CN205628892U - Continuous anaerobic carbonization organic waste's of superheated steam device - Google Patents
Continuous anaerobic carbonization organic waste's of superheated steam device Download PDFInfo
- Publication number
- CN205628892U CN205628892U CN201620450475.5U CN201620450475U CN205628892U CN 205628892 U CN205628892 U CN 205628892U CN 201620450475 U CN201620450475 U CN 201620450475U CN 205628892 U CN205628892 U CN 205628892U
- Authority
- CN
- China
- Prior art keywords
- superheated steam
- organic waste
- data acquisition
- carbonization
- unit
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 238000003763 carbonization Methods 0.000 title claims abstract description 71
- 239000010815 organic waste Substances 0.000 title claims abstract description 51
- 238000004891 communication Methods 0.000 claims abstract description 21
- 239000002699 waste material Substances 0.000 claims abstract description 21
- 238000004332 deodorization Methods 0.000 claims abstract description 19
- 238000000034 method Methods 0.000 claims abstract description 15
- 238000010438 heat treatment Methods 0.000 claims abstract description 11
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 62
- 239000000428 dust Substances 0.000 claims description 31
- 239000003345 natural gas Substances 0.000 claims description 31
- 239000007789 gas Substances 0.000 claims description 25
- 229920006395 saturated elastomer Polymers 0.000 claims description 24
- 238000002485 combustion reaction Methods 0.000 claims description 18
- 238000007599 discharging Methods 0.000 claims description 18
- 238000012545 processing Methods 0.000 claims description 15
- 238000010792 warming Methods 0.000 claims description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 10
- 239000002912 waste gas Substances 0.000 claims description 10
- 239000000523 sample Substances 0.000 claims description 5
- 238000001179 sorption measurement Methods 0.000 claims description 4
- 238000005201 scrubbing Methods 0.000 claims description 3
- 238000005516 engineering process Methods 0.000 abstract description 12
- 108091023288 HOTAIR Proteins 0.000 abstract 1
- GBIHOLCMZGAKNG-UHFFFAOYSA-N flucythrinate Chemical group C=1C=C(OC(F)F)C=CC=1C(C(C)C)C(=O)OC(C#N)C(C=1)=CC=CC=1OC1=CC=CC=C1 GBIHOLCMZGAKNG-UHFFFAOYSA-N 0.000 abstract 1
- 239000003921 oil Substances 0.000 description 16
- 230000000694 effects Effects 0.000 description 7
- 239000000463 material Substances 0.000 description 5
- 230000008901 benefit Effects 0.000 description 4
- 238000001514 detection method Methods 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000013461 design Methods 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 239000002028 Biomass Substances 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000010000 carbonizing Methods 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 238000006477 desulfuration reaction Methods 0.000 description 2
- 230000023556 desulfurization Effects 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 238000010025 steaming Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- OBOXTJCIIVUZEN-UHFFFAOYSA-N [C].[O] Chemical compound [C].[O] OBOXTJCIIVUZEN-UHFFFAOYSA-N 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 239000010903 husk Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 231100000004 severe toxicity Toxicity 0.000 description 1
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 description 1
- 229910010271 silicon carbide Inorganic materials 0.000 description 1
- 125000006850 spacer group Chemical group 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
The utility model belongs to the technical field of organic waste treatment facility technique and specifically relates to a continuous anaerobic carbonization organic waste's of superheated steam device is related to. The device includes control system and the pay -off unit, carbonization unit, ejection of compact unit, a cyclone, the 2nd cyclone, deodorization stove, superheated steam generator, the 3rd cyclone, conduction oil heating apparatus, waste discharge fan and the tail gas terminal handling system that are connected with the control system communication respectively. The device can replenish present incineration technology and deal with a lot of not enough in the dangerous organic waste technique, and it is single still can to solve present carbonization technique simultaneously, the outer hot type that only can be simple to use or the current situation of interior hot type hot -air carbonization technique.
Description
Technical field
This utility model relates to organic waste processing arrangements technical field, especially relates to one
The device of superheated steam continuous anaerobic carbonization organic waste.
Background technology
At present, China's carbonization technical merit is the most single, is used for the carbonization of biomass, such as wood
The organic carbonizations such as material, straw, rice husk, coal.The carbonization effect requirements of carbide is the highest.
Along with the fast development of the industries such as China Chemical Industry, pesticide, medicine, the substantial amounts of danger of annual generation
Organic waste, a lot of garbages no doubt can destroy the pollution of difficult degradation by simple burning
Thing, but substantial amounts of severe toxicity gas two English and residue, flying dust the like waste can be produced simultaneously.
The whole world produces organic waste more than 1,000,000,000 tons every year, China's dangerous waste in 2015
The raw amount of produce surpasses 60,000,000 tons, ends the whole nation in 2011 and holds danger wastes business licence
Unit about 1500, danger wastes year disposal amount also can only be located more than more than 9,000,000 tons
Putting ability and disposal technology can not meet far away present situation, incineration technology can not be disposed completely simultaneously
All of danger wastes.The such as burning of high salt organic waste, can shorten making of incinerator
Use the life-span.Therefore, the disposal industry of organic waste is badly in need of introducing more new technique.
