CN108300517A - It is a kind of to utilize pyrolysis of waste vaporized carbon elelctrochemical power generation device - Google Patents
It is a kind of to utilize pyrolysis of waste vaporized carbon elelctrochemical power generation device Download PDFInfo
- Publication number
- CN108300517A CN108300517A CN201810296120.9A CN201810296120A CN108300517A CN 108300517 A CN108300517 A CN 108300517A CN 201810296120 A CN201810296120 A CN 201810296120A CN 108300517 A CN108300517 A CN 108300517A
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- Prior art keywords
- carbon
- waste
- gasification
- thermal decomposition
- waste heat
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 126
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 108
- 239000002699 waste material Substances 0.000 title claims abstract description 92
- 238000010248 power generation Methods 0.000 title claims abstract description 51
- 238000000197 pyrolysis Methods 0.000 title claims abstract description 45
- 238000002309 gasification Methods 0.000 claims abstract description 145
- 239000007789 gas Substances 0.000 claims abstract description 111
- 239000002918 waste heat Substances 0.000 claims abstract description 110
- 238000002485 combustion reaction Methods 0.000 claims abstract description 90
- 238000005979 thermal decomposition reaction Methods 0.000 claims abstract description 90
- 238000010000 carbonizing Methods 0.000 claims abstract description 65
- 238000004064 recycling Methods 0.000 claims abstract description 57
- 238000007781 pre-processing Methods 0.000 claims abstract description 44
- 230000005611 electricity Effects 0.000 claims abstract description 34
- 239000000463 material Substances 0.000 claims abstract description 26
- 238000011084 recovery Methods 0.000 claims abstract description 24
- 238000001035 drying Methods 0.000 claims description 41
- 239000002994 raw material Substances 0.000 claims description 39
- 238000001816 cooling Methods 0.000 claims description 30
- 238000006243 chemical reaction Methods 0.000 claims description 23
- 239000010881 fly ash Substances 0.000 claims description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 19
- 239000000567 combustion gas Substances 0.000 claims description 18
- 230000015572 biosynthetic process Effects 0.000 claims description 15
- 238000003786 synthesis reaction Methods 0.000 claims description 15
- 238000010438 heat treatment Methods 0.000 claims description 11
- 238000003860 storage Methods 0.000 claims description 11
- 238000003763 carbonization Methods 0.000 claims description 10
- 239000000779 smoke Substances 0.000 claims description 10
- 235000019738 Limestone Nutrition 0.000 claims description 9
- 238000007599 discharging Methods 0.000 claims description 9
- 239000006028 limestone Substances 0.000 claims description 9
- 239000000446 fuel Substances 0.000 claims description 8
- 238000012856 packing Methods 0.000 claims description 8
- 239000010865 sewage Substances 0.000 claims description 8
- WTHDKMILWLGDKL-UHFFFAOYSA-N urea;hydrate Chemical compound O.NC(N)=O WTHDKMILWLGDKL-UHFFFAOYSA-N 0.000 claims description 8
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 7
- 239000003546 flue gas Substances 0.000 claims description 7
- 238000005520 cutting process Methods 0.000 claims description 6
- 239000004615 ingredient Substances 0.000 claims description 6
- 238000009434 installation Methods 0.000 claims description 4
- 238000011068 loading method Methods 0.000 claims description 4
- 235000019504 cigarettes Nutrition 0.000 claims description 2
- 239000002154 agricultural waste Substances 0.000 abstract description 8
- 239000010920 waste tyre Substances 0.000 abstract description 8
- 239000002351 wastewater Substances 0.000 abstract description 6
- 230000000694 effects Effects 0.000 description 8
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 7
- 239000004202 carbamide Substances 0.000 description 7
- 239000003245 coal Substances 0.000 description 7
- 238000012545 processing Methods 0.000 description 7
- 150000001722 carbon compounds Chemical class 0.000 description 5
- 238000002360 preparation method Methods 0.000 description 5
- 239000002956 ash Substances 0.000 description 4
- 230000008901 benefit Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 229920003023 plastic Polymers 0.000 description 4
- 239000004033 plastic Substances 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 239000010828 animal waste Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000004880 explosion Methods 0.000 description 3
- -1 municipal refuse Substances 0.000 description 3
- 239000010883 coal ash Substances 0.000 description 2
- 239000003034 coal gas Substances 0.000 description 2
- 238000004891 communication Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000002737 fuel gas Substances 0.000 description 2
- 239000002296 pyrolytic carbon Substances 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 2
- 229920002554 vinyl polymer Polymers 0.000 description 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000010849 combustible waste Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000003925 fat Substances 0.000 description 1
- 210000003608 fece Anatomy 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 238000010079 rubber tapping Methods 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/58—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels combined with pre-distillation of the fuel
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/72—Other features
- C10J3/86—Other features combined with waste-heat boilers
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0903—Feed preparation
- C10J2300/0906—Physical processes, e.g. shredding, comminuting, chopping, sorting
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0903—Feed preparation
- C10J2300/0909—Drying
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/16—Integration of gasification processes with another plant or parts within the plant
- C10J2300/1671—Integration of gasification processes with another plant or parts within the plant with the production of electricity
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/16—Integration of gasification processes with another plant or parts within the plant
- C10J2300/1687—Integration of gasification processes with another plant or parts within the plant with steam generation
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Gasification And Melting Of Waste (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The present invention discloses a kind of utilization pyrolysis of waste vaporized carbon elelctrochemical power generation device, including Material supply system, feedstock pre-processing system, thermally decompose carbonizing plant, combustion gasification apparatus, waste heat recycling system, carbon recovery system and gas gasification electricity generation system, the Material supply system is connect with the feedstock pre-processing system for dry feedstock, the feedstock pre-processing system is connect with the thermal decomposition carbonizing plant, the thermal decomposition carbonizing plant is connect with the combustion gasification apparatus, the combustion gasification apparatus is connect with the waste heat recycling system, the thermal decomposition carbonizing plant and the gas gasification electricity generation system, combustion gasification apparatus is connected with the carbon recovery system.A kind of utilization pyrolysis of waste vaporized carbon elelctrochemical power generation apparatus structure of the invention is simple, can make full use of waste tire and agricultural wastes generate electricity, it effectively reduces waste water content simultaneously and is recycled heat is generated again, the energy is effectively saved, avoids catching fire and explode.
