CN109266365A

CN109266365A - Ingredient separate type charcoal element system

Info

Publication number: CN109266365A
Application number: CN201811033890.0A
Authority: CN
Inventors: 铃木利昭
Original assignee: Ren Kangping
Current assignee: Ren Kangping
Priority date: 2018-09-05
Filing date: 2018-09-05
Publication date: 2019-01-25
Anticipated expiration: 2038-09-05
Also published as: CN109266365B

Abstract

The present invention relates to ingredient separate type charcoal element systems, the container of waste is loaded through container entrance, moisture vaporising device, high-molecular compound purification device, ingredient the separation decomposer of connection, the charcoal element compound cooling device of charcoal element compound can be converted with oxygen-free environment by passing sequentially through, and container is exported through container outlet；It wherein, include multiple process chambers inside each device, each inner treatment chamber has the transport establishment for moving container；Discharge pipe for filling the ingress pipe of inert gas and for gas in chambers to be discharged；The post-treated recycling of gas being discharged in the chambers.Since waste is by oxygen-free environment charcoal element treatment process, the gas of the inside of chambers is exported, inert gas is filled, prevents burning from generating toxic and harmful gas；Gas after chambers export recycles recycling after post treatment；The generation for reducing waste residue during charcoal element, reduces processing cost, improves treatment effeciency.

Description

Ingredient separate type charcoal element system

Technical field

The present invention relates to solid waste charcoal element processing technology fields, more particularly to ingredient separate type charcoal element Change system.

Background technique

With the fast development of city and economy, pollution caused by common waste and industrial waste becomes increasingly conspicuous, City environmental quality has been seriously affected, the health of the people is threaten.

At present for solid waste generally using landfill, burning, solidification etc., but secondary pollution is generated in disposal process, Poisonous fume, dioxin are such as generated, the problems such as difficult high-concentration garbage percolate.But due to municipal solid wastes Management system is all incomplete, and solid waste management problem is still serious.

Based on this, the system for how providing a kind of ingredient separate type charcoal element is asking for those skilled in the art's urgent need to resolve Topic.

Summary of the invention

In view of this, inhibiting harmful during charcoal element the present invention provides a kind of ingredient separate type charcoal element system The generation of gas and extra residue improves the efficiency of charcoal element.

To achieve the goals above, the present invention adopts the following technical scheme:

Ingredient separate type charcoal element system, the charcoal elementization for waste are handled；The container for loading waste enters through container Mouthful, the evaporation of connection can be converted with oxygen-free environment and remove the moisture vaporising device of moisture in waste, pass through by passing sequentially through Thermal decomposition removal waste in high-molecular compound high-molecular compound purification device, separation waste in organic substance at The charcoal element compound cooling device of the charcoal element compound of decomposition is separated in separation decomposer, cooling waste, and container is through container Outlet output；It wherein, include multiple process chambers inside each device, each inner treatment chamber has the transport for moving container Mechanism；Discharge pipe for filling the ingress pipe of inert gas and for gas in chambers to be discharged；In the chambers The post-treated recycling of the gas of discharge.It can be seen via above technical scheme that compared with prior art, the present disclosure provides A kind of ingredient separate type charcoal element system, since waste passes through in oxygen-free environment charcoal element treatment process, by chambers Internal gas export, fills inert gas, prevents burning from generating toxic and harmful gas；Gas after chambers export passes through Post-processing recycling recycling；The generation for reducing waste residue during charcoal element, reduces processing cost, improves treatment effeciency.

It preferably, further include the standby preparation device of the standby preparation device in front and rear portion；The standby preparation device in front is located at Between container entrance and moisture vaporising device, and connection container entrance and moisture vaporising device can be converted；For preventing inside Foul smell or gas leak into the external standby preparation part in front；The standby preparation device in rear portion be located at charcoal element compound cooling device with Between container outlet；And connection charcoal element compound cooling device and container outlet can be converted, for preventing internal foul smell or gas Leak into the external standby preparation part in rear portion.

It preferably, further include multiple division plate doors；Multiple division plate doors can convert and be connected to the standby preparation device in front, moisture steams Transmitting apparatus, high-molecular compound purification device, ingredient separation decomposer, charcoal element compound cooling device, the standby preparation dress in rear portion Between the multiple process chambers set.

Preferably, ingress pipe is connected to for injecting inert gas inside chambers with gas generating unit；Simultaneously The gas inside chambers is discharged by exhaust pipe；The processing of the standby preparation device of the standby preparation device of its middle front part and rear portion Gas of the room by exhaust pipe discharge enters deodorization, smoke removing device；The gas of moisture vaporising device process chamber discharge is cold through evaporating But cooling trough is flowed into after device condensation；High-molecular compound purification device, ingredient separation decomposer and charcoal element compound are cooling The gas of each process chamber discharge of device enters liquefied substance accumulator tank after liquefying device.

Preferably, moisture vaporising device, high-molecular compound purification device, ingredient separation decomposer and charcoal element compound are cold It but include that temperature sensor is used to detect the temperature inside chambers in the process chamber of device；Moisture vaporising device, height The inner treatment chamber of molecular compound purification device and ingredient separation decomposer all has heating part；Charcoal element compound cooling device Inner treatment chamber all have cooling end.

It preferably, further include electronic control unit；Electronic control unit communicates to connect the standby preparation device in front, moisture steams Transmitting apparatus, high-molecular compound purification device, ingredient separation decomposer, charcoal element compound cooling device, the standby preparation dress in rear portion It sets and container outlet.

Preferably, the transport establishment of each process chamber includes transport base, power part, drive shaft, heat insulation support knot Structure body；Transport base is for moving container；Transport base connects drive shaft one end；It is offered on the side wall of each process chamber One shaft mounting hole；Heat insulation support structural body is supported in shaft mounting hole, and the drive shaft other end is in heat insulation support structural body Portion, and extend out on the outside of process chamber and connect power part.

Preferably, heat insulation support structural body includes the first cover board body, the second cover board body, inner closure plate and external occlusion Plate；

First cover board body is installed in drive shaft；First cover board body has opening on processing chamber outer wall direction, forms the One annulus；Second cover board body is covered on the first cover board body, forms the second annulus；Inner closure plate is installed on axis peace At the inner wall for filling the process chamber of hole corresponding position, outside occlusion plate is installed on the outer wall of the process chamber of shaft mounting hole corresponding position At face.

Preferably, ingredient separates the process chamber of decomposer for stratiform heat insulating structure body, on stratiform heat insulating structure body inner wall With multiple lug bosses, change the flow direction of the gas of separation；Ingredient, which separates, also has wind at the top of the process chamber of decomposer 7 Fan, for stirring isolated gas.

Preferably, container entrance, the standby preparation device in front, moisture vaporising device, high-molecular compound purification device, at Separation decomposer, charcoal element compound cooling device, the standby preparation device in rear portion and container outlet are structure as a whole and are installed on shell In vivo；Housing bottom is equipped with walking arrangement；Case top has funnel part；Waste is put into through heavy equipment to funnel part In, it is taken out after charcoal element through taking-up portion.

Detailed description of the invention

In order to more clearly explain the embodiment of the invention or the technical proposal in the existing technology, to embodiment or will show below There is attached drawing needed in technical description to be briefly described, it should be apparent that, the accompanying drawings in the following description is only this The embodiment of invention for those of ordinary skill in the art without creative efforts, can also basis The attached drawing of offer obtains other attached drawings.

Fig. 1 attached drawing is the side schematic view of ingredient separate type charcoal element system provided by the invention；

Fig. 2 attached drawing is the floor map of ingredient separate type charcoal element system provided by the invention；

Fig. 3 attached drawing is that the ingredient of ingredient separate type charcoal element system provided by the invention separates the cross-sectional view of decomposer；

Fig. 4 attached drawing is the amplification of the heat insulation support structure of the drive shaft of ingredient separate type charcoal element system provided by the invention Schematic diagram；

Fig. 5 attached drawing is the control principle drawing of ingredient separate type charcoal element system provided by the invention；

Fig. 6 attached drawing is the process flowchart of ingredient separate type charcoal element system provided by the invention；

Fig. 7 attached drawing is the schematic diagram of one embodiment of ingredient separate type charcoal element system provided by the invention；

Fig. 8 attached drawing is the schematic diagram of another embodiment of ingredient separate type charcoal element system provided by the invention；

In figure: 1 is ingredient separate type charcoal element system, and 2 be container, and 3 be container entrance, and 4 be the standby preparation device 5 in front It is high-molecular compound purification device for moisture vaporising device, 6,7 separate decomposer for ingredient, and 8 be the cooling dress of charcoal element compound 9 are set as the standby preparation device in rear portion, 10 be container outlet, and 11-1~11-2 is the first to the second front preparation room,

The the first to the second vaporization chamber of the position 11-3~11-4,11-5~11-7 remove room for first to third,

11-8~11-12 is the first to the 5th decomposition chamber, and 11-13~11-15 is first to third cooling chamber,

11-16~11-17 is the first to the second rear portion cooling chamber, and 12-1~12-17 is the first to the 17th transport establishment,

13-1~13-17 is the first to the 17th limit switch, and 14-1~14-17 is the first to the 17th ingress pipe,

15-1~15-17 is the first to the 17th discharge pipe, and 16 be gas generating unit,

17-1~17-2 is the first to the second deodorization smoke removing device, and 18-1~18-13 is the first to the 13rd temperature sensing Device,

19-1~19-10 is the first to the tenth heating part, and 20 be steam cooling device,

23-1~23-3 is first to third liquefying device, and 25-1~25-3 is first to third cooling end,

26-1~26-18 is the first to the 18th division plate door, and 27-1~27-18 closes means for first to eighteenmo,

30 be stratiform heat insulating structure body, and 33 be lug boss, and 36 be drive shaft, and 39 be heat insulation support structural body,

52 be electronic control unit.