At present, there is many defects when datatron garbage in existing carbonization technology, existing
Objective shortcoming is introduced referring to following:
One, the mode of existing carbonized by means of superheated steam stove
Saturated vapor is sequentially entered thermophore, vapour liquid separator, superheater, steam turbine generator
The structure such as group and oxygen-eliminating device forms, and its process complexity is loaded down with trivial details, and superheated steam heats up slow, efficiency
Low, it is difficult to apply to industrialized production, and disposes organic waste.
Two, external-heat continuous carbonization organic waste device
Utilize the mode external heat carbide furnace such as electrical heating firing biomass fuel or heating hot media,
These devices have common shortcoming: energy consumption is high；Heat transfer is slow；Carbonization is uneven；Utilize heating agent
Body there is also the problem such as sealing and hot media leakage in the heating of spacer cavity.
Three, the batch carbonizing plant of external-heat (or interior heating)
The shortcoming of this device is: the most fixing treating capacity is the least；Time is long；Treatment effeciency is very
Low；The waste gas majority that the carbonizing plant of batch produces directly discharges air, pollutes environment, or
Doing simple emission-control equipment, effect is general.
Four, internal heat type continuous carbonization device
Utilization adds hot-air: hot-air rich in oxygen,
Therefore organic waste can not be made to accomplish anaerobic carbonization truly.Rich in oxygen in hot-air
Gas, contact organic waste easily burns, and a lot of melting point of organic matter are the lowest, therefore certain Organic substance
Once melt, the conveyer device of carbonization body of heater and inside thereof will be damaged.
Utility model content
The purpose of this utility model is to provide superheated steam continuous anaerobic carbonization organic waste
Device, to solve that carbonization technology present in prior art is single, carbonization weak effect and setting
The technical problem that standby reliability is the highest.
For solving above-mentioned technical problem, this utility model provides a kind of continuous non-oxygen carbon of superheated steam
Changing the device of organic waste, it includes control system and is connected with control system communication respectively
Feeding unit, carbonation unit, discharging unit, the first cyclone dust extractor, the second cyclone dust removal
Device, deodorization stove, superheated steam generator, the 3rd cyclone dust extractor, conduction-oil warming device,
Waste discharge blower fan and tail gas terminal processing system；Described feeding unit and carbonation unit, discharging unit
It is sequentially connected with；Described carbonation unit is provided with superheated steam entrance point and waste gas outlet end, described mistake
Vapours entrance point is connected with the heat exchange section in described superheated steam generator, described waste gas
The port of export connects successively with described first cyclone dust extractor, the second cyclone dust extractor and deodorization stove
Connect, and described deodorization stove and the furnace chamber part of superheated steam generator, the 3rd cyclone dust extractor,
Conduction-oil warming device, waste discharge blower fan and tail gas terminal processing system are sequentially connected with.
Further, in described carbonation unit, it is provided with carbonization cavity, in carbonization cavity, is provided with carbon
Change feeding screw and superheated steam send vapour device；It is described that described superheated steam send vapour device to be positioned at
The superheated steam entrance point of carbonation unit, and with the heat exchange section of superheated steam generator even
Connect；Pressure measuring unit, described pressure measuring unit, carbonization it is additionally provided with on described carbonation unit
Feeding screw is connected with described control system communication respectively.
Further, described superheated steam generator includes superheated steam combustion furnace, was arranged at
The first heat exchanger in vapours combustion furnace and be arranged at one end, superheated steam combustion furnace
First burner；The port of export of described first heat exchanger and described superheated steam send vapour device to lead to
Piping connect, and be respectively equipped with on pipeline between the first temperature data acquisition mouth,
Second temperature data acquisition mouth；Described first temperature data acquisition mouth and the second temperature data acquisition
Mouth is connected with control system communication respectively；The inlet end of described first burner connects first day
So feed channel, the first air line, described first natural gas line be provided with the first Pressure gauge and
First natural gas intake valve, described first air line is provided with the second Pressure gauge, the first air
Intake valve and the first blower fan；Described superheated steam combustion furnace is provided with the first furnace temperature data acquisition
Mouthful, described first furnace temperature data acquisition mouth is connected with control system communication.
Further, the arrival end of described first heat exchanger connects saturated steam generator；
Passage between the arrival end of described saturated steam generator and the first heat exchanger is provided with
Six Pressure gauges, described saturated steam generator connect and have relief valve, inlet channel and outlet pipe
Road, described inlet channel is provided with water intaking valve and water meter, and described outlet conduit is provided with outlet valve；
One end of described saturated steam generator is provided with the second burner, entering of described second burner
Gas end connects has the second natural gas line, the second air line, on described second natural gas line
Being provided with the 3rd Pressure gauge and the second natural gas intake valve, described second air line is provided with second
Blower fan and the second air valve.
Further, one end of described deodorization stove is provided with the 3rd burner, described 3rd burning
The inlet end of device connects the 3rd natural gas line, the 3rd air line, described 3rd natural gas
Pipeline is provided with the 4th Pressure gauge and the 3rd natural gas intake valve, and described 3rd air line sets
There are the 5th Pressure gauge, the 3rd air inlet valve and the 3rd blower fan；Described deodorization stove is provided with second
Furnace temperature data acquisition mouth, described second furnace temperature data acquisition mouth is with described control system communication even
Connect.