Description
Technical field
The present invention relates to a kind of power generator, and pyrolysis of waste vaporized carbon elelctrochemical power generation device is utilized more particularly to a kind of.
Background technology
In general, it is pyrolyzed using horizontal combustion gas furnace and the waste that gasifies, the heating revolving kiln pyrolysis gasification furnace uses
Heat release rotary kiln pyrolysis gasification furnace with inclined surface, the inclined surface rotate waste using high heat, solid when introducing
When body waste, pyrolysis of waste and high-temperature gasification.In such hot rotary kiln, pyrolytic gasification should be in anoxic and anoxic
Under conditions of carry out, generate a certain amount of gas and residue, however introduce air into cracking gasification furnace, there are prodigious fire
Danger, high temperature thermal shocking, and generate risk of explosion.
It is that fuel carries out gasification and newer method to waste, in order to subtract by this hot rotary kiln pyrogenation gasification furnace
Less by thermal shock phenomenon, much less the service life (run time) of pyrolysis gasification furnace and generating equipment caused by exploding, needs many
Gas flow is maintained high temperature by heat source, the problem of leading to poor thermal efficiency.
Invention content
The present invention is completed to solve in the prior art insufficient, and the object of the present invention is to provide a kind of letters of structure
List can make full use of waste tire and agricultural wastes power generation, while effectively reducing waste water content and will generate heat
It recycles again, effectively saves the energy, avoid catching fire and what is occurred situations such as explosion utilizes pyrolysis of waste gasification carbonization hair
Electric installation.
The a kind of of the present invention utilizes pyrolysis of waste vaporized carbon elelctrochemical power generation device, including Material supply system, raw material to locate in advance
Reason system, thermal decomposition carbonizing plant, combustion gasification apparatus, waste heat recycling system, gasification power generation system, carbon recovery system and
Gas gasification electricity generation system, the Material supply system is connect with the feedstock pre-processing system for dry feedstock, described
Feedstock pre-processing system is connect with the thermal decomposition carbonizing plant, and the thermal decomposition carbonizing plant connects with the combustion gasification apparatus
It connects, the combustion gasification apparatus is connect with the waste heat recycling system, the thermal decomposition carbonizing plant and the combustion gas gas
Elelctrochemical power generation system, the gasification power generation system are connected with the carbon recovery system.
The a kind of of the present invention can also be using pyrolysis of waste vaporized carbon elelctrochemical power generation device：
The thermal decomposition carbonizing plant, the combustion gasification apparatus and the waste heat recycling system with the raw material
Pretreatment system connects.
The feedstock pre-processing system includes drying machine and drying hot-blast stove, the drying machine front and back end respectively with it is described
Material supply system is connected with the thermal decomposition carbonizing plant by device for transporting objects, and the drying hot-blast stove is done with described
Dry machine connection, the thermal decomposition carbonizing plant, the combustion gasification apparatus and the waste heat recycling system are done with described
Dry to be connected to hot-blast stove gas fed, the drying machine is connected to the combustion gasification apparatus burning gases input type, described
Drying machine is connected to the waste heat recycling system dry flue gas input type.
The thermal decomposition carbonizing plant includes thermally decomposing carbide furnace, thermal decomposition hot-blast stove and quick cooling device, described
Drying machine is connect with the input terminal material input type of the thermal decomposition carbide furnace, the combustion gasification apparatus and thermal decomposition carbide furnace
Gas fed is connected to, and the output end of the thermal decomposition carbide furnace is connected to the quick cooling device, the rapid cooling dress
Upper end is set to be connected to the gas gasification electricity generation system and the combustion gasification apparatus respectively, the quick cooling device lower end with
The carbon recovery system connection, the thermal decomposition hot-blast stove are connected to the thermal decomposition carbide furnace input terminal.
Heat exchanger, the heat exchanger difference are provided between the combustion gasification apparatus and the thermal decomposition carbide furnace
Be connected to the combustion gasification apparatus, the thermal decomposition carbide furnace and the waste heat recycling system, the heat exchanger with
Exchange hair-dryer for ambient atmos to be delivered to heat exchanger is connected to.
The combustion gasification apparatus includes gasification combustion furnace, and the gasification combustion furnace middle and lower part is filled with recyclable fuel storage
It sets and is connected to the thermal decomposition carbonizing plant, the gasification combustion furnace middle and upper part is connected to the feedstock pre-processing system, described
Gasification combustion furnace top is connected to urea water tank, and the top of the gasification combustion furnace is connected to the thermal decomposition carbonizing plant, institute
Gasification combustion furnace lower part is stated to be connected to the carbon recovery system.
The gas gasification electricity generation system includes the Cyclone machines being sequentially communicated, synthesis gas cooling tower, combustion gas heat exchanger, natural pond
Gas bin and gas electricity generator, the Cyclone machines are connected to the thermal decomposition carbonizing plant, the combustion gas heat exchanger with
Sewage treatment equipment is connected to.
The waste heat recycling system includes waste heat boiler, waste heat for supplying device, afterheat steam power generator, waste hot air
Body tapping equipment and waste heat flyash retracting device, the waste heat boiler top are connected to the afterheat steam power generator, institute
It states waste heat boiler output end to be connected to waste heat gas discharging apparatus, the waste heat boiler lower part is filled with waste heat flyash recycling
Connection is set, the afterheat steam power generator is connected to the waste heat for supplying device, and the waste heat boiler is located in advance with the raw material
Manage system connectivity.
The afterheat steam power generator includes steam turbine and steam-driven generator, the steam turbine and with the steam
Retarder is connected between generator, the steam turbine is connected to the waste heat boiler.
The waste heat for supplying device include condenser, heat supply cooling tower, pure water treatment device, high steam distributor and
Heating unit, the condenser are connected to the steam turbine, and the condenser is taken cycle with heat supply cooling and is connected to, described
Condenser is connected to the pure water treatment device, and the pure water treatment device connection connects with the high steam distributor
Logical, the high steam distributor is connected to the heating unit, and the high steam distributor is connected to the steam turbine.
Waste heat gas discharging apparatus includes being loaded into hair-dryer, reaction machine, pressure fan, activated carbon hopper, pulverized limestone hopper, cigarette
Air filter and chimney, the loading hair-dryer are connected to the waste heat boiler, and the hair-dryer is connected to machine is reacted, described anti-
Answer machine to be connected to the feedstock pre-processing system, the activated carbon hopper and the pulverized limestone hopper and pressure fan respectively with institute
The connection of reaction machine is stated, the reaction machine is connected to smoke filter, and the smoke filter is connected to chimney.