Specific embodiment

Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete Site preparation description, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other Embodiment shall fall within the protection scope of the present invention.

As shown in Figure 1 and Figure 2, ingredient separate type charcoal element system 1 provided by the invention is that one kind can make all to put into The waste (waste in this application refers to as the waste of household appliances etc. and rubbish etc.) of container 2 ingredient separation be System.

Ingredient separate type charcoal element system 1 is configured with container entrance 3 and preposition standby preparation device 4, moisture vaporising device 5, high-molecular compound purification device 6, ingredient separation decomposer 7, charcoal element cooling device 8, the standby preparation device 9 of postposition, Container outlet 10.

Container entrance 3, preposition standby preparation device 4, moisture vaporising device 5, high-molecular compound purification device 6, ingredient Decomposer 7, charcoal element compound cooling device 8, the standby preparation device 9 of postposition, container outlet 10 are separated all from charcoal element chemical industry journey The front of direction X starts arranged in series setting in sequence.

Dress is decomposed in preposition standby preparation device 4, moisture vaporising device 5, high-molecular compound purification device 6, ingredient separation Set 7, charcoal element compound cooling device 8, the standby preparation device 9 of postposition is integrated.Container entrance 3 is by drum conveyor etc. It constitutes, configures in the front of preposition standby preparation device 4, container 2 is moved into preposition standby preparation device 4.Container outlet 10 are made of drum conveyor etc., and configuration removes at the rear of preposition standby preparation device 9 from the standby preparation device 9 of postposition Container 2.

Preposition standby preparation device 4 be below chambers 11 release when, in order to prevent adverse current and come inside foul smell Device external and being arranged is leaked to gas, is mounted with the first preposition preposition preparation room 11-2 conduct of preparation room 11-1 and second Process chamber.In addition, preposition standby preparation device 4 is not limited to that two preposition preparation rooms can only be installed, standard can be increased or decreased The quantity of standby room.

First preposition preparation room 11-1 is the preparation room positioned at the forefront of ingredient separate type charcoal element system 1, is room temperature Preparation room.The first conveyor structure (drum conveyor etc.) of removable container 2 is provided in first preposition preparation room 11-1 First limit switch 13-1 of the position of 12-1 and decision container 2.First preposition preparation room 11-1, which is connected to, to be externally introduced As the first ingress pipe 14-1 of special gas nitrogen, inner air (oxygen) is emitted into outside in addition, being also connected with First delivery pipe 15-1.First preposition preparation room 11-1 gives off the mode of air by filling nitrogen, is formed in air environment Nitrogen environment.

Similarly, the second preposition preparation room 11-2 be preparation room position more preposition than first more posteriorly be room temperature preparation room.The The of the second conveyor structure 12-1 of mobile container 2 and the position of decision container 2 is provided in two preposition preparation room 11-2 Two limit switch 13-2.Second preposition preparation room 11-2 is connected to the second ingress pipe 14-2 for being externally introduced nitrogen, in addition, It has been also connected with and inner air is emitted into the second external delivery pipe 15-2.Second preposition preparation room 11-2 passes through filling nitrogen, The mode of air is given off, nitrogen environment is formed.

First ingress pipe 14-1 and the second ingress pipe 14-2 are connected to gas generation apparatus 16, utilize gas generation apparatus 16 The nitrogen taken out from atmosphere is set to be directed into the first preposition preposition preparation room 11-2 of preparation room 11-1 and second.In addition, gas produces Generating apparatus 16 can produce other gases also to replace nitrogen.

First delivery pipe 15-1 and the second delivery pipe 15-2 is connected to the air that will be emitted and carries out as hot environment First deodorization smoke consuming apparatus 17-1 of the processing such as deodorization and smoke abatement.First deodorization smoke consuming apparatus 17-1 carries out deodorization and smoke abatement etc. After processing, purified air is emitted into outside.

Moisture vaporising device 5 is the equipment of moisture (for example, 90%) in evaporation and removing waste, is configured with first Vaporization chamber 11-3 and the second vaporization chamber 11-4 are as process chamber.In addition, moisture vaporising device 5 be not limited in can only there are two steam Room is sent out, vaporization chamber can be increased or decreased.First vaporization chamber 11-3 is the steaming of the position preparation room 11-2 more preposition than second more posteriorly Send out room.

First vaporization chamber 11-3 is configured with the third transport establishment 12-3 of mobile container 2 and determines that the position of container 2 is used Third limit switch 13-3 and measure temperature the first temperature sensor 18-1.First vaporization chamber 11-3, which will be provided with, to be held The waste of device 2 is heated to the first heating part (such as electric heater etc.) 19-1 of assigned temperature (such as 150 DEG C).First steams Hair room 11-3 is connected to the third ingress pipe 14-3 for being externally introduced nitrogen, in addition, being also connected with the internal water generated of discharge The third delivery pipe 15-3 of steam.First vaporization chamber 11-3 gives off the mode of vapor by filling nitrogen, forms nitrogen Environment.

Second vaporization chamber 11-4 is the vaporization chamber of the position preparation room 11-3 more preposition than first more posteriorly.Second vaporization chamber 11-4 Be configured with mobile container 2 the 4th transport establishment 12-4 and determine container 2 position the 4th limit switch 13-4 and Measure the second temperature sensor 18-2 of temperature.Second vaporization chamber 11-4 is provided with and is heated to specifying by the waste of container 2 The second heating part (such as electric heater etc.) 19-2 of temperature (such as 150 DEG C).Second vaporization chamber 11-4 is connected to from outside The 4th ingress pipe 14-4 of nitrogen is imported, in addition, being also connected with the 4th delivery pipe 15- of the internal vapor generated of discharge 4.Second vaporization chamber 11-4 gives off the mode of vapor by filling nitrogen, forms nitrogen environment.Third ingress pipe 14-3 and 4th ingress pipe 14-4 is connected to gas generating unit 16, and the nitrogen extracted from atmosphere using gas generating unit 16 is imported To the first vaporization chamber 11-3 and the second vaporization chamber 11-4.

Third delivery pipe 15-3 and the 4th delivery pipe 15-4 cool down the vapor emitted, liquefaction, and even It is connected to the evaporation processing equipment 20 for being handled (deodorization).The water that evaporation processing equipment 20 generates is store via the first communicating pipe 21-1 Ensconce cooling water slot 22.Told about in aftermentioned content be housed in cooling water with the cooling water of slot 22 be cooling charcoal element compound and into Row circulation, is used for first to third cooling end 25-1~25-3.

First heating part 19-1 and the second heating part 19-2 is the evaporation of a kind of not direct and the first vaporization chamber 11-3 and second The structure of the vapor contact of room 11-4.

High-molecular compound purification device 6 be it is a kind of to be mixed into plastic refuse etc. high-molecular compound (chlorine component, Petroleum components etc.) equipment that is thermally decomposed, and remove these high-molecular compounds (dechlorination), it is net to third to be equipped with first Change room 11-5~11-7 as process chamber.In addition, high-molecular compound purification device 6 is not limited in 3 clean rooms, Ke Yizeng Add deduct few clean room.

First clean room 11-5 is positioned at the clean room than the second vaporization chamber 11-4 more posteriorly.First clean room 11-5 setting 5th transport establishment 12-5 of mobile container 2 and the 5th limit switch 13-5 and measurement temperature for determining 2 position of container Third temperature sensor 18-3.First clean room 11-5, which is provided with, is heated to assigned temperature (such as the waste of container 2 300 DEG C) third heating part 19-3.First clean room 11-5 is connected to the 5th ingress pipe 14- for being externally introduced nitrogen 5, but also it is connected to the 5th delivery pipe 15-5 of the cracked gas of the internal high-molecular compound generated of discharge.First clean room 11-5 discharges the cracked gas of high-molecular compound by filling nitrogen, forms nitrogen environment.

Second vaporization chamber 11-6 is positioned at the clean room than the first vaporization chamber 11-5 more posteriorly.Second clean room 11-6 setting 6th transport establishment 12-6 of mobile container 2 and the 6th limit switch 13-6 and measurement temperature for determining 2 position of container 4th temperature sensor 18-4.Second clean room 11-6, which is provided with, is heated to assigned temperature (such as the waste of container 2 300 DEG C) the 4th heating part 19-4.Second clean room 11-6 is connected to the 6th ingress pipe 14- for being externally introduced nitrogen 6, but also it is connected to the 6th delivery pipe 15-6 of the cracked gas of the internal high-molecular compound generated of discharge.Second clean room 11-6 discharges the cracked gas of high-molecular compound by filling nitrogen, forms nitrogen environment.

Third vaporization chamber 11-7 is positioned at the clean room than the second vaporization chamber 11-6 more posteriorly.Third clean room 11-7 setting 7th transport establishment 12-7 of mobile container 2 and the 7th limit switch 13-7 and measurement temperature for determining 2 position of container 5th temperature sensor 18-5.Third clean room 11-7, which is provided with, is heated to assigned temperature (such as the waste of container 2 300 DEG C) the 5th heating part 19-5.Third clean room 11-7 is connected to the 7th ingress pipe 14- for being externally introduced nitrogen 7, but also it is connected to the 7th delivery pipe 15-7 of the cracked gas of the internal high-molecular compound generated of discharge.Third clean room 11-7 discharges the cracked gas of high-molecular compound by filling nitrogen, forms nitrogen environment.