Further, described conduction-oil warming device connects temperature probe, inlet valve and oil extraction
Valve, and in conduction-oil warming device, it is provided with the second heat exchanger, described second heat exchanger
Entrance point and the 3rd cyclone dust extractor connect, the port of export of described second heat exchanger and waste discharge wind
Machine connects.
Further, on the pipeline between described waste discharge blower fan and the port of export of the second heat exchanger
It is provided with the 3rd temperature data acquisition mouth, described 3rd temperature data acquisition mouth and control system communication
Connect.
Further, it is provided with activated carbon adsorption unit, desulfurization in described tail gas terminal processing system
Any one or a few combination in device and denitrification apparatus.
Further, described tail gas terminal processing system includes the cooling tower being connected with waste discharge blower fan
And scrubbing tower.
Further, described feeding unit includes the spiral feeding being arranged at carbonation unit one end
Machine, the arrival end of described spiral feeder is provided with automatic discharging device；Described feeding unit bag
Include the Water-cooled screw collecting machine being arranged at the carbonation unit other end, described Water-cooled screw rewinding
Machine connects rewinding case, and the pipeline between described Water-cooled screw collecting machine and carbonation unit sets
Having the 4th temperature data acquisition mouth, described 4th temperature data acquisition mouth is with control system communication even
Connect.
Using technique scheme, this utility model has the advantages that this utility model
The device of superheated steam continuous anaerobic carbonization organic waste can supplement incineration technology and dispose very
The deficiency of many dangerous organic waste technology, solves current carbonization technology single simultaneously, is only capable of
Use simple external-heat or the present situation of internal heat type hot-air carbonization technology.This device can be continuous
Dispose organic waste in a large number, especially for the dangerous organic waste technology such as high salt, high COD
Advantage becomes apparent from, and also has the highest resource recycling through the organic waste of this device carbonization
Value.This device uses anaerobic carbonization technology truly, therefore does not produces in disposal process
The dangerous combustion such as raw two English.This device belongs to high-temperature pressure equipment, does not use state's laws to limit
The high-pressure bottle of system, equipment is safe and reliable, simple to operate, and floor space is little, it is easy to promote.
Accompanying drawing explanation
In order to be illustrated more clearly that this utility model detailed description of the invention or skill of the prior art
Art scheme is below by the accompanying drawing used required in detailed description of the invention or description of the prior art
It is briefly described, it should be apparent that, the accompanying drawing in describing below is more of the present utility model
Embodiment, for those of ordinary skill in the art, before not paying creative work
Put, it is also possible to obtain other accompanying drawing according to these accompanying drawings.
The superheated steam continuous anaerobic carbonization organic waste that Fig. 1 provides for this utility model embodiment
The structural representation of device.
Reference:
1-feeding unit；2-carbonation unit；3-discharging unit；4-saturated steam generator；5-is overheated
Steam generator；6-the first cyclone dust extractor；7-the second cyclone dust extractor；8-deodorization stove；9-
Superheated steam combustion furnace；10-the 3rd cyclone dust extractor；11-conduction-oil warming device；12-arranges
Useless blower fan；13-tail gas terminal processing system；14-total system electric control unit；15-heat system
Detection, collection and the control unit of system；16-carbonization feeding screw；17-superheated steam send vapour
Device；18-pressure measuring unit；19-the 4th temperature data acquisition mouth；20-water intaking valve；21-
Outlet valve；22-the second burner；23-relief valve；24-the first heat exchanger；25-the first stove
Temperature data acquisition mouth；26-the first burner；27-the first natural gas intake valve；28-first is empty
Gas intake valve；29-butterfly valve；30-butterfly valve；31-the 3rd burner；32-the 3rd natural gas air inlet
Valve；33-the 3rd air inlet valve；34-the second furnace temperature data acquisition mouth；35-butterfly valve；36-
Temperature probe；37-inlet valve；38-draining valve；39-the 3rd temperature data acquisition mouth；40-
First temperature data acquisition mouth；41-the second temperature data acquisition mouth；42-automatic discharging device；
43-rewinding case；44-the first Pressure gauge；45-the 4th Pressure gauge；46-the 5th Pressure gauge；47-
Second Pressure gauge；48-water meter；49-the second heat exchanger；50-the second natural gas intake valve；
51-the 3rd Pressure gauge；52-the second blower fan；53-the 6th Pressure gauge；54-controls valve；55-
First blower fan；56-the 3rd blower fan.
Detailed description of the invention
Below in conjunction with accompanying drawing, the technical solution of the utility model is clearly and completely retouched
State, it is clear that described embodiment is a part of embodiment of this utility model rather than all
Embodiment.Based on the embodiment in this utility model, those of ordinary skill in the art are not having
Make the every other embodiment obtained under creative work premise, broadly fall into this utility model
The scope of protection.
In description of the present utility model, it should be noted that term " " center ", " on ",
D score, "left", "right", " vertically ", " level ", " interior ", " outward " etc. instruction orientation or
Position relationship is based on orientation shown in the drawings or position relationship, is for only for ease of this reality of description
Describe with novel and simplification rather than indicate or imply that the device of indication or element must have spy
Fixed orientation, with specific azimuth configuration and operation, therefore it is not intended that to this utility model
Restriction.Additionally, term " first ", " second ", " the 3rd " are only used for describing purpose, and
It is not intended that instruction or hint relative importance.