The carbon recovery system includes carbon cooler, carbon sorting machine, sorting escaper, carbon recycling conveyor, carbon bin
And packing machine, the carbon cooler are connected to the thermal decomposition carbonizing plant lower part, the carbon sorting machine is located at carbon cooling
At immediately below machine, the carbon sorting machine is connect with the sorting escaper material conveying-type, and the sorting escaper is recycled with carbon
Conveyer connects, and the carbon recycling conveyor is connected to the carbon bin, and the carbon bin is connect with the packing machine.
The Material supply system includes sequentially connected raw material cutting machine, input hopper, ingredient conveyor, raw material sorting
Machine, raw material storage bin hopper and measured quantity dispensing device, the measured quantity dispensing device are connected to the input terminal of the feedstock pre-processing system.
The a kind of of the present invention utilizes pyrolysis of waste vaporized carbon elelctrochemical power generation device, including Material supply system, raw material to locate in advance
Reason system, thermal decomposition carbonizing plant, combustion gasification apparatus, waste heat recycling system, gasification power generation system, carbon recovery system and
Gas gasification electricity generation system, the Material supply system is connect with the feedstock pre-processing system for dry feedstock, described
Feedstock pre-processing system is connect with the thermal decomposition carbonizing plant, and the thermal decomposition carbonizing plant connects with the combustion gasification apparatus
It connects, the combustion gasification apparatus is connect with the waste heat recycling system, the thermal decomposition carbonizing plant and the combustion gas gas
Elelctrochemical power generation system, the gasification power generation system are connected with the carbon recovery system.In this way, the effect of Material supply system is to be rear
Continuous technique provides waste material, and the waste material includes waste tire, waste plastics, useless vinyl, sewage and animal excreta
Just, municipal refuse, agricultural wastes, flyash and food refuse etc..Material supply system is to be delivered to above-mentioned waste material
Raw material preprocessing device.And the effect of raw material preprocessing device is that waste material is sorted and dried so that can carry out
The water content of the waste material of the needs of subsequent processing reduces, and the water content of at least required waste material will just may be used less than 10%
Into follow-up equipment, feedstock pre-processing system will carry out pretreated waste materials and be delivered to thermal decomposition carbonizing plant, heat
It decomposes carbonizing plant to be pyrolyzed the waste materials being delivered in it, generates the pyrolysis carbon compound that temperature is 650-700 DEG C
At gas, which is combined to gas and is transported to the gas gasification electricity generation system to generate electricity, and realizes and utilizes waste
The purpose to generate electricity, and the pyrolysis carbonization gas that a part is transferred out from the thermal decomposition carbonizing plant enters combustion gas makeup
Carry out combustion gasification is set, the heat then generated is delivered to the thermal decomposition carbonizing plant in the thermal decomposition carbonizing plant again
Pretreated waste materials be pyrolyzed, pyrolysis carbonization gas can be recycled in this way, further increase pyrolysis gas
Body (being pyrolyzed carbonization gas) utilization rate reduces energy consumption.And combustion gasification apparatus is connect with the waste heat recycling system, then
It will be delivered to the waste heat recycling system after heat heat exchange in the synthesis gas of gasification and carry out waste heat recycling, utilize this
A little waste heats, which can have, to be acted on：The hot gas that high heat is contained in first this part can be delivered to feedstock pre-processing system pair
Processing is dried in waste materials, saves heat used in dry waste raw material, reduces cost.Second this partial heat
Steam generating system can be delivered to and carry out steam-electric power, gas gasification power generation existing in this way has steam-electric power, generating efficiency again
Height, the energy make full use of, while can also convert this partial heat to steam or hot water, to industry and civilian heat supply and
Heating provides heat；Third can also be prepares flyash using this partial heat.Certain a part of hot gas after treatment may be used
To be discharged into air.And it thermally decomposes the slag being discharged in carbonizing plant and carbon and carbide is carried out by the carbon recovery system being attached thereto
Preparation and recycling, the coal of clean environment firendly can be prepared.Utilize in this way includes waste tire, waste plastics, useless vinyl, sewage
It can generate electricity with animal wastes, municipal refuse, agricultural wastes and food refuse the like waste raw material, heat supply, prepare wiper ring
Coal is protected, while the heat generated in preparation process can also be comprehensively utilized and reused.The energy is made full use of, energy is saved
Source simultaneously generates good economic benefit.Simultaneously because processing is dried in waste materials in feedstock pre-processing system so that
The humidity of waste materials is less than 10%, therefore it is possible to prevente effectively from catching fire and explode during after burning and gasification
Phenomenon occurs, and effectively improves the safety of integral device.The a kind of of the present invention utilizes pyrolysis of waste vaporized carbon elelctrochemical power generation device,
Compared with the existing technology the advantages of is：It is simple in structure, can make full use of waste tire and agricultural wastes power generation, while effectively
It reduces waste water content and is recycled heat is generated again, effectively save the energy, avoid catching fire and be sent out situations such as explosion
It is raw.
Description of the drawings
Fig. 1 present invention is a kind of to utilize pyrolysis of waste vaporized carbon elelctrochemical power generation apparatus structure schematic diagram.
Figure number explanation
1 ... ingredient conveyor 2 ... raw material cutting machine 3 ... puts into hopper
4 ... raw material sorting machine 5 ... raw material storage bin hopper 6 ... measured quantity dispensing devices
7 ... drying machines 8 ... are dry to use hot-blast stove 9 ... device for transporting objects
10 ... dried object bins 11 ... thermally decompose carbide furnace 12 ... thermal decomposition hot-blast stove
13 ... quick cooling device 14 ... heat exchangers 15 ... exchange hair-dryer
16 ... gasification combustion furnace 17 ... urea water tank 18 ... urea nozzles
19 ... waste heat boiler 20 ... steam turbine 21 ... retarders
22 ... steam-driven generator 23 ... condenser 24 ... heat supply cooling towers
25 ... pure water treatment device 26 ... high steam distributor 27 ... heating units
28 ... loading hair-dryer 29 ... reaction machine 30 ... pressure fan 31 ... chimneys
32 ... activated carbon hopper 33 ... pulverized limestone hopper 34 ... smoke filters
35 ... flyash retracting device 36 ... carbon cooler 37 ... carbon sorting machines
38 ... carbon recycling conveyor 39 ... carbon bin 40 ... packing machines
41 ... Cyclone machines 42 ... synthesis gas cooling tower 43 ... combustion gas heat exchangers
44 ... biogas bin 45 ... gas electricity generator 46 ... combustion gas bag filters
47 ... incombustible storage bin hoppers
Specific implementation mode
Fig. 1 below in conjunction with the accompanying drawings makees further a kind of of the present invention using pyrolysis of waste vaporized carbon elelctrochemical power generation device
It is described in detail.