5th to the 7th ingress pipe 14-5~14-7 is connected to gas generating unit 16, using gas generating unit 16 from The nitrogen extracted in atmosphere is directed into first to third clean room 11-5~11-7.

5th to the 7th delivery pipe 15-5~15-7 cools down the cracked gas of high-molecular compound, liquefaction, and even It is connected to the first liquefying device 23-1 for being handled (deodorization).First liquefying device 23-1 processing liquefied substance via It is housed in the first liquefied substance accumulator tank 24-1 the second communicating pipe 21-2.First liquefied substance accumulator tank 24-1 storage liquefied substance be containing Chlorine compound, it by external reaction unit, reacts with Residual water, is recycled as hydrochloric acid and chlorine.Pass through this side Formula can inhibit the generation of chlorine.In addition, the first liquefied substance accumulator tank 23-1 also can handle survival gas.Third is to slender acanthopanax Hot portion 19-3~19-5 is that a kind of not direct high-molecular compound cracked gas with first to third clean room 11-5~11-7 connects The structure of touching.

Ingredient separation decomposer 7 is the equipment that the organic components of a kind of pair of waste carry out separation and charcoal element, It is separated into the organic matter other than macromolecule chemical combination at the charcoal element of Carbon Materials and other ingredients in such a way that ingredient separates Reason.Ingredient separates decomposer 7 and first to the 5th decomposition chamber 11-8~11-12 is arranged as process chamber.In addition, ingredient separation point Solution device 7 is not limited in 5 decomposition chambers, can suitably increase or decrease decomposition chamber quantity.First decomposition chamber 11-8 is position In the decomposition chamber than third clean room 11-7 more posteriorly.First decomposition chamber 11-8 is provided with the 8th transporter of mobile container 2 The 6th temperature sensor 18-6 of the 8th limit switch 13-8 and measurement temperature of structure 12-8 and decision 2 position of container.The One decomposition chamber 11-8 is provided with the 6th heating part 19-6 that the waste of container 2 is heated to assigned temperature (such as 450 DEG C).First Decomposition chamber 11-8 is connected to the 8th ingress pipe 14-8 for being externally introduced nitrogen, but also is connected to the internal generation of discharge 8th delivery pipe 15-8 of the cracked gas (including oil etc.) of charcoal elementization processing.First decomposition chamber 11-8 passes through filling nitrogen, row The cracked gas of charcoal elementization processing is put, nitrogen environment is formed.

Second decomposition chamber 11-9 is positioned at the decomposition chamber than the first decomposition chamber 11-8 more posteriorly.Second decomposition chamber 11-9 setting 9th transport establishment 12-9 of mobile container 2 and the 9th limit switch 13-9 and measurement temperature for determining 2 position of container 7th temperature sensor 18-7.Second decomposition chamber 11-9 be provided with by the waste of container 2 be heated to assigned temperature (such as 450 DEG C) the 7th heating part 19-7.Second decomposition chamber 11-9 is connected to the 9th ingress pipe 14- for being externally introduced nitrogen 9, but also it is connected to the 9th delivery pipe 15-9 of the cracked gas of the internal charcoal elementization processing generated of discharge.Second decomposition chamber 11-9 forms nitrogen environment by filling nitrogen, the cracked gas of discharge charcoal elementization processing.

Third decomposition chamber 11-10 is positioned at the decomposition chamber than the second decomposition chamber 11-9 more posteriorly.Third decomposition chamber 11-10 is set It has set the tenth transport establishment 12-10 of mobile container 2 and has determined the tenth limit switch 13-10 and the measurement of 2 position of container 8th temperature sensor 18-8 of temperature.Third decomposition chamber 11-10, which is provided with, is heated to assigned temperature for the waste of container 2 The 8th heating part 19-8 of (such as 450 DEG C).Third decomposition chamber 11-10 is connected to be externally introduced nitrogen the tenth and imports Pipe 14-10, but also it is connected to the tenth delivery pipe 15-10 of the cracked gas of the internal charcoal elementization processing generated of discharge.Third Decomposition chamber 11-10 forms nitrogen environment by filling nitrogen, the cracked gas of discharge charcoal elementization processing.

4th decomposition chamber 11-11 is positioned at the decomposition chamber than third decomposition chamber 11-10 more posteriorly.4th decomposition chamber 11-11 The 11st limit switch 13-11 of the 11st transport establishment 12-11 and decision 2 position of container provided with mobile container 2 with And the 9th temperature sensor 18-9 of measurement temperature.4th decomposition chamber 11-11 is provided with and is heated to referring to by the waste of container 2 Determine the 9th heating part 19-9 of temperature (such as 450 DEG C).4th decomposition chamber 11-11 is connected to be externally introduced nitrogen the tenth One ingress pipe 14-11, but also it is connected to the 11st delivery pipe 15- of the cracked gas of the internal charcoal elementization processing generated of discharge 11.4th decomposition chamber 11-11 forms nitrogen environment by filling nitrogen, the cracked gas of discharge charcoal elementization processing.

5th decomposition chamber 11-12 is positioned at the decomposition chamber than the 4th decomposition chamber 11-11 more posteriorly.5th decomposition chamber 11-12 The 12nd limit switch 13-12 of the 12nd transport establishment 12-12 and decision 2 position of container provided with mobile container 2 with And the tenth temperature sensor 18-10 of measurement temperature.5th decomposition chamber 11-12 is provided with and is heated to the waste of container 2 Tenth heating part 19-10 of assigned temperature (such as 450 DEG C).5th decomposition chamber 11-12, which is connected to, is externally introduced nitrogen 12nd ingress pipe 14-12, but also it is connected to the 12nd discharge of the cracked gas of the internal charcoal elementization processing generated of discharge Pipe 15-12.5th decomposition chamber 11-12 forms nitrogen environment by filling nitrogen, the cracked gas of discharge charcoal elementization processing.

8th to the 12nd ingress pipe 14-8~14-12 is connected to gas generating unit 16, utilizes gas generating unit 16 The nitrogen extracted from atmosphere is directed into the first~the 5th decomposition chamber 11-8~11-12.8th~the 12nd delivery pipe 15-8 The cracked gas that~15-12 handles charcoal elementization liquefies, and is connected to the second liquefaction processing for generating the liquefied substance of oil Device 23-2.The liquefied substance of second liquefying device 23-2 processing is housed in the second liquefied substance via third connecting pipe 21-3 and returns Receive slot 24-2.Second liquefying device 23-2 also can handle survival gas etc..

6th to the tenth heating part 19-6~19-10 is a kind of not direct and first to the 5th clean room 11-8~11-2 The structure of the cracked gas contact of charcoal elementization processing.That is, ingredient separates the deoxidation in a manner of non-burning of decomposer 7, in oxygen-free environment Under be moved to waste in first to the 5th decomposition chamber 11-8~11-2, lower than under assigned temperature (such as 450 DEG C), The ingredient of organic matter is separated, charcoal element generates charcoal element compound.In this case, ingredient separating device 7 is being lower than assigned temperature In the environment of (such as 450 DEG C), it can prevent noble metal from volatilizing.I.e. waste according to its waste characteristic and meet recycling material Ingredient separation is carried out at a temperature of the management of characteristic.In addition, the nitrogen in air is utilized, no for the charcoal element for realizing waste Burn oxygen, can prevent carbon dioxide packing.

Charcoal element compound cooling device 8 be a kind of charcoal element compound for separating the components into the generation of device 7 it is cooling it is (indirectly cooling) extremely Temperature (such as 50 DEG C or less) that is nonflammable and being not easy to evaporate, is provided with first to third cooling chamber 11-13~11-15 as at Manage room.Charcoal element compound cooling device 8 is not limited only to 3 cooling chambers, can suitably increase or decrease cooling chamber quantity.

First cooling chamber 11-13 is that have positioned at the cooling chamber than the 5th position decomposition chamber 11-12 more posteriorly to ingredient point The charcoal element compound generated from decomposer 6 is cooled down, and avoids charcoal element compound volume is quickly swollen from rising as surge-chamber moreover, having Function.First cooling chamber 11-13 is provided with the 13rd transport establishment 12-13 of mobile container 2 and determines 2 position of container 13rd limit switch 13-13 and the 11st temperature sensor 18-11 for measuring temperature.First cooling chamber 11-13 setting Charcoal element compound is cooled to the first cooling end (such as water cooling) 25-1 of assigned temperature (such as 50 DEG C).First cooling chamber 11-13 It is connected to the 13rd ingress pipe 14-13 for being externally introduced nitrogen, but also is connected to the internal cracked gas generated of discharge 13rd delivery pipe 15-13.First cooling chamber 11-13 discharges internal cracked gas by filling nitrogen, forms nitrogen ring Border.

Second cooling chamber 11-14 is positioned at the cooling chamber than the first position cooling chamber 11-13 more posteriorly.Second cooling chamber 11-14 is provided with the 14th transport establishment 12-14 of mobile container 2 and determines the 14th limit switch 13- of 2 position of container 14 and measure temperature the 12nd temperature sensor 18-12.Second cooling chamber 11-14 is provided with and is cooled to charcoal element compound The second cooling end (such as water cooling etc.) 25-2 of assigned temperature (such as 50 DEG C).Second cooling chamber 11-14 be connected to by nitrogen from 14th ingress pipe 14-14 of external importing, but also it is connected to the 14th discharge of the internal cracked gas generated of discharge Pipe 15-14.Second cooling chamber 11-14 discharges internal cracked gas by filling nitrogen, forms nitrogen environment.