In description of the present utility model, it should be noted that unless otherwise clear and definite regulation and
Limiting, term " is installed ", " being connected ", " connection " should be interpreted broadly, for example, it may be
Fixing connection, it is also possible to be to removably connect, or be integrally connected；Can be to be mechanically connected,
It can also be electrical connection；Can be to be joined directly together, it is also possible to be indirectly connected to by intermediary,
It can be the connection of two element internals.For the ordinary skill in the art, permissible
Concrete condition understands above-mentioned term concrete meaning in this utility model.
As it is shown in figure 1, the superheated steam continuous anaerobic carbonization organic waste that the present embodiment provides
Device, it includes control system and the feeding unit being connected respectively with control system communication
1, carbonation unit 2, discharging unit the 3, first cyclone dust extractor the 6, second cyclone dust extractor 7,
Deodorization stove 8, superheated steam generator the 5, the 3rd cyclone dust extractor 10, conduction-oil warming device
11, waste discharge blower fan 12 and tail gas terminal processing system 13；Feeding unit 1 and carbonation unit 2,
Discharging unit 3 is sequentially connected with；Carbonation unit 2 is provided with superheated steam entrance point and waste gas outlet end,
Superheated steam entrance point is connected with the heat exchange section in superheated steam generator 5, waste gas outlet
End is sequentially connected with first cyclone dust extractor the 6, second cyclone dust extractor 7 and deodorization stove 8；
Wherein, deodorization stove 8 and the furnace chamber part of superheated steam generator 5, the 3rd cyclone dust extractor
10, conduction-oil warming device 11, waste discharge blower fan 12 and tail gas terminal processing system 13 are successively
Connect.
The device carbonization of the superheated steam continuous anaerobic carbonization organic waste that the present embodiment provides
Effective, carbonization is uniform, and carbonization efficiency is high；And this device does not produce two English, flying dust etc.
Toxic and harmful；The said equipment is also high-temperature pressure equipment simultaneously, it is impossible to the high pressure that rule limits
Equipment, simple to operate, safe and reliable, floor space is little, it is easy to promote.
What deserves to be explained is, for control system, its concrete form does not limit to, it is possible to
Complete above-mentioned all parts Automated condtrol.Illustrate: control system can be divided into entirely
System electrical control unit 14 and the detection of hot systems, collection and control unit 15；Certainly,
For meeting user's requirement, person-computer union of also can arranging in pairs or groups, reach the purpose of easy manipulation.
Repeat the most one by one.
The structure composition of all parts in order to be more clearly understood from this enforcement is former with work
Reason, can be found in the narration of following preferred embodiment.
The feeding unit 1 of the present embodiment includes the spiral feeding being arranged at carbonation unit 2 one end
Machine, the arrival end of spiral feeder is provided with automatic discharging device 42；Specifically, spirally
Feeder is preferably the automatic discharging device 42 of cage feeder and band blender, automatic discharging
The lower end of device 42 is provided with control valve 54.It is shown that horizontal feeding in the present embodiment,
Certainly may be designed as tilted spiral feeding, or two groups or three groups feed screws of staggered form,
May be designed as vertical bucket elevator and add star-shaped dust-discharging valve, concrete main according to user place
Situation and day output size and determine machine height, thus final design feed mechanism.
The feeding unit 1 of the present embodiment includes the water-cooled spiral shell being arranged at carbonation unit 2 other end
Rotation collecting machine, Water-cooled screw collecting machine connects rewinding case 43, Water-cooled screw collecting machine
And the pipeline between carbonation unit 2 is provided with the 4th temperature data acquisition mouth 19, the 4th temperature
Data acquisition mouth 19 is connected with control system communication, and it act as detecting temperature and feeding back
Decision-making is carried out to control system.Wherein it is preferred to, feeding unit 1 is the water-cooled of jacketed
Spiral collecting machine.Further, carbonation unit 2 i.e. carbonization cavity can be according to carbonization garbage
Difficulty and treating capacity be designed to multiple (1,2,3 etc.), neighbouring cavity is first
Tail discharging opening and charging aperture vertical out-fall.
The carbonation unit 2 of the present embodiment is provided with the carbonization cavity of high temperature therein, in this carbonization
It is provided with carbonization feeding screw 16 in cavity and superheated steam send vapour device 17；Accordingly, mistake
Vapours send the superheated steam entrance point that vapour device 17 is positioned at carbonation unit 2, and with overheated steaming
The heat exchange section of vapour generator 5 connects；Survey additionally, be additionally provided with pressure on carbonation unit 2
Determining device 18, pressure measuring unit 18, carbonization feeding screw 16 lead to control system respectively
News connect, thus realize automatically controlling the high temperature cabonization of organic waste.Further, carbonization
The quantity of feeding screw 16 can be designed to 1 according to the difficulty of carbonization garbage and treating capacity
To 4.
The superheated steam generator 5 of the present embodiment includes superheated steam combustion furnace 9, was arranged at
The first heat exchanger 24 in vapours combustion furnace 9 and be arranged at superheated steam combustion furnace 9
First burner 26 of one end；The port of export of the first heat exchanger 24 and superheated steam send vapour to fill
Put 17 to be connected by pipeline, and on pipeline between, be respectively equipped with the first temperature data
Acquisition port the 40, second temperature data acquisition mouth 41；First temperature data acquisition mouth 40 and second
Temperature data acquisition mouth 41 is connected with control system communication respectively, and it act as detecting temperature
Degree information also feeds back to carry out in control system decision-making.