The a kind of of the present invention utilizes pyrolysis of waste vaporized carbon elelctrochemical power generation device, please refers to Fig.1 middle related each figure, including original
Expect supply system, feedstock pre-processing system, thermal decomposition carbonizing plant, combustion gasification apparatus, waste heat recycling system, gasification hair
Electric system, carbon recovery system and gas gasification electricity generation system, the Material supply system and the raw material for being used for dry feedstock
Pretreatment system connects, and the feedstock pre-processing system is connect with the thermal decomposition carbonizing plant, the thermal decomposition carbonizing plant
It is connect with the combustion gasification apparatus, the combustion gasification apparatus is connect with the waste heat recycling system, the thermal decomposition
Carbonizing plant is connect with the gas gasification electricity generation system, the gasification power generation system and the carbon recovery system.In this way, raw material
The effect of supply system is to provide waste material for subsequent technique, and the waste material includes waste tire, waste plastics, useless second
Olefine resin, sewage and animal wastes, municipal refuse, agricultural wastes, flyash and food refuse etc..Material supply system be by
Above-mentioned waste material is delivered to raw material preprocessing device.And the effect of raw material preprocessing device be to waste material carry out sorting and
It is dry so that can to carry out the water content of the waste material of the needs of subsequent processing reduce, at least needed for waste material contain
Water, which will be less than 10%, can just enter follow-up equipment, and feedstock pre-processing system is delivered to pretreated waste materials were carried out
Carbonizing plant is thermally decomposed, the waste materials being delivered in it are carried out pyrolysis carbonization by thermal decomposition carbonizing plant, are generated temperature and are
650-700 DEG C of pyrolytic carbon is combined to gas, the pyrolytic carbon be combined to gas be transported to the gas gasification electricity generation system into
The purpose to generate electricity using waste is realized in row power generation, and a part of from the pyrolysis for thermally decomposing carbonizing plant and transferring out
Carbonization synthetic gas enters combustion gasification apparatus and carries out combustion gasification, and the heat then generated is delivered to the thermal decomposition carbonization again
Device is pyrolyzed the pretreated waste materials in the thermal decomposition carbonizing plant, can recycle pyrolysis in this way
Gas further increases pyrolysis gas utilization rate, reduces energy consumption.And combustion gasification apparatus connects with the waste heat recycling system
It connects, then will be delivered to the waste heat recycling system after the heat heat exchange in the synthesis gas of gasification and carry out waste heat recycling,
Can have using these waste heats and act on：The hot gas that high heat is contained in first this part can be delivered to pretreatment of raw material
Processing is dried to waste materials in system, saves heat used in dry waste raw material, reduces cost.Second this portion
Divide heat that can be delivered to steam generating system and carry out steam-electric power, gas gasification power generation existing in this way has steam-electric power again, sends out
Electrical efficiency is high, and the energy makes full use of, while can also convert this partial heat to steam or hot water, to industrial and civilian
Heat supply and heating provide heat；Third can also be prepares flyash using this partial heat.Certainly a part of hot gas is at
It can be discharged into air after reason.And thermally decompose the slag that is discharged in carbonizing plant by the carbon recovery system being attached thereto carry out carbon and
The preparation and recycling of carbide, can prepare the coal of clean environment firendly.Utilize in this way includes waste tire, waste plastics, useless ethylene tree
Fat, sewage and animal wastes, municipal refuse, agricultural wastes and food refuse the like waste raw material can generate electricity, heat supply, preparation
Clean environment firendly coal, while the heat generated in preparation process can also be comprehensively utilized and reused.The energy is made full use of,
It saves the energy and generates good economic benefit.Simultaneously because place is dried in waste materials in feedstock pre-processing system
Reason so that the humidity of waste materials is less than 10%, therefore it is possible to prevente effectively from catching fire during after burning and gasification
The phenomenon that with exploding, effectively improves the safety of integral device.The a kind of of the present invention utilizes pyrolysis of waste gasification carbonization
Power generator, compared with the existing technology the advantages of be：It is simple in structure, can make full use of waste tire and agricultural wastes hair
Electricity, while effectively reducing waste water content and being recycled heat is generated again, effectively saves the energy, avoid catching fire with it is quick-fried
Situations such as fried, occurs.