Third cooling chamber 11-15 is positioned at the cooling chamber than the second position cooling chamber 11-14 more posteriorly.Third cooling chamber 11-15 is provided with the 15th transport establishment 12-15 of mobile container 2 and determines the 15th limit switch 13- of 2 position of container 15 and measure temperature the tenth three-temperature sensor 18-13.Third cooling chamber 11-15 is provided with and is cooled to charcoal element compound Third cooling end (such as water cooling) 25-3 of assigned temperature (such as 50 DEG C).Third cooling chamber 11-15 is connected to nitrogen from outside 15th ingress pipe 14-15 of importing, but also it is connected to the 15th delivery pipe 15- of the internal cracked gas generated of discharge 15.Third cooling chamber 11-15 discharges internal cracked gas by filling nitrogen, forms nitrogen environment.

First to third cooling end 25-1~25-3 is a kind of Water cooling type that the water to circulation is used, it is not direct with Internal cracked gas contact, first to third cooling chamber 11-13~11-5 charcoal element compound can be cooled to will not cause to fire The temperature burnt and evaporated, that is, this is a kind of mode cooled down indirectly.In this way, to utilization first to third cooling chamber The charcoal element compound of 11-13~11-15 temperature difference recycling carries out exhaustive division.

13rd to the 15th ingress pipe 14-3~14-15 is connected to gas generating unit 16, utilizes gas generating unit 16 nitrogen extracted from atmosphere are directed into first to third cooling chamber 11-13~11-15.13rd to the 15th delivery pipe The cracked gas that 15-13~15-15 is connected to the processing of charcoal elementization liquefies, the third liquefying device of the processing such as deodorization 23-3.The liquefied substance of third liquefying device 23-3 processing is housed in third liquid recovery via the 4th communicating pipe 21-4 In 24-3.Third liquefying device 23-3 also can handle survival gas etc..

The standby preparation device 9 of postposition is front chambers in release, in order to prevent adverse current and the inside foul smell that comes and Gas leaks to device external and being arranged, is mounted with the first postposition preparation room 11-16 and the second postposition preparation room 11-17 conduct Process chamber.In addition, the standby preparation device 9 of postposition is not limited to that two postposition preparation rooms can only be installed, standard can be increased or decreased The quantity of standby room.

The standby preparation room 11-16 of first postposition is in positioned at the preparation room than the position third cooling chamber 11-15 more posteriorly Room temperature.The standby preparation room 11-16 of first postposition is provided with the 16th transport establishment 12-16 of mobile container 2 and determines container 2 16th limit switch 13-16 of position.The standby preparation room 11-16 of first postposition is provided be externally introduced nitrogen the 16 ingress pipe 14-16, but also it is connected to the 16th discharge of the internal cracked gas generated of discharge and air (oxygen) Pipe 15-16.The standby preparation room 11-16 of first postposition discharges internal cracked gas by filling nitrogen, forms nitrogen environment.

The standby preparation room 11-17 of second postposition is the preparation room being located at than the first position postposition preparation room 11-16 more posteriorly, It is preparation room of the position after, is in room temperature.The standby preparation room 11-17 of second postposition is provided with the tenth of mobile container 2 Seven transport establishment 12-17 and the 17th limit switch 13-17 for determining 2 position of container.The standby preparation room 11-17 of second postposition is set Set the 17th ingress pipe 14-17 for being externally introduced nitrogen, but also be connected to the internal cracked gas generated of discharge with And the 17th delivery pipe 15-17 of air (oxygen).The standby preparation room 11-17 of second postposition, which passes through, fills nitrogen, in discharge The cracked gas in portion forms nitrogen environment.

The 17th ingress pipe 14-17 of 16th ingress pipe 14-16 is connected to gas generating unit 16, is occurred using gas The nitrogen extracted from atmosphere is directed into first postposition preparation room 11-16 the second postposition preparation room 11-17 by device 16.

16th delivery pipe 15-16, the 17th delivery pipe 15-17, which are connected to, can make the cracked gas of discharge and air The second deodorization smoke consuming apparatus 17-2 of the processing such as deodorization and smoke elimination is carried out for hot environment.Second deodorization smoke consuming apparatus 17-2 exists After carrying out the processing such as deodorization and smoke elimination, the air of purification is emitted into outside.

In addition it is also possible to keep the first deodorization smoke consuming apparatus 17-1 and the second deodorization smoke consuming apparatus 17-2 structure-integrated, at The deodorization smoke consuming apparatus being integrated.

Chambers 11-1~17-1 is the structure that can be connected to (can open) respectively in charcoal element chemical industry journey direction X.Respectively Process chamber 11-1 to 11-17 is separately in the state of separating by each partition door 26-1 to 26-18.

First preposition preparation room 11-1 is configured with the first partition door 26-1 in the side that can move into container 2.First partition door 26- 1 opens or closes the immigration mouth 28 of the side of the first preposition preparation room 11-1 by the first shutter means (transmission device) 27-1. Between the first preposition preposition preparation room 11-2 of preparation room 11-1 and second, it is configured with the second partition door 26-2.Second partition door 26-2 is logical Cross the other side and the second preposition preparation room 11-2 that the second shutter means 27-2 opens or closes the first preposition preparation room 11-1 Side.

Between second preposition preparation room 11-2 and the first vaporization chamber 11-3, it is configured with third partition door 26-3.Third partition door 26- 3 by third shutter means 27-3 open or close the second preposition preparation room 11-2 the other side and the first vaporization chamber 11-3 one Side.Between first vaporization chamber 11-3 and the second vaporization chamber 11-4, it is configured with the 4th partition door 26-4.4th partition door 26-4 passes through the 4th Shutter means 27-4 opens or closes the other side of the first vaporization chamber 11-3 and the side of the second vaporization chamber 11-4.

Between second vaporization chamber 11-4 and the first clean room 11-5, it is configured with the 5th partition door 26-5.5th partition door 26-5 is logical It crosses the 5th shutter means 27-5 and opens or closes the other side of the second vaporization chamber 11-4 and the side of the first clean room 11-5.First Between clean room 11-5 and the second clean room 11-6, it is configured with the 6th partition door 26-6.6th partition door 26-6 passes through the 6th opening and closing hand Section 27-6 opens or closes the other side of the first clean room 11-5 and the side of the second clean room 11-6.

Between second clean room 11-6 and third clean room 11-7, it is configured with the 7th partition door 26-7.7th partition door 26-7 is logical It crosses the 7th shutter means 27-7 and opens or closes the other side of the second clean room 11-6 and the side of third clean room 11-7.

Between third clean room 11-7 and the first decomposition chamber 11-8, it is configured with the 8th partition door 26-8.8th partition door 26-8 is logical It crosses the 8th shutter means 27-8 and opens or closes the other side of third clean room 11-7 and the side of the first decomposition chamber 11-8.First Between decomposition chamber 11-8 and the second decomposition chamber 11-9, it is configured with the 9th partition door 26-9.9th partition door 26-9 passes through the 9th opening and closing hand Section 27-9 opens or closes the other side of the first decomposition chamber 11-8 and the side of the second decomposition chamber 11-9.

Between second decomposition chamber 11-9 and third decomposition chamber 11-10, it is configured with the tenth partition door 26-10.Tenth partition door 26-10 The other side of the second decomposition chamber 11-9 and the side of third decomposition chamber 11-10 are opened or closed by the tenth shutter means 27-10. Between third decomposition chamber 11-10 and the 4th decomposition chamber 11-11, it is configured with the 11st partition door 26-11.11st partition door 26-11 is logical Cross the 11st shutter means 27-11 open or close third decomposition chamber 11-10 the other side and the 4th decomposition chamber 11-11 one Side.Between 4th decomposition chamber 11-11 and the 5th decomposition chamber 11-12, it is configured with the 12nd partition door 26-12.12nd partition door 26-12 By the 12nd shutter means 27-12 open or close the 4th decomposition chamber 11-11 the other side and the 5th decomposition chamber 11-12 one Side.

Between 5th decomposition chamber 11-12 and the first cooling chamber 11-13, it is configured with the 13rd partition door 26-13.13rd partition door 26-13 opens or closes the other side and the first cooling chamber 11- of the 5th decomposition chamber 11-12 by the 13rd shutter means 27-13 13 side.Between first cooling chamber 11-13 and the second cooling chamber 11-14, it is configured with the 14th partition door 26-14.14th every Door 26-14 opens or closes the other side and the second cooling chamber of the first cooling chamber 11-13 by the 14th shutter means 27-14 The side of 11-14.Between second cooling chamber 11-14 and third cooling chamber 11-15, it is configured with the 15th partition door 26-15.15th Partition door 26-15 opens or closes the other side and the third cooling chamber of the second cooling chamber 11-14 by the 15th shutter means 27-15 The side of 11-15.

Between third cooling chamber 11-15 and the first postposition preparation room 11-16, it is configured with the 16th partition door 26-16.16th Partition door 26-16 closes the other side and the first postposition standard that means 27-16 opens or closes third cooling chamber 11-15 by sixteenmo The side of standby 11-16.Between first postposition preparation room 11-16 and the second postposition preparation room 11-17, it is configured with the 17th partition door 26-17.17th partition door 26-17 opens or closes the another of the first postposition preparation room 11-16 by the 17th shutter means 27-17 Side and the second postposition prepare the side of 11-17.