Specifically, the first burner 26 inlet end connect have the first natural gas line, first
Air line, the first natural gas line is provided with the first Pressure gauge 44 and the first natural gas air inlet
Valve 27, the first air line is provided with second Pressure gauge the 47, first air inlet valve 28 and
One blower fan 55；The igniting direction of the first burner 26 is towards the first heat exchanger 24, by control
Make each valve above-mentioned, Pressure gauge and blower fan and realize the control to temperature.
Additionally, be provided with the first furnace temperature data acquisition mouth 25 on superheated steam combustion furnace 9, the
One furnace temperature data acquisition mouth 25 is connected with control system communication, and its effect is similarly for detecting
Temperature information also feeds back to carry out in control system decision-making.
In the present embodiment, if there being saturated vapor source, it is overheated to be directly communicates with in saturated vapor source
Steam generator 5, thus without additionally arranging saturated steam generator 4.Otherwise, also need
To connect at the arrival end of the first heat exchanger 24 and to have saturated steam generator 4.
Specifically, between saturated steam generator 4 and the arrival end of the first heat exchanger 24
Passage is provided with the 6th Pressure gauge 53, and is also associated with peace on saturated steam generator 4
Full valve 23, inlet channel and outlet conduit, inlet channel is provided with water intaking valve 20 and water meter 48,
Outlet conduit is provided with outlet valve 21；Additionally, one end of saturated steam generator 4 is provided with
Second burner 22, the inlet end of the second burner 22 connect have the second natural gas line, the
Two air lines, the second natural gas line is provided with the 3rd Pressure gauge 51 and the second natural gas enters
Air valve 50, the second air line is provided with the second blower fan 52.By controlling each valve, pressure
Power table and blower fan realize regulation ignition process.
Wherein, saturated vapor refers at one atm, and temperature is the steam of 100 DEG C.Full
Can improve temperature by improving pressure with water vapour, pressure reaches 22Mpa, and critical temperature is
373 DEG C, after exceeding this temperature, improve pressure in time and also cannot generate higher temperature.
Accordingly, superheated steam can reach the high temperature of more than 1000 DEG C under normal pressure.
Superheated steam and the evaporation rate comparative experiments result adding hot-air, the overheated steaming of more than 160 DEG C
Steam raising speed is faster than high temperature air.From social benefit, economic benefit, superheated steam has
Machine thing can reach more preferable effect.
First cyclone dust extractor the 6, second cyclone dust extractor 7 and the 3rd whirlwind of the present embodiment
Cleaner unit 10 correspondence can include butterfly valve 29, butterfly valve 30 and butterfly valve 35 respectively, above-mentioned these
Butterfly valve may be designed to star-shaped dust-discharging valve, may be designed to manually or automatically control, it is possible to be designed to two
Individual linkage, does not the most limit to.
The present embodiment is provided with the 3rd burner 31, the 3rd burner in one end of deodorization stove 8
The inlet end of 31 connects the 3rd natural gas line, the 3rd air line, the 3rd natural gas tube
Road is provided with the 4th Pressure gauge 45 and the 3rd natural gas intake valve 32, and the 3rd air line sets
There is the 5th Pressure gauge the 46, the 3rd air inlet valve 33 and the 3rd blower fan 56；Additionally, in deodorize
Stove 8 is provided with the second furnace temperature data acquisition mouth 34, the second furnace temperature data acquisition mouth 34 and control
System communication connects.
In the present embodiment, conduction-oil warming device 11 connects temperature probe 36, inlet valve 37
With draining valve 38, and in conduction-oil warming device 11, it is provided with the second heat exchanger 49, second
Entrance point and the 3rd cyclone dust extractor 10 of heat exchanger 49 connect, the second heat exchanger 49
The port of export be connected with waste discharge blower fan 12.Second heat exchanger 49 is preferably in roundabout bending
Shape.Further, above conduction-oil warming device, simply a kind of method of UTILIZATION OF VESIDUAL HEAT IN and dress
Put, it is possible to access the device that other waste heat uses.
Pipeline between waste discharge blower fan 12 and the port of export of the second heat exchanger 49 in the present embodiment
It is provided with the 3rd temperature data acquisition mouth 39, the 3rd temperature data acquisition mouth 39 and control system
Communication connects.
It is provided with activated carbon adsorption unit, desulfurization in the tail gas terminal processing system 13 of the present embodiment
Any one or a few combination in device and denitrification apparatus.Wherein, activated carbon adsorption unit master
If the difference according to handled organic waste and the difference of exhaust gas component finally discharged
And design.Certainly, the concrete form of tail gas terminal processing system 13 does not limit to, optional
Use cooling tower of the prior art and structure of column scrubber, i.e. tail gas terminal processing system 13
Including the cooling tower being connected with waste discharge blower fan and scrubbing tower.
The work process of the device of this enforcement superheated steam continuous anaerobic carbonization organic waste is:
By pending organic waste by automatic discharging device 42, send through feeding unit 1
Entering in carbonation unit 2, spiral feeder had both advanced material, simultaneously worked as material again uniform
The effect of contact superheated steam, thus ensure that carbonization is uniform.
