CN108342226A - A kind of device producing reclaimed oil using pyrolysis of waste vaporized carbon metaplasia - Google Patents
A kind of device producing reclaimed oil using pyrolysis of waste vaporized carbon metaplasia Download PDFInfo
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- CN108342226A CN108342226A CN201810297912.8A CN201810297912A CN108342226A CN 108342226 A CN108342226 A CN 108342226A CN 201810297912 A CN201810297912 A CN 201810297912A CN 108342226 A CN108342226 A CN 108342226A
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- reclaimed oil
- carbon
- waste
- thermal decomposition
- waste heat
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- 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
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/002—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal in combination with oil conversion- or refining processes
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/10—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal from rubber or rubber waste
-
- 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
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1003—Waste materials
-
- 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
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Processing Of Solid Wastes (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
Abstract
The present invention discloses the device that reclaimed oil is produced using pyrolysis of waste vaporized carbon metaplasia, supply system including interconnection, pretreatment system, thermally decompose carbonizing plant, combustion gasification apparatus, waste heat recycling system, carbon recovery system and reclaimed oil prepare collection system, it includes being quickly cooled down tower that reclaimed oil, which prepares collection system, reclaimed oil condensed device, reclaimed oil purifying column and reclaimed oil fuel reserve tank, tower is quickly cooled down to be connected to thermal decomposition carbonizing plant, it is quickly cooled down in tower and is connected to reclaimed oil condensed device, it reclaimed oil condensed device and is quickly cooled down tower and is connected to reclaimed oil fuel reserve tank, reclaimed oil condensed device is connected to reclaimed oil purifying column, it is connected to combustion gasification apparatus and reclaimed oil fuel reserve tank on purifying column.Apparatus structure that the present invention produces reclaimed oil using pyrolysis of waste vaporized carbon metaplasia is simple, waste tire and agricultural wastes is made full use of to prepare reclaimed oil, it effectively reduces waste water content and is recycled heat is generated again, the energy is saved, avoids catching fire and explode.
Description
Technical field
The present invention relates to a kind of reclaimed oil preparation facilities, are produced using pyrolysis of waste vaporized carbon metaplasia more particularly to a kind of
The device of reclaimed oil.
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 production reclaimed oil, while effectively reducing waste water content and will produce
Heat amount recycles again, effectively saves the energy, avoids catching fire and what is occurred situations such as explosion is gasified using pyrolysis of waste
The device of carbonization production reclaimed oil.
A kind of device producing reclaimed oil using pyrolysis of waste vaporized carbon metaplasia of the present invention, including Material supply system,
Feedstock pre-processing system, thermal decomposition carbonizing plant, combustion gasification apparatus, waste heat recycling system, carbon recovery system and regeneration
Oil prepares collection system, and the Material supply system is connect with the feedstock pre-processing system for dry feedstock, the original
Material pretreatment system is connect with the thermal decomposition carbonizing plant, and the thermal decomposition carbonizing plant prepares collection system with reclaimed oil and connects
It connects, the combustion gasification apparatus is connect with the waste heat recycling system, the thermal decomposition carbonizing plant and the reclaimed oil
Preparation collection system, combustion gasification apparatus are connected with the carbon recovery system, and it includes quick that the reclaimed oil, which prepares collection system,
Cooling tower, reclaimed oil condensed device, reclaimed oil purifying column and reclaimed oil fuel reserve tank, it is described to be quickly cooled down top of tower and the thermal decomposition
Carbonizing plant is connected to, and the tower bottom that is quickly cooled down is connected to the reclaimed oil fuel reserve tank, it is described be quickly cooled down tower middle and lower part and
Reclaimed oil condensed device one end is connected to, and reclaimed oil condensed device lower part is connected to the reclaimed oil fuel reserve tank, and the reclaimed oil is solidifying
The contracting device other end is connected to the reclaimed oil purifying column, the purifying column upper and lower side respectively with the combustion gasification apparatus and described
Reclaimed oil fuel reserve tank is connected to.
A kind of device being produced reclaimed oil using pyrolysis of waste vaporized carbon metaplasia of the present invention can also be：
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
It sets upper end and is quickly cooled down tower and the combustion gasification apparatus is connected to described respectively, the quick cooling device lower end and the carbon
Recovery system connects, and the thermal decomposition hot-blast stove is 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 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, the waste heat boiler and the raw material
Pretreatment system is connected to.
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 is connected to the high steam distributor, institute
It states high steam distributor to be connected to the heating unit, 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.