Second postposition preparation room 11-17 is configured with the 18th partition door 26-18 on the other side for removing container 2.18th Partition door 26-18 closes the removal mouth that means 27-18 opens or closes second other side postposition preparation room 11-17 by eighteenmo 29。

First to the 18th partition door 26-1~26-18 is accommodated in cabinet.

As shown in figure 3, at least decomposition chamber 11-8 to 11-12 (hereinafter, Fig. 3 is individually recorded as " room 11 ") is by insulating layer structure Body 30 is constituted.Insulating layer structure body 30 is made of glass wool material, since inside in sequence, two layers of hardboard 31- 1,31-2 and two soft fiberboard 32-1,32-2 and one layer of hardboard 31-3 and one layer of softboard 32-3 are built up 6 layers constitute multiple fiberboards.Insulating layer structure body 30 is the inner wall 30A and outside wall surface 30B for making room 11 by smearing mode It fixes and is hardened to formation, good in insulation effect, furthermore, it is possible to chronically, repeatedly use.If insulating layer structure Functional deterioration occurs for the inner wall 30A of body 30, it is only necessary to replace innermost hardboard 31-1, be readily inspected and tie up Shield, moreover, low in cost.

In addition, foring on the inner wall 30A of insulating layer structure body 30 in order to make the longitudinal wall face of up and down direction become recessed Convex surface and the multiple lug bosses 33 being arranged.In this way, in room 11, promote the stirring for decomposing gas (hot gas), prevent It only decomposes gas to be detained, waste is uniformly heated, the time of charcoal elementization processing can be shortened.And in process chamber 11 In be provided with and on top facilitate the stirring blade 34 of cracking gas agitating.Stirring blade 34 is driven by fan motor 35, The temperature difference in process chamber 11 is offset, can efficiently link with the lug boss 33 of inner wall 30A, stir cracked gas.Moreover, stirring It mixes with blade 34 other than it may be mounted at top, it can also be in more than two more suits of position installation such as other sides It sets.In addition, other process chambers such as vaporization chamber and cooling chamber other than decomposition chamber, can also be applied in insulating layer structure body 30.

As shown in Figure 3, Figure 4, it among room 11, is provided in order to which Shi Ge transport establishment 12-1~12-17 is (hereinafter, scheming 3, in Fig. 4, only it is recorded as " transport establishment 12 ") drive shaft 36 that works.An end inside room 11 is connected to fortune On transfer mechanism 12, on another end outside room 11, drive shaft 36 is connected with engine (motor) 37.Pass through fixation Among the shaft mounting hole 38 of stratiform heat insulating structure body 30, heat insulation support structural body 39 supports drive shaft 36.Heat insulation support knot Structure body 39 is made of the first cover board body 40 and the second cover board body 41 and inside occlusion plate 42 and outside occlusion plate 43.The One cover board body 40 is made of the ring bodies with specific thickness, on axis direction, form it is towards outer openings, First annulus 44, and be embedded into and be mounted among drive shaft 36.Second cover board body 41, be covered on the first cover board body 40, It forms the second annulus 45, and outer peripheral surface, is fixed on mounting hole 38.Inside occludes plate 42, is one and is located at layer On the inner wall 30A of the shape heat insulating structure body 30 and portion that is covered on the inner face of the first cover board body 40 and the second cover board body 41 Part.Outside occludes plate 43, is on the outside wall surface 30B for being located at stratiform heat insulating structure body 30 and to be covered on the first cover board body 40 And second cover board body 41 outer end face on component.The nitrogen from nitrogen supply arrangement 46 is filled by nitrogen supply pipe 47 Among the first annulus 44.In addition, being connected to the inlet tube 48 for exporting cooling water among the second annulus 45 With outlet 49, the cooling water from cooling water supply unit 50 is recycled.By using this method, drive can be improved The heat insulation of 36 installation position of moving axis, prevents the heat loss of room 11.

In addition, as shown in figure 4, among drive shaft 36, on axle center, according to from room 11 an end, to heat-insulated The length of 39 present position of supporting structure, forms cooling water axis hole 51, so as among cooling water axis hole 51, Recycle the cooling water from apparatus for supplying cool water 50.By using this method, on heat insulation support structural body 39, The heat insulation of 36 installation position of drive shaft can be further increased, heat release loss is eliminated, prevents the heat loss of room 11.In addition, It can also prevent from being thermally conducted to outside in room 11, so as to avoid the hidden danger that fire occurs.Additionally it is possible to prevent room 11 Interior decomposition gas leaks into outside.

As shown in figure 5, there is electronic control unit 52 in composition separate type charcoal element system 1.Electronic control unit 52, Control gas generating unit 16, deodorization smoke removing device 17-1,17-12, steam cooling device 20, liquid handling device 23-1~ 23-3.Electronic control unit 52 controls heating part 19-1~19-10 and cooling end 25-1~25-3.When this is the case, Electronic control unit 52, in order at least vaporization chamber 11-3,11-4 and removal room 11-5~11-7 and decomposition chamber 11-8~11- 12 temperature controls respectively at predetermined temperature (such as 10 DEG C), heating part 19-1~19-10 is driven to work.Electronic control dress 52 are set, after receiving the signal from sensor 18-1~18-13, drives heating part 19-1~19-10 and cooling end 25- 1~25-3 works.

Electronic control unit 52 after receiving the signal from limit switch 13-1~13-17, controls transport establishment Container 2 is moved to specified position by 12-1~12-17.Electronic control unit 52, control switch means 27-1~27-18, according to The defined time makes division plate door 26-1~26-18 carry out switch work.Electronic control unit 52, control fan motor 35 start Machine 37, nitrogen feedway 46 and apparatus for supplying cool water 50.

Separate type charcoal element system 1 is formed, is a kind of using heat source as electric power, in order to improve the efficiency of charcoal elementization processing, It is stringent to carry out temperature management, using low temperature (such as 450 DEG C), under anaerobic state, the processing of charcoal elementization is carried out to waste, to press down The equipment of the generations of harmful substances such as carbon dioxide packing and dioxin processed.

In addition, composition separate type charcoal element system 1, due to without the oxidizing fire (heat carried out by high-temperature oxydation It is decomposed into oxidation reaction, reduction reaction), therefore, it is a kind of equipment that will not generate coal ash.

Referring to attached drawing 6, the course of work of composition separate type charcoal element system 1 involved in this embodiment is said It is bright.In composition separate type charcoal element system 1, respectively according to regulation time (for example, every 40 minutes), all thrown primary The container 2 for entering waste is moved among each room 11-1~11-17.

It is container 2 by opening first partition door 26-1 that S101 container, which moves into, makes one of the first front preparation room 11-1 The mouth 28 of moving in of end face opens, to be moved to the inside towards the direction of the first front preparation room 11-1 from container entrance 3.

It is prepared as if the front S102 is standby through first conveyor structure 12-1, to move container 2, and it is moved to the If the specified position of one front preparation room 11-1, first partition door 26-1 be may turn off, to make at second partition door 26-2 In closed state, therefore the first front preparation room 11-1 becomes blocked state.In the first front preparation room 11-1, led from first Enter pipe 14-1 importing nitrogen and air is discharged from the first discharge pipe 15-1 at the same time.First front preparation room 11-1, is in Normal temperature state becomes nitrogen atmosphere environment.

After second partition door 26-2 is opened, become the first front preparation room 11-1 and the second front preparation room 11-2 When connected state (open state), by first conveyor structure 12-1 and second conveyor structure 12-2, from the first front preparation room 11-1, towards the second front preparation room 11-2, to move container 2.When container 2 reaches the predetermined bits of the second front preparation room 11-2 After setting, second partition door 26-2 be may turn off, to make third division plate door 26-3 become closed state, therefore the second front is quasi- Standby room 11-2 becomes blocked state.In the second front preparation room 11-2, nitrogen is imported from the second ingress pipe 14-2, it is same with this When, air is discharged from the second discharge pipe 15-2.First front preparation room 11-2 is in normal temperature state, becomes nitrogen atmosphere collarette Border.

The air being discharged from the first discharge pipe 15-1, the second discharge pipe 15-2, in the first deodorization smoke removing device 17-1 Deodorization, smoke abatement processing are obtained, is discharged among atmosphere after being cleaned.

In the standby preparation part 4 in front, have the first front preparation room 11-1 being connected to side by side and the second front quasi- Standby room 11-2 can prevent from countercurrently rushing in the inside foul smell come when each room opening being located behind or gas leaking into outside Portion.In addition, in order to carry out the composition separation of waste and the processing of charcoal elementization simultaneously, it can be strictly to composition separate type charcoal element The temperature of change system 1 is managed.Additionally it is possible to inhibit heat loss, contribute to save the energy.

S103 processing evaporation of water is to make the second front preparation room 11-2 and first after third division plate door 26-3 is opened When vaporization chamber 11-3 becomes connected state, by second conveyor structure 12-2 and third transport establishment 12-3, from the second front standard Standby room 11-2, towards the first vaporization chamber 11-3, to move container 2.When container 2 reach the first vaporization chamber 11-3 specified position it Afterwards, third division plate door 26-3 may turn off, so that the 4th division plate door 26-4 be made to become closed state, therefore the first vaporization chamber 11-3 Become blocked state.For the waste in the container 2 inside the first vaporization chamber 11-3, added using the first heating part 19-1 Heat.In the first vaporization chamber 11-3, nitrogen is imported from third ingress pipe 14-3 and is arranged from third discharge pipe 15-3 at the same time Vapor out becomes nitrogen atmosphere environment.