During start, be first turned on tap water water intaking valve the 20, second air inlet valve, second day
So gas intake valve the 50, second blower fan 52 and Pressure gauge control inlet, start the second burning
Device 22, saturated steam generator 4 works, relief valve 23 overload protection.Start superheated steam
Generator 5, opens the first natural gas intake valve 27, the first air inlet valve 28, the first wind
Machine 55 and Pressure gauge control input quantity.Superheated steam combustion furnace 9 is to entering the first heat exchange
The saturated vapor of device 24 is heated, and the superheat steam temperature made is by the first furnace temperature data
Acquisition port 25 controls.And its superheated steam produced send vapour device 17 by superheated steam
Send into carbonation unit 2, first temperature data acquisition mouth the 40, second temperature data acquisition mouth 41
Detection, collection with hot systems link with control unit 15, total system electric control unit 14
Control system is run.Further, the i.e. carbonization number of cavities of carbonation unit 2 can be according to being disposed
The carbonization difficulty of organic waste and treating capacity be designed to multiple (1,2,3 etc.),
Two neighbouring carbide furnace head and the tail discharging openings and charging aperture vertical out-fall.
Pressure measuring unit 18, spiral feeder link with control system, organic waste
High temperature cabonization.Spiral feeder quantity can be according to the carbonization difficulty of the organic waste disposed
And treating capacity be designed to one to the four dry distilling gas produced through the first cyclone dust extractor 6, the
Two cyclone dust extractors 7 are sent into deodorization stove 8 and are burnt.
Open the 3rd natural gas intake valve 32, the 3rd air inlet valve 33, the 3rd blower fan 56
And Pressure gauge participates in controlling, open the 3rd burner 31, set deodorization stove 8 temperature 850～
1100 DEG C, the second furnace temperature data acquisition mouth 34 coordinated control system run, start deodorization stove
8 pairs of waste gas burnings sent into, clean process.Waste gas after clean process sends into superheated steam combustion
Burning stove 9 and carry out second-time burning, the furnace temperature of superheated steam combustion furnace 9 is by the first furnace temperature data acquisition
Mouth the 25, first temperature data acquisition mouth 40 and the second temperature data acquisition mouth 41 coordinated signals
System is run.The waste gas that secondary cleaning processes enters conduction oil through the 3rd cyclone dust extractor 10 and adds
Temperature device 11, then through the second heat exchanger 49, is sent into tail gas end by waste discharge blower fan 12
Reason system 13.Conduction-oil warming device 11 is by the most sharp for the waste heat of the tail gas through second-time burning
With, conduction oil of can heating, it is also possible to access saturated vapor device；Or individually heat warm water
Or access other devices needing heating.The circular heating work of conduction oil, simultaneously by inlet valve
37, draining valve 38, temperature probe 36, high temperature oil pump and other auxiliary device coordinate.Tail gas
Terminal processing system 13 can be different according to the organic waste of carbonization, final emission detections
The result of data, carries out conventional design and configuration.
To sum up, the technological means that the present embodiment mainly uses is summarized as follows:
One, according to the temperature needed for organic waste carbonization, 300 DEG C of-1000 DEG C of scopes are selected
Interior superheated steam is sent in carbide furnace (carbonation unit), makes the material in carbide furnace with overheated
The mixing contact that steam is full and uniform.Further, superheated steam is by common saturated vapor
Thermal dehydration forms, quick heating, and cost is the lowest.Because being that directly contact organic waste is passed away carbon
Changing speed fast, efficiency is high.
Two, the saturated vapor that water makes more than 100 DEG C by saturated steam generator is sent into
Superheated steam generator, utilizes combustion of natural gas to heat, quick by internal heat exchanger system
Make the superheated steam of about 1000 DEG C.
Three, according to the specified temp needed for organic waste carbonization, system is controlled by temperature acquisition
Uniting and the superheated steam of specific 100 DEG C～1000 DEG C silicon carbide is sent into carbide furnace, carbonization is organic
Garbage.
Four, in superheated steam sends into carbide furnace, the organic waste in stove is made to fill with superheated steam
The mixing contact divided.
Five, the spiral propeller in carbide furnace, in addition to advancing the organic waste effect of moving ahead, with
Time also full and uniform for organic waste is exposed in superheated steam, make organic waste abundant
Uniform high-efficiency carbonization.
Six, for ensureing that this device is anaerobic carbonization, carbide furnace is designed as negative pressure carbide furnace, logical
Cross vacuum extractor and input and output material sealing device complete, it is ensured that air does not enter in carbide furnace,
The high temperature gas that superheated steam is dehydration sending into carbide furnace is also free from oxygen, so this device
Anaerobic carbonization stove for real meaning.
Seven, carbide furnace internal coiling propeller further ensure that the organic waste of carbonization fully,
Mix, directly contact superheated steam.
It is last it is noted that various embodiments above is only in order to illustrate technical side of the present utility model
Case, is not intended to limit；Although this utility model having been carried out in detail with reference to foregoing embodiments
Explanation, it will be understood by those within the art that: it still can be to aforementioned each enforcement
Technical scheme described in example is modified, or enters the most some or all of technical characteristic
Row equivalent；And these amendments or replacement, do not make the essence disengaging of appropriate technical solution
The scope of this utility model each embodiment technical scheme.