The a kind of of the present invention utilizes pyrolysis of waste vaporized carbon elelctrochemical power generation device, please refers to Fig.1 middle related each figure, in front
Can be specifically on the basis of technical solution：The thermal decomposition carbonizing plant, the combustion gasification apparatus and the waste heat recovery
It is connect with the feedstock pre-processing system using system.In this way, the waste materials after feedstock pre-processing system drying process
It is delivered to a part of hot gas in thermal decomposition carbonizing plant being thermally decomposed, and being discharged in feedstock pre-processing system and then enters burning
As burning air in gasification installation, and another part hot gas is then recycled into feedstock pre-processing system again, while heat point
Solution carbonizing plant in a part of burn synthesis gas be also delivered to feedstock pre-processing system be used as after fuel combustion offer heat to
Feedstock pre-processing system makes it that waste materials be dried.And the waste heat in the waste heat recycling system has one
Divide and waste materials are dried also by the feedstock pre-processing system being attached thereto, in this way, feedstock pre-processing system is dry
Dry required heat has sufficient source, effectively save the energy and make full use of heat that the system in whole device generates with
Thermal energy.The technical further preferred technical solution of technical solution is in front：The feedstock pre-processing system includes drying
Machine 7 and dry hot-blast stove 8,7 front and back end of the drying machine are disguised with the Material supply system and the thermally decomposed carbon respectively
It sets and is connected by device for transporting objects 9, the drying is connected to hot-blast stove 8 with the drying machine 7, the thermally decomposed carbon makeup
Set, the combustion gasification apparatus and the waste heat recycling system are connected to the drying with 8 gas fed of hot-blast stove,
The drying machine 7 is connected to the combustion gasification apparatus burning gases input type, the drying machine 7 and the heat recovery
System dry flue gas input type is connected to.Drying machine 7 is for being dried the waste materials being delivered in it, reducing waste
The humidity of raw material subsequently carries out pyrolytic gasification to 10% hereinafter, facilitating, while avoiding feelings that are on fire when pyrolytic gasification or exploding
Condition occurs, and the drying is hot wind of the conveying for dry waste raw material into the drying machine 7 with the effect of hot-blast stove 8
And thermal energy, and thermally decompose carbonizing plant, the waste heat recycling system and combustion gasification apparatus with the drying hot wind
8 gas fed of stove is connected to, in the thermal decomposition carbonizing plant described in this way, combustion gasification apparatus and the waste heat recycling system
Heat and hot gas can be delivered in the drying hot-blast stove 8, and said that the drying hot-blast stove 8 was delivered to drying
Processing is dried to waste materials in machine 7.And the gas that drying machine 7 is discharged can then enter subsequent coal ash for manufacturing for work
Flyash is prepared in skill, certain a portion hot gas can also be again introduced into cycle in the drying hot-blast stove 8, wherein one
Part hot gas can also be used as burning air by the combustion gasification apparatus being connected to drying machine 7 and enter gas in combustion gasification apparatus
Change reaction.And the waste materials after drying are transported in dried object bin 10, are then being transported to the heat
It decomposes carbonizing plant to be thermally decomposed, realizes the purpose of gas gasification power generation.And drying machine 7 and the waste heat recycling system
Connection, then be that dry flue gas is delivered to the waste heat recycling system to prepare flyash.Technical solution is technical in front
Technical solution still more preferably is：The thermal decomposition carbonizing plant includes thermal decomposition carbide furnace 11, thermal decomposition hot-blast stove
12 and quick cooling device 13, the drying machine 7 is connect with the input terminal material input type of the thermal decomposition carbide furnace 11, described
Combustion gasification apparatus is connected to thermal decomposition 11 gas fed of carbide furnace, the output end of the thermal decomposition carbide furnace 11 and the urgency
Fast cooling device 13 be connected to, 13 upper end of the quick cooling device respectively with the gas gasification electricity generation system and the combustion gas
Makeup set connection, 13 lower end of the quick cooling device connect with the carbon recovery system, it is described thermally decompose use hot-blast stove 12 and
11 input terminal of the thermal decomposition carbide furnace connection.In this way, the waste materials after drying are delivered to the thermal decomposition by drying machine 7
Carbide furnace 11 is thermally decomposed, and the thermal decomposition provides air-heater heat with hot-blast stove 12 to the thermal decomposition carbide furnace 11
Wind, the hot gas that the thermal decomposition carbide furnace 11 generates cool down rear portion gas by the quick cooling device 13 and are then conveyed
Gasification reaction is participated in combustion gasification apparatus, and solid residue then carries out recycling and the system of carbon and carbide by carbon recovery system
Standby clean environment firendly coal.And the part in the hot synthesis gas generated after gasification reaction in combustion gasification apparatus passes through described in connection
Thermal decomposition carbide furnace 11, which enters in the thermal decomposition carbide furnace 11, thermally decomposes waste materials.The thermal decomposition may be implemented in this way
Gas gasification after carbide furnace 11 is thermally decomposed generates electricity, while the hot gas of generation can promote combustion gasification apparatus gasification synthesis
Gas, the heat then generated are delivered to the waste heat recycling system and feedstock pre-processing system and combustion gasification respectively
Device.The technical solution technically still more preferably of technical solution is in front：The combustion gasification apparatus and the heat
Decompose and be provided with heat exchanger 14 between carbide furnace 11, the heat exchanger 14 respectively with the combustion gasification apparatus, the heat
Carbide furnace 11 is decomposed be connected to the waste heat recycling system, the heat exchanger 14 be used to ambient atmos being delivered to heat
The exchange hair-dryer 15 of exchanger 14 is connected to.In this way, the heat exchanger 14 by the gasification that combustion gasification apparatus generates synthesize into
The gasification synthesis gas that temperature decreases is delivered in the thermal decomposition carbide furnace 11 and participates in waste materials by row heat exchange
Thermal decomposition, and the waste heat after exchanging heat then be delivered to the waste heat recycling system carry out waste heat recycle generate electricity, heat supply or
Person prepares flyash etc., can also be delivered to feedstock pre-processing system certainly and waste materials are dried.And exchange blowing
The effect of machine 15 be will exchange heat required gas be delivered to the burn synthesis gas that is generated with combustion gasification apparatus in heat exchanger into
Row heat exchange.
The a kind of of the present invention utilizes pyrolysis of waste vaporized carbon elelctrochemical power generation device, please refers to Fig.1 middle related each figure, in front
It can also be on the basis of technical solution：The combustion gasification apparatus includes gasification combustion furnace 16, in the gasification combustion furnace 16
Lower part is connected to recyclable fuel storage device and the thermal decomposition carbonizing plant, 16 middle and upper part of the gasification combustion furnace with it is described
Feedstock pre-processing system is connected to, and 16 top of the gasification combustion furnace is connected to urea water tank 17, the top of the gasification combustion furnace 16
Portion is connected to the thermal decomposition carbonizing plant, and 16 lower part of the gasification combustion furnace is connected to the carbon recovery system.In this way, described
Gasification combustion furnace 16 is so that gas and urea and burning air etc. generate gasification synthesis gas body, the gasification in its interior combustion gasification
Synthetic gas is delivered in thermal decomposition carbonizing plant by the thermal decomposition carbonizing plant in communication helps positioned at described again
Thermally decompose the waste materials thermal decomposition in carbonizing plant.Certainly previously described heat exchanger 14 can be set between the two,
And the effect of heat exchanger 14 is to carry out heat exchange, the heat after heat exchange to the gasification synthesis gas that the gasification combustion furnace 16 generates
It is delivered to waste heat recycling system and carries out UTILIZATION OF VESIDUAL HEAT IN.And the gasification combustion furnace 16 is connected to recyclable fuel storage device
It is then that recyclable fuel is delivered to realization pyrolytic gasification reaction in the gasification combustion furnace 16, while the gasification combustion furnace 16
Top be connected to urea water tank 17, then be that urea is delivered to 16 internal reference of the gasification combustion furnace to add gasification reaction.The gas
Change 16 middle and lower part of combustion furnace to be connected to the thermal decomposition carbonizing plant, then being will in the end direction for thermally decomposing carbonizing plant
A part for hot gas after thermal decomposition, which is delivered in the gasification combustion furnace 16, completes gasification reaction.And the thermal decomposition carbonization
Another part of gas after the thermal decomposition of the terminal position of device is then used for fuel gas generation.And in the gasification combustion furnace 16
Lower part is connected to the carbon recovery system, is the recycling that the lime-ash etc. after gasification, and combustion is carried out to subsequent carbon and carbon compound
After prepare clean environment firendly coal.Furthermore it is also possible to be to be provided with urea between the urea water tank 17 and the gasification combustion furnace 16
Nozzle 18, the urea nozzle 18 are connected to 16 inside of the gasification combustion furnace, the urea nozzle 18 and the urea water tank
17 connections.It urea may be implemented so preferably conveys more uniformly to be transported to 16 internal reference of the gasification combustion furnace and add gasified reverse
It answers.