A kind of device producing reclaimed oil using pyrolysis of waste vaporized carbon metaplasia of the present invention, including Material supply system,
Feedstock pre-processing system, thermal decomposition carbonizing plant, combustion gasification apparatus, waste heat recycling system, carbon recovery system and regeneration
Oil prepares collection system, and the Material supply system is connect with the feedstock pre-processing system for dry feedstock, the original
Material pretreatment system is connect with the thermal decomposition carbonizing plant, and the thermal decomposition carbonizing plant prepares collection system with reclaimed oil and connects
It connects, the combustion gasification apparatus is connect with the waste heat recycling system, the thermal decomposition carbonizing plant and the reclaimed oil
Preparation collection system, combustion gasification apparatus are connected with the carbon recovery system, and it includes quick that the reclaimed oil, which prepares collection system,
Cooling tower, reclaimed oil condensed device, reclaimed oil purifying column and reclaimed oil fuel reserve tank, it is described to be quickly cooled down top of tower and the thermal decomposition
Carbonizing plant is connected to, and the tower bottom that is quickly cooled down is connected to the reclaimed oil fuel reserve tank, it is described be quickly cooled down tower middle and lower part and
Reclaimed oil condensed device one end is connected to, and reclaimed oil condensed device lower part is connected to the reclaimed oil fuel reserve tank, and the reclaimed oil is solidifying
The contracting device other end is connected to the reclaimed oil purifying column, the purifying column upper and lower side respectively with the combustion gasification apparatus and described
Reclaimed oil fuel reserve tank is connected to.In this way, the effect of Material supply system is to provide waste material, the waste for subsequent technique
Material includes waste tire, waste plastics, the vinyl that gives up, sewage and animal wastes, municipal refuse, agricultural wastes, flyash and
Food refuse etc..Material supply system is that above-mentioned waste material is delivered to raw material preprocessing device.And raw material preprocessing device
Effect be that waste material is sorted and dried so that the aqueous of the waste material of the needs of subsequent processing can be carried out
Amount reduces, at least needed for the water content of waste material to be less than 10% and can just enter follow-up equipment, feedstock pre-processing system will be into
Pretreated waste materials of going are delivered to thermal decomposition carbonizing plant, the waste that thermal decomposition carbonizing plant will be delivered in it
Raw material is pyrolyzed, and the pyrolysis carbonization gas that temperature is 650-700 DEG C is generated, which is transported to the regeneration
Oil prepares collection system and produces reclaimed oil, the purpose for the preparation that reclaimed oil is carried out using waste is realized, specifically, pyrolytic carbon
Reclaimed oil can directly be prepared after being exported to quickly cooling device in thermal decomposition carbonizing plant by changing gas, while can also be heat
Generation reclaimed oil is delivered in reclaimed oil fuel reserve tank after solution carbonization gas enters the condensation of reclaimed oil condensed device.In addition it being again
Reclaimed oil in oil generation condensed device is delivered in reclaimed oil purifying column after purification, and purified a part of reclaimed oil is delivered to regeneration
In oily fuel reserve tank, another part is then sent to combustion gasification apparatus promotes gasification reaction as fuel.And it is a part of from described
The pyrolysis carbonization gas that thermal decomposition carbonizing plant transfers out enters combustion gasification apparatus and carries out combustion gasification, the heat then generated
It is delivered to the thermal decomposition carbonizing plant again, heat is carried out to the pretreated waste materials in the thermal decomposition carbonizing plant
Solution, can recycle pyrolysis carbonization gas in this way, further increase pyrolysis carbonization gas effciency, reduce energy consumption.And it burns
Gasification installation is connect with the waste heat recycling system, then will be delivered to after the heat heat exchange in the synthesis gas of gasification described
Waste heat recycling system carries out waste heat recycling, can have using these waste heats and act on：Contain first this part
The hot gas of high heat can be delivered to feedstock pre-processing system and processing is dried to waste materials, and it is former to save dry waste
Heat used in material, reduces cost.Second this partial heat can be delivered to steam generating system and carry out steam-electric power, power generation
Efficient, the energy makes full use of, while can also convert this partial heat to steam or hot water, to industry and civilian confession
Heat and heating provide heat；Third can also be prepares flyash using this partial heat.Certainly a part of hot gas is by processing
After can be discharged into air.And it thermally decomposes the slag being discharged in carbonizing plant and carbon and carbon is carried out by the carbon recovery system being attached thereto
The preparation and recycling of compound, can prepare the coal of clean environment firendly.In this way using include waste tire, waste plastics, give up vinyl,
Sewage and animal wastes, municipal refuse, agricultural wastes and food refuse the like waste raw material can prepare reclaimed oil, heat supply,
Clean environment firendly coal is prepared, while the heat generated in preparation process can also be comprehensively utilized and reused.It makes full use of
The energy saves the energy and generates good economic benefit.Simultaneously because waste materials are done in feedstock pre-processing system
Dry processing so that the humidity of waste materials is less than 10%, therefore it is possible to prevente effectively from during after burning and gasification
The phenomenon that catching fire and exploding effectively improves the safety of integral device.The a kind of of the present invention is gasified using pyrolysis of waste
Carbonization production reclaimed oil device, compared with the existing technology the advantages of be：It is simple in structure, can make full use of waste tire and agriculture
Industry waste produces reclaimed oil, while effectively reducing waste water content and being recycled heat is generated again, and effectively saves
The energy, situations such as avoiding catching fire and exploding.
Description of the drawings
A kind of apparatus structure schematic diagram for producing reclaimed oil using pyrolysis of waste vaporized carbon metaplasia of Fig. 1 present invention.