Claims (10)
1. the device of a superheated steam continuous anaerobic carbonization organic waste, it is characterised in that
The feeding unit that including control system and is connected with control system communication respectively, carbonation unit,
Discharging unit, the first cyclone dust extractor, the second cyclone dust extractor, deodorization stove, superheated steam are sent out
Raw device, the 3rd cyclone dust extractor, conduction-oil warming device, waste discharge blower fan and tail gas terminal processes
System；
Described feeding unit is sequentially connected with carbonation unit, discharging unit；
Described carbonation unit is provided with superheated steam entrance point and waste gas outlet end, described superheated steam
Entrance point is connected with the heat exchange section in described superheated steam generator, described waste gas outlet end
It is sequentially connected with described first cyclone dust extractor, the second cyclone dust extractor and deodorization stove, and,
Furnace chamber part, the 3rd cyclone dust extractor of described deodorization stove and superheated steam generator, lead
Deep fat heating apparatus, waste discharge blower fan and tail gas terminal processing system are sequentially connected with.
Superheated steam the most according to claim 1 continuous anaerobic carbonization organic waste
Device, it is characterised in that be provided with carbonization cavity in described carbonation unit, sets in carbonization cavity
Carbonization feeding screw and superheated steam is had to send vapour device；
Described superheated steam send the superheated steam entrance point that vapour device is positioned at described carbonation unit, and
It is connected with the heat exchange section of superheated steam generator；
Pressure measuring unit, described pressure measuring unit, carbonization it is additionally provided with on described carbonation unit
Feeding screw is connected with described control system communication respectively.
Superheated steam the most according to claim 2 continuous anaerobic carbonization organic waste
Device, it is characterised in that described superheated steam generator includes superheated steam combustion furnace, setting
The first heat exchanger in superheated steam combustion furnace and be arranged at superheated steam combustion furnace one
First burner of end；
The port of export of described first heat exchanger and described superheated steam send vapour device to pass through pipeline
Connect, and on pipeline between, be respectively equipped with the first temperature data acquisition mouth, the second temperature
Degrees of data acquisition port；Described first temperature data acquisition mouth and the second temperature data acquisition mouth are respectively
It is connected with control system communication；
The inlet end of described first burner connects the first natural gas line, the first air hose
Road, described first natural gas line is provided with the first Pressure gauge and the first natural gas intake valve, institute
State the first air line and be provided with the second Pressure gauge, the first air inlet valve and the first blower fan；
Described superheated steam combustion furnace is provided with the first furnace temperature data acquisition mouth, described first furnace temperature
Data acquisition mouth is connected with control system communication.
Superheated steam the most according to claim 3 continuous anaerobic carbonization organic waste
Device, it is characterised in that the arrival end of described first heat exchanger connects has saturated vapor to occur
Device；
Set on passage between the arrival end of described saturated steam generator and the first heat exchanger
Having the 6th Pressure gauge, described saturated steam generator connects to be had relief valve, inlet channel and goes out
Waterpipe, described inlet channel is provided with water intaking valve and water meter, and described outlet conduit is provided with out
Water valve；
One end of described saturated steam generator is provided with the second burner, described second burner
Inlet end connect have the second natural gas line, the second air line, described second natural gas tube
Road is provided with the 3rd Pressure gauge and the second natural gas intake valve, and described second air line is provided with
Second blower fan and the second air valve.
Superheated steam the most according to claim 4 continuous anaerobic carbonization organic waste
Device, it is characterised in that one end of described deodorization stove is provided with the 3rd burner, the described 3rd
The inlet end of burner connects the 3rd natural gas line, the 3rd air line, described 3rd day
So feed channel is provided with the 4th Pressure gauge and the 3rd natural gas intake valve, described 3rd air line
It is provided with the 5th Pressure gauge, the 3rd air inlet valve and the 3rd blower fan；
Described deodorization stove is provided with the second furnace temperature data acquisition mouth, described second furnace temperature data acquisition
Mouth is connected with described control system communication.
Superheated steam the most according to claim 3 continuous anaerobic carbonization organic waste
Device, it is characterised in that described conduction-oil warming device connect have temperature probe, inlet valve and
Draining valve, and in conduction-oil warming device, it is provided with the second heat exchanger, described second heat exchange
The entrance point of device and the 3rd cyclone dust extractor connect, the port of export of described second heat exchanger and row
Useless blower fan connects.
Superheated steam the most according to claim 6 continuous anaerobic carbonization organic waste
Device, it is characterised in that the pipe between described waste discharge blower fan and the port of export of the second heat exchanger
Road is provided with the 3rd temperature data acquisition mouth, described 3rd temperature data acquisition mouth and control system
Communication connects.
Superheated steam the most according to claim 1 continuous anaerobic carbonization organic waste
Device, it is characterised in that be provided with in described tail gas terminal processing system activated carbon adsorption unit,
Any one or a few combination in desulfurizer and denitrification apparatus.
Superheated steam the most according to claim 1 continuous anaerobic carbonization organic waste
Device, it is characterised in that described tail gas terminal processing system includes cold with what waste discharge blower fan was connected
But tower and scrubbing tower.