The a kind of of the present invention utilizes pyrolysis of waste vaporized carbon elelctrochemical power generation device, please refers to Fig.1 middle related each figure, in front
It can also be on the basis of technical solution：The gas gasification electricity generation system includes the Cyclone machines 41 being sequentially communicated, gas synthesis gas
Cooling tower 42, combustion gas heat exchanger 43, combustion biogas bin 44 and gas electricity generator 45, the Cyclone machines 41 and the thermal decomposition
Carbonizing plant is connected to, and the combustion gas heat exchanger 43 is connected to with sewage treatment equipment.In this way, the thermal decomposition carbonizing plant heat
The thermal decomposition gas generated after decomposition is transported to Cyclone machines 41, then takes cooling using synthesis air cooling, is entering later
Combustion gas heat exchanger 43 cools down, and then enters back into getting up early bin, is generated electricity later by gas electricity generator 45, and combustion gas
Heat exchanger 43 is connected to sewage treatment equipment then can further save energy by the waste water after heat exchange again recycling
Source.It is, of course, also possible to be that combustion gas bag filter 46 is arranged between gas synthesis gas cooling tower 42 and combustion gas heat exchanger 43.If
The effect for setting combustion gas bag filter 46 is the impurity in further filtering thermal decomposition gas, improves the efficiency of gas gasification power generation
Ensure the safety of gas gasification power generation simultaneously.And gas gasification power generation itself be currently with more power generation project it
One, therefore no longer specifically repeat its specific structure and principle.Technical solution still more preferably is the gas electricity generator
45 are connected to the waste heat boiler 19, and the hot gas after burning is delivered to waste heat boiler 19 and is recycled, energy is effectively saved
Source simultaneously further generates electricity.
The a kind of of the present invention utilizes pyrolysis of waste vaporized carbon elelctrochemical power generation device, please refers to Fig.1 middle related each figure, in front
It can also be on the basis of technical solution：The waste heat recycling system includes waste heat boiler 19, waste heat for supplying device, waste heat
Steam electric power generator, waste heat gas discharging apparatus and waste heat flyash retracting device 35, the top of the waste heat boiler 19 with it is described
Afterheat steam power generator is connected to, and 19 output end of the waste heat boiler is connected to waste heat gas discharging apparatus, the waste heat boiler
19 lower parts are connect with the waste heat flyash retracting device 35, and the afterheat steam power generator connects with the waste heat for supplying device
Logical, the waste heat boiler 19 is connected to the feedstock pre-processing system.Waste heat recycling system can both pass through waste heat in this way
Waste heat is delivered to the afterheat steam power generator and is converted into steam by boiler 19 to generate electricity, and can be that waste heat boiler 19 will
Heat is delivered to waste heat for supplying device and provides hot water or hot gas supply for factory or building, realizes industry or civilian confession
Heat.Band can have surplus heat the gas of waste heat boiler 19 is delivered in waste heat gas discharging apparatus simultaneously, is prepared straight after flyash
It connects and the partial reaction object is delivered in waste heat flyash retracting device 35.In addition, in the lower part of waste heat boiler 19 and waste heat powder
Coal ash retracting device 35 connects, then is that the lime-ash etc. for generating its waste heat boiler 19 is fed directly to waste heat flyash retracting device
35 carry out the recycling of flyash.Waste heat evaporation power generator is connected to waste heat for supplying device simultaneously, by waste heat for steaming
Raw remaining heat carries out industry or domestic heating by waste heat for supplying device after hair power generation.And the waste heat boiler 19 with it is described
Feedstock pre-processing system is connected to, then is that a part of gas in waste heat boiler 19 is delivered in the feedstock pre-processing system to fill
Point the waste materials in drying machine 7 are dried using hot gas, subsequent handling is avoided to occur exploding or on fire.Further
Preferably technical solution is：The afterheat steam power generator includes steam turbine 20 and steam-driven generator 22, the vapor wheel
Machine 20 and retarder 21 is connected between the steam-driven generator 22, the steam turbine 20 is filled with afterheat steam power generation
It sets including steam turbine 20 and steam-driven generator 22, the steam turbine 20 and being connected between the steam-driven generator 22 subtracts
Fast device 21, the steam turbine 20 are connected to the waste heat boiler 19.In this way, the steam that the waste heat boiler 19 generates is conveyed
The steam hair that steam-driven generator 22 carries out one of UTILIZATION OF VESIDUAL HEAT IN is delivered into steam turbine 20, then after slowing down by retarder 21
Electricity.Not only there is fuel gas generation in this way, while there is steam-electric power, the waste heat generated in whole equipment is made full use of, into one
Step submits the generating efficiency of power generator.The technical solution on the basis of technical solution still more preferably is in front：It is described
Waste heat for supplying device includes condenser 23, heat supply cooling tower 24, pure water treatment device 25, high steam distributor 26 and heat supply
Unit 27, the condenser 23 are connected to the steam turbine 20, and the condenser 23 is taken cycle with heat supply cooling and is connected to,
The condenser 23 is connected to the pure water treatment device 25, the connection of the pure water treatment device 25 and the high steam
Distributor 26 is connected to, and the high steam distributor 26 is connected to the heating unit 27, the high steam distributor 26 and
The steam turbine 20 is connected to.The gas being discharged from the steam turbine 20 in this way enters pure water process by condenser 23
It enters back into high steam distributor 26 and is allocated after treatment in device 25, some certain high steam is direct
It is fed directly to the high steam distributor 26 from steam turbine 20, final high steam distributor 26 is by hot gas or hot water
It is supplied respectively to heating unit 27 in communication and carries out heat supply.And circulating picture-changing is carried out between heat supply cooling tower 24 and condenser 23
Heat.It can also be that waste heat gas discharging apparatus includes being loaded into hair-dryer 28, reaction machine 29, sending on the basis of technical solution in front
Wind turbine 30, activated carbon hopper 32, pulverized limestone hopper 33, smoke filter 34 and chimney 31, the loading hair-dryer 28 with it is described
Waste heat boiler 19 is connected to, and the hair-dryer is connected to machine 29 is reacted, and the reaction machine 29 is connected to the feedstock pre-processing system,
The activated carbon hopper 32 and the pulverized limestone hopper 33 and pressure fan 30 are connected to the machine 29 that reacts respectively, the reaction
Machine 29 is connected to smoke filter 34, and the smoke filter 34 is connected to chimney 31.In this way, being loaded into hair-dryer 28 by waste heat pot
The hot gas of stove 19 is delivered to reaction machine 29, while the dry flue gas of feedstock pre-processing system output also enters in reaction machine 29,
Activated carbon and pulverized limestone are delivered to reaction machine with the activated carbon hopper 32 and pulverized limestone hopper 33 for reacting the connection of machine 29 simultaneously
29 simultaneously, and outside air is delivered to reaction machine 29 by pressure fan 30, reaction is carried out in reaction machine 29 and by smoke filter 34
After filtering, flue gas is transported to chimney 31 and is emitted into air, and remaining solid matter is then transported to waste heat flyash recycling dress
It sets in 35.