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 ... are quickly cooled down tower 42 ... reclaimed oil condensed device 43 ... reclaimed oil purifying column
44 ... reclaimed oil fuel reserve tank 45 ... reclaimed oil cooling tower 47 ... incombustible storage bin hoppers
Specific implementation mode
A kind of devices that using pyrolysis of waste vaporized carbon metaplasia produces reclaimed oil of the Fig. 1 below in conjunction with the accompanying drawings to the present invention
It is described in further detail.
A kind of device being produced reclaimed oil using pyrolysis of waste vaporized carbon metaplasia of the present invention is please referred to Fig.1 middle related each
Figure, including Material supply system, feedstock pre-processing system, thermal decomposition carbonizing plant, combustion gasification apparatus, heat recovery system
System, carbon recovery system and reclaimed oil prepare collection system, and the Material supply system and the raw material for dry feedstock are pre-
Processing system connects, and the feedstock pre-processing system connect with the thermal decomposition carbonizing plant, the thermal decomposition carbonizing plant and
Reclaimed oil prepares collection system connection, and the combustion gasification apparatus is connect with the waste heat recycling system, the thermal decomposition
Carbonizing plant prepares collection system, combustion gasification apparatus and the carbon recovery system with the reclaimed oil and connect, the reclaimed oil
It includes being quickly cooled down tower 41, reclaimed oil condensed device 42, reclaimed oil purifying column 43 and reclaimed oil fuel reserve tank 44, institute to prepare collection system
It states to be quickly cooled down at the top of tower 41 and be connected to the thermal decomposition carbonizing plant, 41 bottom of tower that is quickly cooled down is stored up with the reclaimed oil
Fuel tank 44 is connected to, and 41 middle and lower part of tower that is quickly cooled down is connected to 42 one end of reclaimed oil condensed device, the reclaimed oil condensed device 42
Lower part is connected to the reclaimed oil fuel reserve tank 44, and 42 other end of reclaimed oil condensed device connects with the reclaimed oil purifying column 43
Logical, the purifying column upper and lower side is connected to the combustion gasification apparatus and the reclaimed oil fuel reserve tank 44 respectively.In this way, raw material supplies
It is to provide waste material for subsequent technique to answer the effect of system, and the waste material includes waste tire, waste plastics, useless ethylene
Resin, sewage and animal wastes, municipal refuse, agricultural wastes and food refuse etc..Material supply system is will be above-mentioned discarded
Material is delivered to raw material preprocessing device.And the effect of raw material preprocessing device is that waste material is sorted and dried, and is made
Obtaining the water content of the waste material for the needs that can carry out subsequent processing reduces, and the water content of at least required waste material wants low
Follow-up equipment can just be entered in 10%, feedstock pre-processing system was delivered to thermally decomposed carbon by pretreated waste materials are carried out
Makeup is set, and the waste materials being delivered in it are pyrolyzed by thermal decomposition carbonizing plant, generates the heat that temperature is 650-700 DEG C
Carbonization gas is solved, which is transported to the reclaimed oil and prepares collection system production reclaimed oil, realize using useless
Gurry carries out the purpose of the preparation of reclaimed oil, specifically, pyrolysis carbonization gas is exported from thermal decomposition carbonizing plant to quick
Reclaimed oil can be directly prepared after cooling device, at the same can also be pyrolysis carbonization gas enter reclaimed oil condensed device 42 condense after
Reclaimed oil is generated to be delivered in reclaimed oil fuel reserve tank 44.In addition it being that the reclaimed oil in reclaimed oil condensed device 42 is delivered to again
In oil generation purifying column 43 after purification, purified a part of reclaimed oil is delivered in reclaimed oil fuel reserve tank 44, and another part is then sent
Promote gasification reaction as fuel to combustion gasification apparatus.And the heat that a part is transferred out from the thermal decomposition carbonizing plant
Solution carbonization gas enters combustion gasification apparatus and carries out combustion gasification, and the heat then generated is delivered to the thermally decomposed carbon makeup again
It sets and the pretreated waste materials in the thermal decomposition carbonizing plant is pyrolyzed, pyrolytic carbon can be recycled in this way
Change gas, further increases pyrolysis carbonization gas effciency, reduce energy consumption.And combustion gasification apparatus and the heat recovery
System 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 again
It utilizes, 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 raw material
Processing is dried to waste materials in pretreatment system, saves heat used in dry waste raw material, reduces cost.The
Two this partial heats can be delivered to steam generating system and carry out steam-electric power, and generating efficiency is high, and the energy makes full use of, while
This partial heat can be converted to steam or hot water, heat is provided to industry and civilian heat supply and heating；Third may be used also
To be to prepare flyash using this partial heat.Certain a part of hot gas can be discharged into air after treatment.And it thermally decomposes
The slag being discharged in carbonizing plant carries out the preparation and recycling of carbon and carbide by the carbon recovery system being attached thereto, and can prepare
The coal of clean environment firendly.In this way using include waste tire, waste plastics, the vinyl that gives up, sewage and animal wastes, municipal refuse,
Agricultural wastes and food refuse the like waste raw material can prepare reclaimed oil, heat supply, prepare clean environment firendly coal, while can be with
The heat generated in preparation process is comprehensively utilized to be reused.The energy is made full use of, the energy is saved and is generated good
Economic benefit.Simultaneously because processing is dried in waste materials in feedstock pre-processing system so that waste materials it is wet
Degree is less than 10%, therefore it is possible to prevente effectively from during after burning and gasification the phenomenon that catch fire and explode, effectively
Improve the safety of integral device.A kind of device producing reclaimed oil using pyrolysis of waste vaporized carbon metaplasia of the present invention, relatively
It is in the advantages of prior art：It is simple in structure, can make full use of waste tire and agricultural wastes prepare reclaimed oil, have simultaneously
Effect reduces waste water content and will generate situations such as heat recycles, effectively saves the energy, avoid catching fire and exploding again
Occur.Technical solution further preferred on the basis of technical solution is in front：Reclaimed oil condensed device 42 is cooled down with reclaimed oil
The connection heat exchange of tower 45, such reclaimed oil cooling tower 45 can carry out heat exchange with reclaimed oil condensed device 42 and realize to solidifying into reclaimed oil
Reclaimed oil or gas in contracting device 42 are condensed and are compressed.