After the 4th division plate door 26-4 is opened, the first vaporization chamber 11-3 and the second vaporization chamber 11-4 is made to become connected state When, by third transport establishment 12-3 and the 4th transport establishment 12-4, from the first vaporization chamber 11-3, towards the second vaporization chamber 11- 4, to move container 2.After container 2 reaches the specified position of the second vaporization chamber 11-4, the 4th division plate door 26-4 be may turn off, To make the 5th division plate door 26-5 become closed state, therefore the second vaporization chamber 11-4 becomes blocked state.For the second evaporation The waste in container 2 inside the 11-4 of room, is heated using the second heating part 19-2.In the second vaporization chamber 11-4, from 4th ingress pipe 14-4 imports nitrogen and vapor is discharged from the 4th discharge pipe 15-4 at the same time, becomes nitrogen atmosphere collarette Border.

For the vapor being discharged from third discharge pipe 15-3, the 4th discharge pipe 15-4, using equipment for steam treatment 20 into After row processing, it is stored among cooling water tank 22.

In moisture evaporation section 5, if being unable to the moisture in ingredient removal waste in the first vaporization chamber 11-3 Words, can remove remaining moisture in the second vaporization chamber 11-4.Therefore, the moisture in waste can be expeditiously removed, Moisture is set to reach specified amount.

In addition, in moisture evaporation section 5, electronic control unit 52 individually and/or periodically controls first and adds Hot portion 19-1 and the second heating part 19-2, additionally it is possible to the temperature of the first vaporization chamber 11-3, be changed to and the second vaporization chamber 11-4 Different temperature.That is, according to the characteristic of waste, by the first vaporization chamber 11-3 and the second vaporization chamber 11-4 difference Become different temperature, so as to properly remove the moisture in waste.

The removal of S104 high-molecular compound is to make the second vaporization chamber 11-4 and first after the 5th division plate door 26-5 is opened When removal room 11-5 becomes connected state, by the 4th transport establishment 12-4 and the 5th transport establishment 12-5, from the second vaporization chamber 11-4, towards the first removal room 11-5, to move container 2.After container 2 reaches the specified position of the first removal room 11-5, 5th division plate door 26-5 may turn off, to make the 6th division plate door 26-6 become closed state, therefore the first removal room 11-5 becomes At blocked state.For the waste in the container 2 inside the first removal room 11-5, added using third heating part 19-3 Heat.In the first removal room 11-5, nitrogen is imported from the 5th ingress pipe 14-5 and is arranged from the 5th discharge pipe 15-5 at the same time The decomposition gas of high-molecular compound out, becomes nitrogen atmosphere environment.

After the 6th division plate door 26-6 is opened, so that the first removal room 11-5 and second is removed room 11-6 and become connected state When, by the 5th transport establishment 12-5 and the 6th transport establishment 12-6, from the first removal room 11-5, towards the second removal room 11- 6, to move container 2.After container 2 reaches the specified position of the second removal room 11-6, the 6th division plate door 26-6 be may turn off, To make the 7th division plate door 26-7 become closed state, therefore the second removal room 11-6 becomes blocked state.For the second removal The waste in container 2 inside the 11-6 of room, is heated using the 4th heating part 19-4.In the second removal room 11-6, from 6th ingress pipe 14-6 imports nitrogen, at the same time, the decomposition gas of high-molecular compound is discharged from the 6th discharge pipe 15-6, Become nitrogen atmosphere environment.

After the 7th division plate door 26-7 is opened, so that the second removal room 11-6 and third is removed room 11-7 and become connected state When, room 11- is removed towards third from the second removal room 11-6 by the 6th transport establishment 12-6 and the 7th transport establishment 12-7 7, to move container 2.After container 2 reaches the specified position of third removal room 11-7, the 7th division plate door 26-7 be may turn off, To make the 8th division plate door 26-8 become closed state, therefore third removal room 11-7 becomes blocked state.Third is removed The waste in container 2 inside the 11-7 of room, is heated using the 5th heating part 19-5.In third removal room 11-7, from 7th ingress pipe 14-7 imports nitrogen, at the same time, the decomposition gas of high-molecular compound is discharged from the 7th discharge pipe 15-7, Become nitrogen atmosphere environment.

The decomposition gas for the high-molecular compound that discharge pipe 14-5~14-7 is ejected from the 5th to the 7th, all first It obtains becoming liquefied substance after processing in liquefying device 23-1, be stored among the first liquefied substance recycling can 24-1.It is logical It crosses in this way, discharge exhaust gas can be made to reach zero.

It, can be efficient by removing room 10-5~10-7 with first to third in high-molecular compound purification device 6 High-molecular compound is removed to rate, so as to eliminate the source of generation of the harmful substances such as dioxin.

In addition, electronic control unit 52 can be individually and/or interim in high-molecular compound purification device 6 Ground controls third to the 5th heating part 19-3~19-5, additionally it is possible to the temperature of first~third removal room 11-5~11-7, become More different temperature.That is, according to the characteristic of waste, by the way that first~third is removed room 11-5~11-7 difference Become different temperature, so as to remove high-molecular compound conscientiously.

S105 composition separation resolution process is so that third is removed room 11-7 and first after the 8th division plate door 26-8 is opened When decomposition chamber 11-8 becomes connected state, by the 7th transport establishment 12-7 and the 8th transport establishment 12-8, room is removed from third 11-7, towards the first decomposition chamber 11-8, to move container 2.After container 2 reaches the specified position of the first decomposition chamber 11-8, 8th division plate door 26-8 may turn off, to make the 9th division plate door 26-9 become closed state, therefore the first decomposition chamber 11-8 becomes At blocked state.For the waste in the container 2 inside the first decomposition chamber 11-8, added using the 6th heating part 19-6 Heat.In the first decomposition chamber 11-8, nitrogen is imported from the 8th ingress pipe 14-8 and is arranged from the 8th discharge pipe 15-8 at the same time The decomposition gas of charcoal elementization processing out, becomes nitrogen atmosphere environment.

After the 9th division plate door 26-9 is opened, the first decomposition chamber 11-8 and the second decomposition chamber 11-9 is made to become connected state When, by the 8th transport establishment 12-8 and the 9th transport establishment 12-9, from the first decomposition chamber 11-8, towards the second decomposition chamber 11- 9, to move container 2.After container 2 reaches the specified position of the second decomposition chamber 11-9, the 9th division plate door 26-9 be may turn off, To make the tenth division plate door 26-10 become closed state, therefore the second decomposition chamber 11-9 becomes blocked state.It is decomposed for second The waste in container 2 inside the 11-9 of room, is heated using the 7th heating part 19-7.In the second decomposition chamber 11-9, from 9th ingress pipe 14-9 imports nitrogen, at the same time, the decomposition gas of charcoal elementization processing is discharged from the 9th discharge pipe 15-9, becomes At nitrogen atmosphere environment.

After the tenth division plate door 26-10 is opened, the second decomposition chamber 11-9 and third decomposition chamber 11-10 is made to become connected state When state, by the 9th transport establishment 12-9 and the tenth transport establishment 12-10, from the second decomposition chamber 11-9, towards third decomposition chamber 11-10, to move container 2.After container 2 reaches the specified position of third decomposition chamber 11-10, the tenth division plate door 26-10 is just It can close, to make the 11st division plate door 26-11 become closed state, therefore third decomposition chamber 11-10 becomes blocked state.It is right The waste in container 2 inside the third decomposition chamber 11-10, is heated using the 8th heating part 19-8.It is decomposed in third In the 11-10 of room, nitrogen is imported from the tenth ingress pipe 14-10, at the same time, is discharged from charcoal element from the tenth discharge pipe 15-10 The decomposition gas of reason, becomes nitrogen atmosphere environment.

After the 11st division plate door 26-11 is opened, third decomposition chamber 11-10 and the 4th decomposition chamber 11-11 is made to become to connect When logical state, by the tenth transport establishment 12-10 and the 11st transport establishment 12-11, from third decomposition chamber 11-10, towards the Four decomposition chamber 11-11, to move container 2.After container 2 reaches the specified position of the 4th decomposition chamber 11-11, the 11st partition Door 26-11 may turn off, to make the 12nd division plate door 26-12 become closed state, therefore the 4th decomposition chamber 11-11 becomes to close Plug-like state.For the waste in the container 2 inside the 4th decomposition chamber 11-11, heated using the 9th heating part 19-9.? In 4th decomposition chamber 11-11, nitrogen is imported from the 11st ingress pipe 14-11, at the same time, from the 11st discharge pipe 15-11 The decomposition gas of charcoal elementization processing is discharged, becomes nitrogen atmosphere environment.