The a kind of of the present invention utilizes pyrolysis of waste vaporized carbon elelctrochemical power generation device, please refers to Fig.1 middle related each figure, in front
It can also be on the basis of technical solution：The carbon recovery system include carbon cooler 36, carbon sorting machine 37, sorting escaper,
Carbon recycling conveyor 38, carbon bin 39 and packing machine 40, the carbon cooler 36 connect with the thermal decomposition carbonizing plant lower part
Logical, the carbon sorting machine 37 is located at 36 underface of the carbon cooler, and the carbon sorting machine 37 discharges implements with the sorting
Expect that conveying-type connection, the sorting escaper are connect with carbon recycling conveyor 38, the carbon recycling conveyor 38 is stored up with the carbon
It hides slot 39 to be connected to, the carbon bin 39 is connect with the packing machine 40.The conveying of thermal decomposition carbonizing plant lower part is unburned in this way
Burn object or lime-ash etc. and enter and be transported to carbon sorting machine 37 after carbon cooler 36 cools down and sorted, the waste residue after sorting then by
Discharge, and useful solid matter, that is, carbon and carbon compound are then fallen in carbon recycling conveyor 38, useful carbon and carbon compound
Object is exported after being then delivered to carbon bin 39 by carbon recycling conveyor 38 and is packed with packing machine 40.The same gasification
The carbon and carbon compound that combustion furnace 16 generates again may be by above equipment and recycles to prepare environment-protecting clean coal.
The a kind of of the present invention utilizes pyrolysis of waste vaporized carbon elelctrochemical power generation device, please refers to Fig.1 middle related each figure, in front
It can also be on the basis of technical solution：The Material supply system include sequentially connected raw material cutting machine 2, input hopper 3,
Ingredient conveyor 1, raw material sorting machine 4, raw material storage bin hopper 5 and measured quantity dispensing device 6, the measured quantity dispensing device 6 and the raw material are pre-
The input terminal of processing system is connected to.Waste materials are fed into input hopper 3 after the cutting of raw material cutting machine 2 in this way
It is interior, it is then delivered in raw material sorting machine 4 and is sorted by ingredient conveyor 1, useful waste materials enter raw material storing
In bucket 5, and the incombustible such as metal sorted out are then transported in incombustible storage bin hopper 47.Then combustible useful useless
Gurry raw material is delivered in measured quantity dispensing device 6 by ingredient conveyor 1 out of raw material storage bin hopper 5 and to eventually enter into the raw material pre-
Processing system such as is dried at the pretreatments.The humidity that such Material supply system can provide after drying for subsequent handling is less than
10% combustible waste material raw material further ensures raw material supply and the safety of subsequent handling, avoid occurring it is on fire or
Situations such as person is exploded.
In addition, it is necessary to which explanation is that in the accompanying drawings, A represents dry flue gas, B represents burning air, and C represents burning coal gas, D generations
Table burning coal gas, E represent urea water, and H represents steam, and I represents waste water, and J represents exhaust gas, and K represents flyash, and L represents fuel, M
Lime-ash.
It is above-mentioned that only several specific embodiments in the present invention are illustrated, but can not be as the protection model of the present invention
Enclose, it is every according to the present invention in design spirit made by equivalent change or modification or equal proportion zoom in or out, should all
Think to fall into protection scope of the present invention.
Claims (13)
1. a kind of utilizing pyrolysis of waste vaporized carbon elelctrochemical power generation device, it is characterised in that：Locate in advance including Material supply system, raw material
Reason system, thermal decomposition carbonizing plant, combustion gasification apparatus, waste heat recycling system, carbon recovery system and gas gasification power generation
System, the Material supply system are connect with the feedstock pre-processing system for dry feedstock, the pretreatment of raw material system
System is connect with the thermal decomposition carbonizing plant, and the thermal decomposition carbonizing plant is connect with the combustion gasification apparatus, the burning
Gasification installation is connect with the waste heat recycling system, the thermal decomposition carbonizing plant and the gas gasification electricity generation system,
Combustion gasification apparatus is connected with the carbon recovery system.
2. a kind of utilization pyrolysis of waste vaporized carbon elelctrochemical power generation device according to claim 1, it is characterised in that：The heat
Carbonizing plant, the combustion gasification apparatus and the waste heat recycling system is decomposed to connect with the feedstock pre-processing system
It connects.
3. a kind of utilization pyrolysis of waste vaporized carbon elelctrochemical power generation device according to claim 2, it is characterised in that：The original
Material pretreatment system includes drying machine and drying hot-blast stove, the drying machine front and back end respectively with the Material supply system and
The thermal decomposition carbonizing plant is connected by device for transporting objects, and the drying hot-blast stove is connected to the drying machine, described
It thermally decomposes carbonizing plant, the combustion gasification apparatus and the waste heat recycling system and dry uses hot wind furnace gases with described
Input type is connected to, and the drying machine is connected to the combustion gasification apparatus burning gases input type, the drying machine with it is described remaining
Recuperation of heat is connected to using system dry flue gas input type.