A kind of device being produced reclaimed oil using pyrolysis of waste vaporized carbon metaplasia of the present invention is please referred to Fig.1 middle related each
Scheme, can be specifically on the basis of technical solution in front：The thermal decomposition carbonizing plant, the combustion gasification apparatus and described
Waste heat recycling system is connect with the feedstock pre-processing system.In this way, useless after feedstock pre-processing system drying process
It is thermally decomposed in gurry feedstock transportation to thermal decomposition carbonizing plant, and a part of hot gas being discharged in feedstock pre-processing system is then
Into, as burning air, and another part hot gas is then recycled into feedstock pre-processing system again in combustion gasification apparatus,
A part of burn synthesis gas for thermally decomposing in carbonizing plant simultaneously is also delivered to feedstock pre-processing system as being carried after fuel combustion
Heating load makes it that waste materials be dried to feedstock pre-processing system.And it is useless in the waste heat recycling system
Some is dried waste materials also by the feedstock pre-processing system being attached thereto heat, in this way, pretreatment of raw material
The required heat of drying of system has sufficient source, effectively saves the energy and the system in whole device is made full use of to generate
Heat and thermal energy.The technical further preferred technical solution of technical solution is in front：The feedstock pre-processing system
Including drying machine 7 and dry hot-blast stove 8,7 front and back end of the drying machine is divided with the Material supply system and the heat respectively
Solution carbonizing plant is connected by device for transporting objects 9, and the drying is connected to hot-blast stove 8 with the drying machine 7, the thermal decomposition
Carbonizing plant, the combustion gasification apparatus and the waste heat recycling system are inputted with drying 8 gas of hot-blast stove
Formula is connected to, and the drying machine 7 is connected to the combustion gasification apparatus burning gases input type, the drying machine 7 and the waste heat
Recycling system dry flue gas input type is connected to.Drying machine 7 is for being dried, dropping by the waste materials being delivered in it
The humidity of low waste materials to 10% hereinafter, convenient follow-up carry out pyrolytic gasification, while while avoiding pyrolytic gasification it is on fire or
The case where explosion, occurs, and the drying is that conveying is former for dry waste into the drying machine 7 with the effect of hot-blast stove 8
The hot wind and thermal energy of material, and thermally decompose carbonizing plant, the waste heat recycling system and combustion gasification apparatus and done with described
It is dry to be connected to 8 gas fed of hot-blast stove, the thermal decomposition carbonizing plant described in this way, combustion gasification apparatus and waste heat recovery profit
With in 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 defeated
It send to drying machine 7 is interior and processing is dried to waste materials.And the gas that drying machine 7 is discharged can then enter subsequent fine coal
Flyash is prepared in grey preparation process, certain a portion hot gas can also be again introduced into drying hot-blast stove 8 and follow
Ring, a portion hot gas can also be used as burning air by the combustion gasification apparatus being connected to drying machine 7 and enter combustion gas
Middle gasification reaction is set in makeup.And the waste materials after drying are transported in dried object bin 10, then defeated
It send to the thermal decomposition carbonizing plant and is thermally decomposed, realization prepares the purpose of reclaimed oil.And drying machine 7 and the waste heat recovery
It is connected using system, is then that dry flue gas is delivered to the waste heat recycling system to prepare flyash.Technical solution in front
Technically technical solution still more preferably be：The thermal decomposition carbonizing plant includes thermal decomposition carbide furnace 11, thermal decomposition
With hot-blast stove 12 and quick cooling device 13, the input terminal material input type of the drying machine 7 and the thermal decomposition carbide furnace 11
Connection, the combustion gasification apparatus are connected to thermal decomposition 11 gas fed of carbide furnace, the output of the thermal decomposition carbide furnace 11
End is connected to the quick cooling device 13,13 upper end of the quick cooling device respectively with the tower 41 and described of being quickly cooled down
Combustion gasification apparatus is connected to, and 13 lower end of the quick cooling device is connect with the carbon recovery system, the thermal decomposition hot wind
Stove 12 is connected to 11 input terminal of thermal decomposition carbide furnace.In this way, drying machine 7 waste materials after drying are delivered to it is described
Thermal decomposition carbide furnace 11 is thermally decomposed, and the thermal decomposition provides air-heater with hot-blast stove 12 to the thermal decomposition carbide furnace 11
With hot wind, hot gas that the thermal decomposition carbide furnace 11 generates by the quick cooling device 13 cool down rear portion gas then by