Superheated steam the most according to claim 1 continuous anaerobic carbonization organic waste
Device, it is characterised in that described feeding unit includes being arranged at the spiral of carbonation unit one end
Feeder, the arrival end of described spiral feeder is provided with automatic discharging device；
Described feeding unit includes the Water-cooled screw collecting machine being arranged at the carbonation unit other end,
Described Water-cooled screw collecting machine connects rewinding case, described Water-cooled screw collecting machine and carbonization
Pipeline between unit is provided with the 4th temperature data acquisition mouth, described 4th temperature data acquisition
Mouth is connected with control system communication.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620450475.5U CN205628892U (en) | 2016-05-17 | 2016-05-17 | Continuous anaerobic carbonization organic waste's of superheated steam device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620450475.5U CN205628892U (en) | 2016-05-17 | 2016-05-17 | Continuous anaerobic carbonization organic waste's of superheated steam device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205628892U true CN205628892U (en) | 2016-10-12 |
Family
ID=57056842
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620450475.5U Active CN205628892U (en) | 2016-05-17 | 2016-05-17 | Continuous anaerobic carbonization organic waste's of superheated steam device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205628892U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105834196A (en) * | 2016-05-17 | 2016-08-10 | 江苏亿尔等离子体科技有限公司 | Device for continuously conducting oxygen-free carbonization on organic waste through superheated steam |
| CN106348371A (en) * | 2016-11-17 | 2017-01-25 | 山东大学 | method for removing volatile organic compounds from degradation-resistant water |
| CN108102674A (en) * | 2017-12-22 | 2018-06-01 | 江苏民和机械制造有限公司 | Carbonized by means of superheated steam stove |
-
2016
- 2016-05-17 CN CN201620450475.5U patent/CN205628892U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105834196A (en) * | 2016-05-17 | 2016-08-10 | 江苏亿尔等离子体科技有限公司 | Device for continuously conducting oxygen-free carbonization on organic waste through superheated steam |
| CN106348371A (en) * | 2016-11-17 | 2017-01-25 | 山东大学 | method for removing volatile organic compounds from degradation-resistant water |
| CN106348371B (en) * | 2016-11-17 | 2019-04-12 | 山东大学 | The minimizing technology of volatile organic matter in a kind of water difficult to degrade |
| CN108102674A (en) * | 2017-12-22 | 2018-06-01 | 江苏民和机械制造有限公司 | Carbonized by means of superheated steam stove |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105834196A (en) | Device for continuously conducting oxygen-free carbonization on organic waste through superheated steam | |
| CN103376002B (en) | Method and device for utilizing waste heat of high-temperature flue gas | |
| CN106006799A (en) | Method and device for carbonizing production wastewater of printing and dyeing intermediates through superheated steam | |
| CN205628892U (en) | Continuous anaerobic carbonization organic waste's of superheated steam device | |
| CN205653405U (en) | Superheated steam carbide furnace | |
| CN106001050B (en) | The device and method of carbonized by means of superheated steam organic waste heat recovery | |
| CN105889986A (en) | Gas cooking stove purifying lampblack through heat power | |
| CN107022363A (en) | A kind of continuous biomass pyrolysis gas is reversely flowd back towards with charcoal gas cogeneration facility | |
| CN206369204U (en) | A kind of pipeline for gas flue gas waste heat recovery system | |
| CN104101225B (en) | For improving the system and method for calcium carbide stove exhaust comprehensive utilization ratio | |
| CN204097408U (en) | A kind of medical waste cracking refining equipment | |
| CN106679174A (en) | High-temperature hot blast stove | |
| CN207596786U (en) | The equipment that a kind of tedge waste heat recovery and coking smoke comprehensive are administered | |
| CN205893035U (en) | Low heat value mud " three change " processing apparatus | |
| CN108102674A (en) | Carbonized by means of superheated steam stove | |
| CN107270308A (en) | A kind of carbide furnace combustible exhaust gas calory burning retracting device | |
| CN203464804U (en) | Device utilizing waste heat of high-temperature flue gas | |
| CN103629682A (en) | Boiler waste heat utilization system | |
| CN209876897U (en) | Superheated steam generator and high-temperature steam generating device | |
| CN204421018U (en) | A kind of dangerous waste incineration and bootstrap system thereof | |
| CN206221008U (en) | Single-row feed pump turbine exhaust valve system and the fired power generating unit using the system | |
| CN206369480U (en) | Copper refining flue gas system and its flue gas cooling device | |
| CN207750970U (en) | A kind of biomass direct-fired flue gas coupled electricity-generation system | |
| CN206546026U (en) | Sectional type hot air stove | |
| CN206799536U (en) | A kind of full-automatic damaged tire cracker |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20231229 Address after: 225400 Hanzhuang Road, Huangqiao Industrial Park, Taixing City, Taizhou City, Jiangsu Province Patentee after: Jiangsu Blue Green Environmental Protection Technology Co.,Ltd. Address before: 215300 Hanzhuang Road, Huangqiao Industrial Park, Taixing City, Taizhou City, Jiangsu Province Patentee before: JIANGSU YIER PLASMA SCIENCE & TECHNOLOGY Co.,Ltd. |
|
| TR01 | Transfer of patent right |