4. a kind of utilization pyrolysis of waste vaporized carbon elelctrochemical power generation device according to claim 3, it is characterised in that：The heat
It includes thermal decomposition carbide furnace, thermal decomposition hot-blast stove and quick cooling device, the drying machine and the heat to decompose carbonizing plant
The input terminal material input type connection of carbide furnace is decomposed, the combustion gasification apparatus connects with thermal decomposition carbonization furnace gases input type
Logical, the output end of the thermal decomposition carbide furnace is connected to the quick cooling device, the quick cooling device upper end respectively with
The gas gasification electricity generation system is connected to the combustion gasification apparatus, and the quick cooling device lower end is with carbon recycling
System connection, the thermal decomposition hot-blast stove are connected to the thermal decomposition carbide furnace input terminal.
5. a kind of utilization pyrolysis of waste vaporized carbon elelctrochemical power generation device according to claim 4, it is characterised in that：The combustion
Burn and be provided with heat exchanger between gasification installation and the thermal decomposition carbide furnace, the heat exchanger respectively with the combustion gasification
Device, the thermal decomposition carbide furnace are connected to the waste heat recycling system, the heat exchanger with for by ambient atmos
It is delivered to the exchange hair-dryer connection of heat exchanger.
6. a kind of utilization pyrolysis of waste vaporized carbon elelctrochemical power generation according to claim 1 to 5 any one claim fills
It sets, it is characterised in that：The combustion gasification apparatus includes gasification combustion furnace, the gasification combustion furnace middle and lower part and recyclable fuel
Storage device is connected to the thermal decomposition carbonizing plant, and the gasification combustion furnace middle and upper part connects with the feedstock pre-processing system
Logical, the gasification combustion furnace top is connected to urea water tank, the top of the gasification combustion furnace and the thermal decomposition carbonizing plant
Connection, the gasification combustion furnace lower part is connected to the carbon recovery system.
7. a kind of utilization pyrolysis of waste vaporized carbon elelctrochemical power generation according to claim 1 to 5 any one claim fills
It sets, it is characterised in that：The gas gasification electricity generation system includes the Cyclone machines being sequentially communicated, synthesis gas cooling tower, the friendship of combustion gas heat
It changes planes, biogas bin and gas electricity generator, the Cyclone machines are connected to the thermal decomposition carbonizing plant, the combustion gas heat exchange
Machine is connected to with sewage treatment equipment.
8. a kind of utilization pyrolysis of waste vaporized carbon elelctrochemical power generation according to claim 1 to 5 any one claim fills
It sets, it is characterised in that：The waste heat recycling system include waste heat boiler, waste heat for supplying device, afterheat steam power generator,
Waste heat gas discharging apparatus and waste heat flyash retracting device, the waste heat boiler top connect with the afterheat steam power generator
Logical, the waste heat boiler output end is connected to waste heat gas discharging apparatus, the waste heat boiler lower part and the waste heat flyash
Retracting device connects, and the afterheat steam power generator is connected to the waste heat for supplying device, the waste heat boiler and the original
Expect pretreatment system connection.
9. a kind of utilization pyrolysis of waste vaporized carbon elelctrochemical power generation device according to claim 8, it is characterised in that：It is described remaining
Hot steam power generator includes steam turbine and steam-driven generator, the steam turbine and is connected between the steam-driven generator
There are retarder, the steam turbine to be connected to the waste heat boiler.
10. a kind of utilization pyrolysis of waste vaporized carbon elelctrochemical power generation device according to claim 9, it is characterised in that：It is described
Waste heat for supplying device includes condenser, heat supply cooling tower, pure water treatment device, high steam distributor and heating unit, institute
It states condenser to be connected to the steam turbine, the condenser is taken cycle with heat supply cooling and is connected to, the condenser and institute
Pure water treatment device connection is stated, the pure water treatment device connection is connected to the high steam distributor, the high pressure
Steam distributor is connected to the heating unit, and the high steam distributor is connected to the steam turbine.
11. a kind of utilization pyrolysis of waste vaporized carbon elelctrochemical power generation device according to claim 8, it is characterised in that：Waste heat
Gas discharging apparatus includes being loaded into hair-dryer, reaction machine, pressure fan, activated carbon hopper, pulverized limestone hopper, smoke filter and cigarette
Chimney, the loading hair-dryer are connected to the waste heat boiler, and the hair-dryer is connected to machine is reacted, the reaction machine and the original
Expect that pretreatment system connection, the activated carbon hopper and the pulverized limestone hopper and pressure fan connect with the machine that reacts respectively
Logical, the reaction machine is connected to smoke filter, and the smoke filter is connected to chimney.
12. a kind of utilization pyrolysis of waste vaporized carbon elelctrochemical power generation according to claim 1 to 5 any one claim fills
It sets, it is characterised in that：The carbon recovery system includes carbon cooler, carbon sorting machine, sorting escaper, carbon recycling conveyor, carbon
Bin and packing machine, the carbon cooler are connected to the thermal decomposition carbonizing plant lower part, and the carbon sorting machine is located at described
Place immediately below carbon cooler, the carbon sorting machine is connect with the sorting escaper material conveying-type, the sorting escaper and
Carbon recycling conveyor connects, and the carbon recycling conveyor is connected to the carbon bin, the carbon bin and the packing machine
Connection.
13. a kind of utilization pyrolysis of waste vaporized carbon elelctrochemical power generation according to claim 1 to 5 any one claim fills
It sets, it is characterised in that：The Material supply system includes sequentially connected raw material cutting machine, input hopper, ingredient conveyor, original
Expect that sorting machine, raw material storage bin hopper and measured quantity dispensing device, the input terminal of the measured quantity dispensing device and the feedstock pre-processing system connect
It is logical.
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| CN201810296120.9A CN108300517A (en) | 2018-03-30 | 2018-03-30 | It is a kind of to utilize pyrolysis of waste vaporized carbon elelctrochemical power generation device |
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| CN201810296120.9A CN108300517A (en) | 2018-03-30 | 2018-03-30 | It is a kind of to utilize pyrolysis of waste vaporized carbon elelctrochemical power generation device |
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