It is delivered to combustion gasification apparatus and participates in gasification reaction, and solid residue then carries out the recycling of carbon and carbide by carbon recovery system
And prepare clean environment firendly coal.And the part in the hot synthesis gas generated after gasification reaction in combustion gasification apparatus passes through connection
The thermal decomposition carbide furnace 11, which enters in the thermal decomposition carbide furnace 11, thermally decomposes waste materials.The heat may be implemented in this way
The reclaimed oil for preparing after carbide furnace 11 is thermally decomposed is decomposed, while the hot gas generated can promote combustion gasification apparatus gasification to close
At gas, the heat then generated is delivered to the waste heat recycling system and feedstock pre-processing system and combustion gas respectively
Makeup is set.The technical solution technically still more preferably of technical solution is in front：The combustion gasification apparatus with it is described
Be provided with heat exchanger 14 between thermal decomposition carbide furnace 11, the heat exchanger 14 respectively with the combustion gasification apparatus, described
Thermal decomposition carbide furnace 11 be connected to the waste heat recycling system, the heat exchanger 14 be used to ambient atmos being delivered to
The exchange hair-dryer 15 of heat exchanger 14 is connected to.In this way, the gasification that the heat exchanger 14 generates combustion gasification apparatus synthesizes
Heat exchange is carried out, the gasification synthesis gas that temperature decreases is delivered in the thermal decomposition carbide furnace 11 and participates in waste materials
Thermal decomposition, and the waste heat after exchanging heat then is delivered to the waste heat recycling system and carries out waste heat and recycles to produce regeneration
Oil, heat supply prepare flyash etc., can also be delivered to feedstock pre-processing system certainly and waste materials are dried.And
The effect for exchanging hair-dryer 15 is that the required gas that will exchange heat is delivered to the burning generated with combustion gasification apparatus in heat exchanger
Synthesis gas exchanges heat.
A kind of device being produced reclaimed oil using pyrolysis of waste vaporized carbon metaplasia of the present invention is please referred to Fig.1 middle related each
Figure, can also be on the basis of technical solution in front：The combustion gasification apparatus includes gasification combustion furnace 16, the gasification combustion
Burn 16 middle and lower part of stove be connected to recyclable fuel storage device and the thermal decomposition carbonizing plant, in the gasification combustion furnace 16 on
Portion is connected to the feedstock pre-processing system, and 16 top of the gasification combustion furnace is connected to urea water tank 17, the gasification, and combustion
The top of stove 16 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, the gasification combustion furnace 16 is so that gas and urea and burning air etc. generate gasification synthesis gas in its interior combustion gasification
Body, the gasification synthesis gas body are delivered in thermal decomposition carbonizing plant by the thermal decomposition carbonizing plant in communication help again
Waste materials thermal decomposition in the thermal decomposition carbonizing plant.Certainly previously described heat can be arranged between the two to hand over
Parallel operation 14, and the effect of heat exchanger 14 is to carry out heat exchange to the gasification synthesis gas that the gasification combustion furnace 16 generates, heat exchange
Heat afterwards is delivered to waste heat recycling system and carries out UTILIZATION OF VESIDUAL HEAT IN.And the gasification combustion furnace 16 is stored with recyclable fuel
Device connection is then that recyclable fuel is delivered to realization pyrolytic gasification reaction in the gasification combustion furnace 16, while the gasification
The top of combustion furnace 16 is connected to urea water tank 17, then is that urea is delivered to 16 internal reference of the gasification combustion furnace to add gasified reverse
It answers.16 middle and lower part of the gasification combustion furnace is connected to the thermal decomposition carbonizing plant, then is in the thermal decomposition carbonizing plant
A part for hot gas after thermal decomposition is delivered in the gasification combustion furnace 16 and completes gasification reaction by end direction.And it is described
The another part for thermally decomposing the gas after the thermal decomposition of the terminal position of carbonizing plant is then used to prepare reclaimed oil.And in the gas
The lower part for changing combustion furnace 16 is connected to the carbon recovery system, is that the lime-ash etc. after gasification, and combustion is carried out subsequent carbon and carbon
Clean environment firendly coal is prepared after the recycling of compound.Furthermore it is also possible to be, the urea water tank 17 and the gasification combustion furnace 16 it
Between be provided with urea nozzle 18, the urea nozzle 18 and 16 inside of the gasification combustion furnace are connected to, the urea nozzle
18 are connected to the urea water tank 17.It urea may be implemented so preferably conveys more uniformly to be transported to the gasification, and combustion
16 internal reference of stove adds gasification reaction.
