the problem of solving low-load combustion-stabilizing.
7. a kind of Thermal generation unit cooperated with consumer waste method for pyrolysis, it is characterized in that:Thermal generation unit boiler is produced
Part high-temperature flue gas is sent directly into pyrolysis installation and the house refuse of its inside is pyrolyzed, and the combustion gas for being pyrolyzed generation is introduced into pot
The top of burner region in stove, then fired, realize the low NOx drainage of boiler.
8. a kind of Thermal generation unit cooperated with consumer waste method for pyrolysis as claimed in claims 6 or 7, it is characterized in that:High temperature
The temperature of flue gas is 600-1000 DEG C.
9. a kind of Thermal generation unit cooperated with consumer waste method for pyrolysis as claimed in claims 6 or 7, it is characterized in that:High temperature
The introduction volume of flue gas confirms and adjusted according to its temperature.
10. a kind of Thermal generation unit cooperated with consumer waste method for pyrolysis as claimed in claims 6 or 7, it is characterized in that:Life
Rubbish first passes through sorting, crushes and dries pretreatment in advance.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710249980.2A CN107062240A (en) | 2017-04-17 | 2017-04-17 | The system and method for Thermal generation unit cooperated with consumer waste pyrolysis |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710249980.2A CN107062240A (en) | 2017-04-17 | 2017-04-17 | The system and method for Thermal generation unit cooperated with consumer waste pyrolysis |
Publications (1)
Publication Number | Publication Date |
---|---|
CN107062240A true CN107062240A (en) | 2017-08-18 |
Family
ID=59600129
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201710249980.2A Pending CN107062240A (en) | 2017-04-17 | 2017-04-17 | The system and method for Thermal generation unit cooperated with consumer waste pyrolysis |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN107062240A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113862007A (en) * | 2021-09-24 | 2021-12-31 | 中国科学院广州能源研究所 | Industrial organic solid waste pyrolysis gasification and coal-fired cogeneration coupling method |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5937652A (en) * | 1992-11-16 | 1999-08-17 | Abdelmalek; Fawzy T. | Process for coal or biomass fuel gasification by carbon dioxide extracted from a boiler flue gas stream |
CN202411083U (en) * | 2012-02-23 | 2012-09-05 | 南京凯盛开能环保能源有限公司 | High-temperature-air and efficient gasification collaborated waste pressing system by combining cement kiln and rotary furnace |
CN105838401A (en) * | 2015-01-14 | 2016-08-10 | 烟台龙源电力技术股份有限公司 | Method and system for processing pollutant resulting from coal fines pyrolysis and boiler combustion system |
CN106247342A (en) * | 2016-09-30 | 2016-12-21 | 上海垒锦环境科技中心 | Coal and house refuse coupling combustion system |
CN207035138U (en) * | 2017-04-17 | 2018-02-23 | 山东大学 | The system of Thermal generation unit cooperated with consumer waste pyrolysis |
-
2017
- 2017-04-17 CN CN201710249980.2A patent/CN107062240A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5937652A (en) * | 1992-11-16 | 1999-08-17 | Abdelmalek; Fawzy T. | Process for coal or biomass fuel gasification by carbon dioxide extracted from a boiler flue gas stream |
CN202411083U (en) * | 2012-02-23 | 2012-09-05 | 南京凯盛开能环保能源有限公司 | High-temperature-air and efficient gasification collaborated waste pressing system by combining cement kiln and rotary furnace |
CN105838401A (en) * | 2015-01-14 | 2016-08-10 | 烟台龙源电力技术股份有限公司 | Method and system for processing pollutant resulting from coal fines pyrolysis and boiler combustion system |
CN106247342A (en) * | 2016-09-30 | 2016-12-21 | 上海垒锦环境科技中心 | Coal and house refuse coupling combustion system |
CN207035138U (en) * | 2017-04-17 | 2018-02-23 | 山东大学 | The system of Thermal generation unit cooperated with consumer waste pyrolysis |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113862007A (en) * | 2021-09-24 | 2021-12-31 | 中国科学院广州能源研究所 | Industrial organic solid waste pyrolysis gasification and coal-fired cogeneration coupling method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN105032884B (en) | Cement rotary kiln collaboration processes house refuse and energy comprehensive utilization system and method | |
CN102705837B (en) | System and method for collaborative garbage disposal of cement clinker production line | |
CN205048449U (en) | Processing system of grate type waste incinerator multifuel combustion mud | |
CN108278617A (en) | Municipal refuse cyclone burning system and its coupling coal fired power plant electricity generation system and method | |
CN108534142A (en) | A kind of refuse pyrolysis gasification burning chimney-free Zero discharging system | |
CN2795672Y (en) | Three burning type burning processing system for liquid and solid waste materials | |
CN106940017A (en) | The system and method for coal-burning power plant's cooperated with consumer waste gasification | |
CN101737784B (en) | Method for mixed burning of agriculture and forestry waste, sludge and household garbage by using grate furnace | |
CN208282120U (en) | Coal cooperates with combustion power generation system with rubbish | |
CN105351019A (en) | Power generation technique based on pyrolyzation and gasification of refuse derived fuel (RDF) prepared from household refuse and incineration of fuel gas | |
CN207035138U (en) | The system of Thermal generation unit cooperated with consumer waste pyrolysis | |
CN201992665U (en) | Electrical heating incineration type medical treatment waste incinerator | |
CN206626580U (en) | The system of coal-burning power plant's cooperated with consumer waste gasification | |
CN107062240A (en) | The system and method for Thermal generation unit cooperated with consumer waste pyrolysis | |
CN208332277U (en) | Municipal refuse cyclone burning system and its coupling coal fired power plant electricity generation system | |
CN204026685U (en) | One way of life high temperature garbage anaerobism pyrolysis system | |
CN202188512U (en) | Urban household garbage combustion power generating system | |
CN201093506Y (en) | Incinerator | |
CN202719614U (en) | Cement clinker production line co-processing garbage system | |
CN203980293U (en) | A kind of cement kiln associated treatment combustible waste material and the power generation complemented system of bypass | |
CN206572533U (en) | A kind of device of cement kiln synergic processing house refuse exhaust gas volumn equivalent displacement | |
CN101704014B (en) | Dispersed disposal system and disposal method of household wastes in small towns | |
CN208535995U (en) | Domestic garbage gasification burns integrated incinerator | |
CN206540134U (en) | A kind of solid waste pyrolysis and combustion system | |
CN202660560U (en) | 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 |