After the 12nd division plate door 26-12 is opened, the 4th decomposition chamber 11-11 and the 5th decomposition chamber 11-12 is made to become to connect When logical state, by the 11st transport establishment 12-11 and the 12nd transport establishment 12-12, from the 4th decomposition chamber 11-11, towards 5th decomposition chamber 11-12, to move container 2.When container 2 reach the 5th decomposition chamber 11-12 specified position after, the 12nd every Plate door 26-12 may turn off, to make the 13rd division plate door 26-12 become closed state, therefore the 5th decomposition chamber 11-12 becomes Blocked state.For the waste in the container 2 inside the 5th decomposition chamber 11-12, added using the tenth heating part 19-10 Heat.In the 5th decomposition chamber 11-12, nitrogen is imported from the 12nd ingress pipe 14-12, at the same time, from the 12nd discharge pipe 15- The decomposition gas of charcoal elementization processing is discharged in 12, becomes nitrogen atmosphere environment.

The decomposition gas ejected from the 8th discharge pipe 15-12 of discharge pipe 15-8~the 12nd, all at the second liquefaction It obtains becoming liquefied substance after processing in reason device 23-2, be stored among the second liquefied substance recycling can 24-2.By using This method can make discharge exhaust gas reach zero.

It separates and is decomposed in part 7 in composition, by having first to the 5th decomposition chamber 11-8~11-12, can conscientiously may be used Waste being heated to specified temperature by ground, the composition that can expeditiously carry out waste organic matter decomposes and charcoal element, To generate charcoal element compound.

It is decomposed in part 7 in addition, being separated in composition, due to being under nitrogen atmosphere environment, so will not aoxidize Burning, so that the harmful substances such as carbon dioxide packing will not be generated.

It is decomposed in part 7 in addition, being separated in composition, electronic control unit 52 individually and/or can be controlled periodically Make the 6th~the tenth heating part 19-6~19-10, additionally it is possible to the temperature of first to the 5th decomposition chamber 11-8~11-12, change For different temperature.That is, waste can be promoted to form according to the characteristic of waste and the management temperature of salvage material Separation, can come easily among the muddy thing together of a variety of materials composition according to every kind of material, every kind of composition Recycle a variety of materials.

S106 charcoal element compound cooling treatment be when the 13rd division plate door 26-13 open after, make the 5th decomposition chamber 11-12 with When first cooling chamber 11-13 becomes connected state, by the 12nd transport establishment 12-12 and the 13rd transport establishment 12-13, from 5th decomposition chamber 11-12, towards the first cooling chamber 11-13, to move container 2.When container 2 reaches the first cooling chamber 11-13's After specified position, the 13rd division plate door 26-13 be may turn off, so that the 13rd division plate door 26-14 is made to become closed state, because This first cooling chamber 11-13 becomes blocked state.Among the first cooling chamber 11-13, using the first cooling end 25-11, to appearance Charcoal element compound in device 2 is cooled down.In the first cooling chamber 11-13, nitrogen is imported from the 13rd ingress pipe 14-13, with this Meanwhile internal decomposition gas being discharged from the 13rd discharge pipe 15-13, become nitrogen atmosphere environment.

After the 14th division plate door 26-14 is opened, the first cooling chamber 11-13 and the second cooling chamber 11-14 is made to become to connect When logical state, by the 13rd transport establishment 12-13 and the 14th transport establishment 12-14, from the first cooling chamber 11-13, towards Second cooling chamber 11-14, to move container 2.When container 2 reach the second cooling chamber 11-14 specified position after, the 14th every Plate door 26-14 may turn off, to make the 15th division plate door 26-15 become closed state, therefore the second cooling chamber 11-14 becomes Blocked state.Among the second cooling chamber 11-14, using the second cooling end 25-12, the charcoal element compound in container 2 is carried out cold But.In the second cooling chamber 11-14, nitrogen is imported from the 14th ingress pipe 14-14, at the same time, from the 14th discharge pipe 15- Internal decomposition gas is discharged in 14, becomes nitrogen atmosphere environment.

After the 15th division plate door 26-15 is opened, the second cooling chamber 11-14 and third cooling chamber 11-15 is made to become to connect When logical state, by the 14th transport establishment 12-14 and the 15th transport establishment 12-15, from the second cooling chamber 11-14, towards Third cooling chamber 11-15, to move container 2.When container 2 reach third cooling chamber 11-15 specified position after, the 15th every Plate door 26-15 may turn off, to make the 16th division plate door 26-16 become closed state, therefore third cooling chamber 11-15 becomes Blocked state.Among third cooling chamber 11-15, using third cooling end 25-13, the charcoal element compound in container 2 is carried out cold But.In third cooling chamber 11-15, nitrogen is imported from the 15th ingress pipe 13-15, at the same time, from the 15th discharge pipe 15- Internal decomposition gas is discharged in 15, becomes nitrogen atmosphere environment.From the 13rd discharge pipe 15- of discharge pipe 15-13~the 15th The 15 decomposition gases ejected, become liquefied substance after all being handled in third liquefying device 23-3, are stored Among third liquefied substance recycling can 24-3.By using this method, discharge exhaust gas can be made to reach zero.

It is able to carry out pressure regulation on charcoal element compound cooling device 8, to avoid occurring in the first cooling chamber 11-13 unexpected Volume expansion.In addition, finger can also be cooled to indirectly charcoal element compound by first to third cooling chamber 11-13~11-15 Fixed temperature (such as 50 DEG C or less), that is to say, that charcoal element compound can be cooled to the temperature that will not occur to burn and evaporate.

In addition, in charcoal element compound cooling device 8, electronic control unit 52 individually and/or can be controlled periodically Make first~third cooling end 25-1~25-3, additionally it is possible to the temperature of first~third cooling chamber 11-13~11-15, change For different temperature.That is, according to the material of charcoal element compound, by first to third cooling chamber 11-13~11-15's Temperature becomes different temperature, can properly cool down charcoal element compound.

The rear portion S107 is standby to be prepared as making third cooling chamber 11-15 and first after the 16th division plate door 26-16 is opened When rear portion preparation room 11-16 becomes connected state, by the 15th transport establishment 12-15 and the 16th transport establishment 12-16, from Third cooling chamber 11-15, towards the first rear portion preparation room 11-16, to move container 2.When container 2 reaches the first rear portion preparation room After the specified position of 11-16, the 16th division plate door 26-16 be may turn off, so that the 17th division plate door 26-17 be made to become to close State, therefore the first rear portion preparation room 11-16 becomes blocked state.Among the first rear portion preparation room 11-16, led from the 16th Enter pipe 14-16 and import nitrogen, at the same time, internal decomposition gas and air (oxygen is discharged from the 16th discharge pipe 15-16 Gas), become nitrogen atmosphere environment.

After the 17th division plate door 26-17 is opened, make the first rear portion preparation room 11-16 and the second rear portion preparation room 11- 17 when becoming connected state, by the 16th transport establishment 12-16 and the 17th transport establishment 12-17, prepares from the first rear portion Room 11-16, towards the second rear portion preparation room 11-17, to move container 2.When container 2 reaches the second rear portion preparation room 11-17's After specified position, the 17th division plate door 26-17 be may turn off, so that the 18th division plate door 26-18 is made to become closed state, because This second rear portion preparation room 11-17

Become blocked state.Among the second rear portion preparation room 11-17, nitrogen is imported from the 17th ingress pipe 14-17, with Internal decomposition gas and air are discharged from the 17th discharge pipe 15-17, becomes nitrogen atmosphere environment simultaneously for this.From the tenth The decomposition gas and air being discharged in six discharge pipe 15-16, the 17th discharge pipe 15-17, in the second deodorization smoke removing device 17-2 In obtain deodorization, smoke abatement processing, be cleaned after be discharged among atmosphere.

In the standby preparation device 9 in rear portion, by having the first rear portion preparation room 11-16 and the second rear portion preparation room 11- 17, it can prevent from countercurrently rushing in the inside foul smell come when each room for being located at front is open or gas leaking into outside.Separately Outside, strictly the temperature for forming separate type charcoal element system 1 can be managed, so as to inhibit heat loss, to save energy Source contributes.

S108 container removes that the second rear portion preparation room 11-17's is another to make after the 18th division plate door 26-18 opening A section move out mouth 29 it is open when, by the 17th transport establishment 12-17, from the second rear portion preparation room 11-17, being equipped with The container 2 of charcoal element compound is discharged to the outside, and then, moves out part 10 using container, and container 2 is moved out to come.For removing container Charcoal element compound in outlet 10, since the shapes and sizes of every kind of material are all different, using them as metal class or carbon material Ingredient etc. is recycled respectively.When this is the case, can be according to composition type, soil sand, iron, nonferrous metal, glass material Material or rare metal etc. become the state for being easy recycling.Moreover, these materials for being separately recovered, it can be respectively as work Industry charcoal element waste and retrieve utilization.

According to this as a result, in this embodiment, being able to suppress the harmful substances such as carbon dioxide packing or without residue (pulverizer powder Dirt) etc. output.In addition it is possible to control do not occur oxidizing fire (as caused by high-temperature oxydation thermal decomposition be oxidation reaction, Reduction reaction), the composition of waste can be separated well, improve the efficiency of charcoal elementization processing.In addition, need not also carry on a shoulder pole The heart can there is a situation where atmosphere pollution or water pollutions.

It is by multiple fiberboard 31-1~31-3,32- in addition, as shown in figure 3, at least decomposition chamber 11-8~11-12 What the stratiform heat insulating structure body 30 that 1~32-3 overlaps was formed.By using this method, improve decomposition chamber 11-8~ While the heat insulation of 11-12, when the function of the inner wall 30A of stratiform heat insulating structure body 30 generates deterioration, only need to change The hardboard 31-1 of memory can, can easily carry out maintenance inspection, and cheap, can be realized reduces cost Purpose.