A kind of device being produced reclaimed oil using pyrolysis of waste vaporized carbon metaplasia of the present invention is please referred to Fig.1 middle related each
Figure, can also be on the basis of technical solution in front：The waste heat recycling system includes waste heat boiler 19, waste heat for supplying
Device, afterheat steam power generator, waste heat gas discharging apparatus and waste heat flyash retracting device 35, the waste heat boiler 19 push up
Portion is connected to the afterheat steam power generator, and 19 output end of the waste heat boiler is connected to waste heat gas discharging apparatus, described
19 lower part of waste heat boiler is connect with the waste heat flyash retracting device 35, and the afterheat steam power generator is supplied with the waste heat
Thermal is connected to, and the waste heat boiler 19 is connected to the feedstock pre-processing system.Waste heat recycling system had been both in this way
Waste heat can be delivered to the afterheat steam power generator by waste heat boiler 19 and be converted into steam and generated electricity, and can be
Waste heat boiler 19 delivers heat to waste heat for supplying device and provides hot water or hot gas supply for factory or building, realizes industry
Or civilian heat supply.The gas that waste heat boiler 19 can have surplus heat band simultaneously is delivered in waste heat gas discharging apparatus, is prepared
Directly the partial reaction object is delivered in waste heat flyash retracting device 35 after flyash.In addition, under waste heat boiler 19
Portion is connect with waste heat flyash retracting device 35, then is that the lime-ash etc. for generating its waste heat boiler 19 is fed directly to waste heat fine coal
Grey retracting device 35 carries out the recycling of flyash.Waste heat evaporation power generator is connected to waste heat for supplying device simultaneously, will
Waste heat carries out industry or domestic heating for raw remaining heat after evaporating power generation by waste heat for supplying device.And the waste heat pot
Stove 19 is connected to the feedstock pre-processing system, then is that a part of gas in waste heat boiler 19 is delivered to the raw material
It makes full use of hot gas that the waste materials in drying machine 7 are dried in pretreatment system, subsequent handling is avoided to explode
Or it is on fire.Further preferred technical solution is：The afterheat steam power generator includes steam turbine 20 and steam-electric power
Machine 22, the steam turbine 20 and is connected with retarder 21 between the steam-driven generator 22, the steam turbine 20 and with
Retarder 21 is connected between the steam-driven generator 22, the steam turbine 20 is connected to the waste heat boiler 19.In this way, institute
The steam for stating the generation of waste heat boiler 19 is transported in steam turbine 20, then is delivered to steam-electric power after slowing down by retarder 21
Machine 22 carries out the steam-electric power of one of UTILIZATION OF VESIDUAL HEAT IN.Reclaimed oil can be not only prepared in this way, while there is steam-electric power, it will be entire
The waste heat generated in equipment makes full use of, and further increases the generating efficiency of power generator.In front on the basis of technical solution
Technical solution still more preferably is：The waste heat for supplying device includes condenser 23, heat supply cooling tower 24, pure water process
Device 25, high steam distributor 26 and heating unit 27, the condenser 23 are connected to the steam turbine 20, the condensation
Device 23 is taken cycle with heat supply cooling and is connected to, and the condenser 23 is connected to the pure water treatment device 25, described pure
Water treatment facilities 25 is connected to the high steam distributor 26, and the high steam distributor 26 connects with the heating unit 27
Logical, the high steam distributor 26 is connected to the steam turbine 20.The gas being discharged from the steam turbine 20 in this way
Enter in pure water treatment device 25 to enter back into after treatment in high steam distributor 26 by condenser 23 and be allocated,
Some certain high steam is directly fed directly to the high steam distributor 26, final high pressure from steam turbine 20
Hot gas or hot water are supplied respectively to heating unit 27 in communication and carry out heat supply by steam distributor 26.And heat supply cooling tower 24
Cycle heat exchange is carried out between condenser 23.It can also be that waste heat gas discharging apparatus includes on the basis of technical solution in front
It is loaded into hair-dryer 28, reaction machine 29, pressure fan 30, activated carbon hopper 32, pulverized limestone hopper 33, smoke filter 34 and chimney
31, the loading hair-dryer 28 is connected to the waste heat boiler 19, and the hair-dryer is connected to machine 29 is reacted, the reaction machine 29
Be connected to the feedstock pre-processing system, the activated carbon hopper 32 and the pulverized limestone hopper 33 and pressure fan 30 respectively with
The reaction machine 29 is connected to, and the reaction machine 29 is connected to smoke filter 34, and the smoke filter 34 is connected to chimney 31.
In this way, be loaded into hair-dryer 28 is delivered to reaction machine 29 by the hot gas of waste heat boiler 19, while the feedstock pre-processing system exports
Dry flue gas also enter reaction machine 29 in, while with react machine 29 be connected to activated carbon hopper 32 and pulverized limestone hopper 33 will be active
Charcoal and pulverized limestone are delivered to reaction machine 29 simultaneously, and outside air is delivered to reaction machine 29 by pressure fan 30, in reaction machine 29 into
After row is reacted and filtered by smoke filter 34, flue gas is transported to chimney 31 and is emitted into air, and remaining solid matter is then
It is transported in waste heat flyash retracting device 35.
A kind of device being produced reclaimed oil using pyrolysis of waste vaporized carbon metaplasia of the present invention is please referred to Fig.1 middle related each
Figure, can also be on the basis of technical solution in front：The carbon recovery system includes carbon cooler 36, carbon sorting machine 37, divides
Escaper, carbon recycling conveyor 38, carbon bin 39 and packing machine 40, the carbon cooler 36 is selected to disguise with the thermally decomposed carbon
Lower part connection is set, the carbon sorting machine 37 is located at 36 underface of the carbon cooler, the carbon sorting machine 37 and the sorting
Escaper material conveying-type connects, and the sorting escaper connect with carbon recycling conveyor 38, the carbon recycling conveyor 38 and
The carbon bin 39 is connected to, and the carbon bin 39 is connect with the packing machine 40.Thermal decomposition carbonizing plant lower part in this way is defeated
The unburned object sent or lime-ash etc. are transported to carbon sorting machine 37 after being cooled down into carbon cooler 36 and are sorted, after sorting
Waste residue is then discharged, and useful solid matter, that is, carbon and carbon compound are then fallen in carbon recycling conveyor 38, useful carbon
It exports after being then delivered to carbon bin 39 by carbon recycling conveyor 38 with carbon compound and is packed with packing machine 40.Similarly
The carbon and carbon compound that the gasification combustion furnace 16 generates again may be by above equipment and recycles to prepare environment-protecting clean
Coal.
A kind of device being produced reclaimed oil using pyrolysis of waste vaporized carbon metaplasia of the present invention is please referred to Fig.1 middle related each
Figure, can also be on the basis of technical solution in front：The Material supply system include sequentially connected raw material cutting machine 2,
Put into 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 with
The input terminal of the feedstock pre-processing system is connected to.Waste materials are fed into after the cutting of raw material cutting machine 2 in this way
It puts into hopper 3, is then delivered in raw material sorting machine 4 and is sorted by ingredient conveyor 1, useful waste materials enter
In raw material storage bin hopper 5, and the incombustible such as metal sorted out are then transported in incombustible storage bin hopper 47.Then combustible
Useful waste materials are delivered in measured quantity dispensing device 6 by ingredient conveyor 1 out of raw material storage bin hopper 5 and eventually enter into institute
It states feedstock pre-processing system and the pretreatments such as is dried.After such Material supply system can provide drying for subsequent handling
Humidity is less than 10% combustible waste material raw material, further ensures raw material supply and the safety of subsequent handling, avoids sending out
Situations such as life is on fire or explodes.
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 F represents purification oil, and H represents steam, and I represents waste water, and J represents exhaust gas, and K represents flyash,
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 (12)
1. a kind of device producing reclaimed oil using pyrolysis of waste vaporized carbon metaplasia, it is characterised in that：Including Material supply system,
Feedstock pre-processing system, thermal decomposition carbonizing plant, combustion gasification apparatus, waste heat recycling system, carbon recovery system and regeneration
Oil prepares collection system, and the Material supply system is connect with the feedstock pre-processing system for dry feedstock, the original
Material pretreatment system is connect with the thermal decomposition carbonizing plant, and the thermal decomposition carbonizing plant prepares collection system with reclaimed oil and connects
It connects, the combustion gasification apparatus is connect with the waste heat recycling system, the thermal decomposition carbonizing plant and the reclaimed oil
Preparation collection system, combustion gasification apparatus are connected with the carbon recovery system, and it includes quick that the reclaimed oil, which prepares collection system,
Cooling tower, reclaimed oil condensed device, reclaimed oil purifying column and reclaimed oil fuel reserve tank, it is described to be quickly cooled down top of tower and the thermal decomposition
Carbonizing plant is connected to, and the tower bottom that is quickly cooled down is connected to the reclaimed oil fuel reserve tank, it is described be quickly cooled down tower middle and lower part and
Reclaimed oil condensed device one end is connected to, and reclaimed oil condensed device lower part is connected to the reclaimed oil fuel reserve tank, and the reclaimed oil is solidifying
The contracting device other end is connected to the reclaimed oil purifying column, the purifying column upper and lower side respectively with the combustion gasification apparatus and described
Reclaimed oil fuel reserve tank is connected to.
2. a kind of device being produced reclaimed oil using pyrolysis of waste vaporized carbon metaplasia according to claim 1, feature are existed
In：The thermal decomposition carbonizing plant, the combustion gasification apparatus and the waste heat recycling system are located with the raw material in advance
Reason system connects.
3. a kind of device being produced reclaimed oil using pyrolysis of waste vaporized carbon metaplasia according to claim 2, feature are existed
In：The feedstock pre-processing system includes drying machine and drying hot-blast stove, the drying machine front and back end respectively with the raw material
Supply system is connected with the thermal decomposition carbonizing plant by device for transporting objects, the drying hot-blast stove and the drying machine
Connection, the thermal decomposition carbonizing plant, the combustion gasification apparatus and the waste heat recycling system are used with the drying
Hot-blast stove gas fed is connected to, and the drying machine is connected to the combustion gasification apparatus burning gases input type, the drying
Machine is connected to the waste heat recycling system dry flue gas input type.