In addition, as shown in figure 3, in the inside face 30A of stratiform heat insulating structure body 30, in order to make it become male and fomale(M&F), shape At multiple lug bosses 33.Therefore, the inner wall 30A for forming lug boss 33 is directly hit by decomposition gas, makes to decompose gas Nonlinearity flowing, it is complicated, make its promote gas stirring, prevent decompose gas be detained, and can to raw material into Row is evenly heated, so as to shorten the time of charcoal elementization processing.

In addition, as shown in figure 3, making stirring fan 34 by driving stirring fan 34, in formation lug boss 30 Wall surface 30A is worked together, and makes to decompose gas stochastic flow dynamic, and obtains efficient stirring, temperature difference in decontamination chamber, equably plus Hot waste.Additionally it is possible to shorten the time of charcoal elementization processing.

In addition, in charcoal element compound cooling device 8, due to that can be cooled to and not burn indirectly charcoal element compound Or the temperature of evaporation, so the temperature of charcoal element compound can be reduced properly, and the generation of harmful substance can also be inhibited.

Fig. 7 is shown as one embodiment provided by the invention；As shown in fig. 7, in composition separation decomposer 7, setting When container 2 reaches the 5th decomposition chamber 11-12, container 2 is made to return to first to fourth point of front by transport establishment 61 Solve any one decomposition chamber in the 11-8~11-11 of room.When this is the case, returning to transport establishment 61 can be roller conveyor It is constituted with equipment such as turning machines.

By using this method, waste in container 2, even if reaching the 5th decomposition chamber 11-12, but charcoal is plain It, can be container 2, as the room in front, back in first to fourth decomposition chamber 11-8~11-1 when change is still not enough Either one or two of it is indoor, then carry out charcoal element, the processing of charcoal elementization can be carried out solidly.

In addition, composition separation decomposer 7 is not limited solely to, even if in the standby preparation device 4 in front, moisture vaporising device 5, high-molecular compound purification device 6, in the standby preparation device 9 of charcoal element compound cooling device 8 and rear portion, by can also be with The upper surface of these parts are useful in, the structure of transport establishment 61 is returned using setting.

Fig. 8 is to indicate another embodiment of the present invention.As shown in figure 8, composition separate type charcoal element system 1, using It is capable of the structure of automatic moving.Separate type charcoal element system 1 is formed, with the standby preparation device in front, moisture vaporising device, high score Sub- compound purification device, ingredient separate decomposer, the standby preparation device of charcoal element compound cooling device and rear portion, by one Body formula is mounted among shell 62, can be moved to and be deposited by several wheels 63 of the transport establishment positioned at 62 bottom of shell At the position of waste G.On shell 62, there is the investment funnel part 64 of investment waste, take out taking for charcoal element compound Part 65 out.By the equipment such as heavy equipment 66, waste G is put among waste investment funnel part 64.By adopting In this way, composition separate type charcoal element system 1 can be moved to there are the workshop of waste G, can be carried out in workshop The processing of charcoal elementization therefore, there is no need to be transported to waste G inside other buildings etc., so as to easily use very much Form separate type charcoal element system 1.Composition separate type charcoal element system according to the present invention, can be adapted for various processing systems System.

For device disclosed by the embodiments of the present invention, since it is corresponded to the methods disclosed in the examples, so retouching That states is fairly simple, and reference may be made to the description of the method.The foregoing description of the disclosed embodiments makes this field Professional technician can be realized or using the present invention.Various modifications to these embodiments are to those skilled in the art For will be apparent, the general principles defined herein can be the case where not departing from the spirit or scope of the present invention Under, it realizes in other embodiments.Therefore, the present invention will not be limited to the embodiments shown herein, but to accord with Close the widest scope consistent with the principles and novel features disclosed herein.

Claims

1. ingredient separate type charcoal element system, the charcoal elementization for waste is handled；It is characterized in that, loading the waste Container (2) passes sequentially through with oxygen-free environment through container entrance (3), can convert the evaporation of connection and remove in the waste The moisture vaporising device (5) of moisture, the high-molecular compound for removing high-molecular compound in the waste by thermal decomposition are net Makeup is set (6), ingredient separation decomposer (7) of organic substance in the separation waste, is separated in the cooling waste The charcoal element compound cooling device (8) of the charcoal element compound of decomposition, and the container (2) is exported through container outlet (10)；

Wherein, include multiple process chambers inside each device, each inner treatment chamber all has:

For moving the transport establishment of the container (2)；

For filling the ingress pipe of inert gas；

With the discharge pipe for gas in chambers to be discharged；The post-treated recycling of the gas being discharged in the chambers is sharp again With.

2. ingredient separate type charcoal element system according to claim 1, which is characterized in that further include the standby preparation dress in front Set the standby preparation device in (4) and rear portion (9)；

The standby preparation device in front (4), and can between the container entrance (3) and the moisture vaporising device (5) Conversion is connected to the container entrance (3) and the moisture vaporising device (5)；It is outer for preventing internal foul smell or gas from leaking into The standby preparation part in the front in portion；

The standby preparation device in rear portion (9) is between the charcoal element compound cooling device (8) and the container outlet (10)； And can convert and be connected to the charcoal element compound cooling device (8) and the container outlet (10), for preventing internal foul smell or gas Body leaks into the external standby preparation part in rear portion.

3. ingredient separate type charcoal element system according to claim 2, which is characterized in that further include multiple division plate doors；Institute It states multiple division plate doors and can convert and be connected to the standby preparation device in the front (4), the moisture vaporising device (5), the high score Sub- compound purification device (6), ingredient separation decomposer (7), the charcoal element compound cooling device (8) and the rear portion Between multiple process chambers of standby preparation device (9).

4. ingredient separate type charcoal element system according to claim 2, which is characterized in that the ingress pipe is sent out with gas Generating apparatus (16) connection is for injecting inert gas inside chambers；It is discharged in chambers by the exhaust pipe simultaneously The gas in portion；

Wherein the process chamber of the standby preparation device of the standby preparation device in the front (4) and the rear portion (9) passes through the exhaust The gas of pipe discharge enters deodorization, smoke removing device；

The gas of moisture vaporising device (5) the process chamber discharge flows into cooling trough after evaporation-cooled device (20) condensation；

The high-molecular compound purification device (6), ingredient separation decomposer (7) and the charcoal element compound cooling device (8) gas of each process chamber discharge enters liquefied substance accumulator tank after liquefying device.

5. ingredient separate type charcoal element system according to claim 2, which is characterized in that the moisture vaporising device (5), The high-molecular compound purification device (6), ingredient separation decomposer (7) and the charcoal element compound cooling device (8) Process chamber in include that temperature sensor is used to detect temperature inside chambers；

The moisture vaporising device (5), the high-molecular compound purification device (6) separate decomposer (7) with the ingredient Inner treatment chamber all have heating part；

The inner treatment chamber of the charcoal element compound cooling device (8) all has cooling end.

6. according to the described in any item ingredient separate type charcoal element systems of claim 2-5, which is characterized in that further include electronics control Device (52) processed；The electronic control unit (52) communicates to connect the standby preparation device in front (4), moisture evaporation dress Set (5), the high-molecular compound purification device (6), ingredient separation decomposer (7), the cooling dress of the charcoal element compound Set the standby preparation device in (8) and the rear portion (9).

7. ingredient separate type charcoal element system according to claim 1-5, which is characterized in that each process chamber The transport establishment include transport base, power part (37), drive shaft (36), heat insulation support structural body (39)；

The transport base is for moving the container (2)；The transport base connects described drive shaft (36) one end；It is described every A shaft mounting hole (38) is offered on the side wall of one process chamber；The heat insulation support structural body (39) is supported in the axis In mounting hole (38), drive shaft (36) other end is extend out to described in the middle part of the heat insulation support structural body (39) The power part (37) is connected on the outside of process chamber.

8. ingredient separate type charcoal element system according to claim 7, which is characterized in that the heat insulation support structural body It (39) include the first cover board body (40), the second cover board body (41), inner closure plate (42) and external occlusion plate (43)；

The first cover board body (40) is installed on the drive shaft (36)；The first cover board body (40) is to outside the process chamber There is opening on wall direction, formed the first annulus (44)；The second cover board body (41) is covered in the first cover board body (40) it on, is formed the second annulus (45)；The inner closure plate (42) is installed on the shaft mounting hole (38) corresponding position Process chamber inner wall at, external occlusion plate (43) is installed on the process chamber of the shaft mounting hole (38) corresponding position At outside wall surface.

9. ingredient separate type charcoal element system according to claim 8, which is characterized in that the ingredient separates decomposer (7) process chamber is stratiform heat insulating structure body (30), has multiple lug bosses on layered heat insulating structure body (30) inner wall (33), change the flow direction of the gas of separation；Also there is fan at the top of the process chamber of ingredient separation decomposer (7), For stirring the isolated gas.

10. according to the described in any item ingredient separate type charcoal element systems of claim 2-5, which is characterized in that the container enters Mouth (3), the standby preparation device in the front (4), the moisture vaporising device (5), the high-molecular compound purification device (6), ingredient separation decomposer (7), the charcoal element compound cooling device (8), the standby preparation device in the rear portion (9) and The container outlet (10), which is structure as a whole, to be installed in shell (62)；Shell (62) bottom is equipped with walking arrangement；It is described There are funnel part (64) at the top of shell (62)；The waste is put into through heavy equipment (66) to the funnel part (64) In, it is taken out after charcoal element through taking-up portion (65).