4. a kind of device being produced reclaimed oil using pyrolysis of waste vaporized carbon metaplasia according to claim 3, feature are existed
In：The thermal decomposition carbonizing plant includes thermal decomposition carbide furnace, thermal decomposition hot-blast stove and quick cooling device, the drying machine
It is connect with the input terminal material input type of the thermal decomposition carbide furnace, the combustion gasification apparatus and thermal decomposition carbonization furnace gases are defeated
Enter formula connection, the output end of the thermal decomposition carbide furnace is connected to the quick cooling device, the quick cooling device upper end
Tower is quickly cooled down with described and the combustion gasification apparatus is connected to, the quick cooling device lower end is with carbon recycling respectively
System connection, the thermal decomposition hot-blast stove are connected to the thermal decomposition carbide furnace input terminal.
5. a kind of device being produced reclaimed oil using pyrolysis of waste vaporized carbon metaplasia according to claim 4, feature are existed
In：Be provided with heat exchanger between the combustion gasification apparatus and the thermal decomposition carbide furnace, the heat exchanger respectively with institute
State combustion gasification apparatus, the thermal decomposition carbide furnace is connected to the waste heat recycling system, the heat exchanger be used for
Ambient atmos are delivered to the exchange hair-dryer connection of heat exchanger.
6. a kind of utilization pyrolysis of waste vaporized carbon metaplasia production according to claim 1 to 5 any one claim is again
The device of oil generation, it is characterised in that：The combustion gasification apparatus includes gasification combustion furnace, the gasification combustion furnace middle and lower part with can
Generative fuel storage device is connected to the thermal decomposition carbonizing plant, the gasification combustion furnace middle and upper part and the pretreatment of raw material
System connectivity, the gasification combustion furnace top are connected to urea water tank, the top of the gasification combustion furnace and the thermally decomposed carbon
Connection is set in makeup, and the gasification combustion furnace lower part is connected to the carbon recovery system.
7. a kind of utilization pyrolysis of waste vaporized carbon metaplasia production according to claim 1 to 5 any one claim is again
The device of oil generation, it is characterised in that：The waste heat recycling system includes 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 and the afterheat steam
Power generator is connected to, and the waste heat boiler output end is connected to waste heat gas discharging apparatus, the waste heat boiler lower part with it is described
Waste heat flyash retracting device connects, and the afterheat steam power generator is connected to the waste heat for supplying device, the waste heat pot
Stove is connected to the feedstock pre-processing system.
8. a kind of device being produced reclaimed oil using pyrolysis of waste vaporized carbon metaplasia according to claim 7, feature are existed
In：The afterheat steam power generator includes steam turbine and steam-driven generator, the steam turbine and with the steam-electric power
Retarder is connected between machine, the steam turbine is connected to the waste heat boiler.
9. a kind of device being produced reclaimed oil using pyrolysis of waste vaporized carbon metaplasia according to claim 8, feature are existed
In：The waste heat for supplying device includes condenser, heat supply cooling tower, pure water treatment device, high steam distributor and heat supply
Unit, the condenser are connected to the steam turbine, and the condenser is taken cycle with heat supply cooling and is connected to, the condensation
Device is connected to the pure water treatment device, and the pure water treatment device is connected to the high steam distributor, the height
Pressure steam distributor is connected to the heating unit, and the high steam distributor is connected to the steam turbine.
10. a kind of device being produced reclaimed oil using pyrolysis of waste vaporized carbon metaplasia according to claim 7, feature are existed
In：Waste heat gas discharging apparatus includes being loaded into hair-dryer, reaction machine, pressure fan, activated carbon hopper, pulverized limestone hopper, flue gas mistake
Filter and 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
Be connected to the feedstock pre-processing system, the activated carbon hopper and the pulverized limestone hopper and pressure fan respectively with it is described anti-
Machine is answered to be connected to, the reaction machine is connected to smoke filter, and the smoke filter is connected to chimney.
11. a kind of utilization pyrolysis of waste vaporized carbon metaplasia production according to claim 1 to 5 any one claim is again
The device of oil generation, it is characterised in that：The carbon recovery system include carbon cooler, carbon sorting machine, sorting escaper, carbon recycling it is defeated
Machine, carbon bin and packing machine, the carbon cooler is sent to be connected to the thermal decomposition carbonizing plant lower part, the carbon sorts seat in the plane
At carbon cooler underface, the carbon sorting machine is connect with the sorting escaper material conveying-type, the sorting row
Device is put to connect with carbon recycling conveyor, the carbon recycling conveyor is connected to the carbon bin, the carbon bin with it is described
Packing machine connects.
12. a kind of utilization pyrolysis of waste vaporized carbon metaplasia production according to claim 1 to 5 any one claim is again
The device of oil generation, it is characterised in that：The Material supply system includes sequentially connected raw material cutting machine, input hopper, raw material
Conveyer, raw material sorting machine, raw material storage bin hopper and measured quantity dispensing device, the measured quantity dispensing device and the feedstock pre-processing system
Input terminal is connected to.
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