CN108018051A - Destructive distillation carbonization machine and destructive distillation carbonizing apparatus - Google Patents
Destructive distillation carbonization machine and destructive distillation carbonizing apparatus Download PDFInfo
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- CN108018051A CN108018051A CN201810000773.8A CN201810000773A CN108018051A CN 108018051 A CN108018051 A CN 108018051A CN 201810000773 A CN201810000773 A CN 201810000773A CN 108018051 A CN108018051 A CN 108018051A
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- destructive distillation
- material conveying
- condenser
- carbonization machine
- conveying device
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- 238000000197 pyrolysis Methods 0.000 title claims abstract description 48
- 238000003763 carbonization Methods 0.000 title claims abstract description 32
- 238000010000 carbonizing Methods 0.000 title claims abstract description 11
- 239000000463 material Substances 0.000 claims abstract description 83
- 230000007246 mechanism Effects 0.000 claims abstract description 31
- 238000010438 heat treatment Methods 0.000 claims abstract description 30
- 238000010079 rubber tapping Methods 0.000 claims description 21
- 239000002893 slag Substances 0.000 claims description 12
- 238000007789 sealing Methods 0.000 claims description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 10
- 230000002093 peripheral effect Effects 0.000 claims 1
- 239000007789 gas Substances 0.000 description 51
- 239000003921 oil Substances 0.000 description 25
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 9
- 238000000034 method Methods 0.000 description 6
- 239000000446 fuel Substances 0.000 description 5
- 239000000498 cooling water Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000004064 recycling Methods 0.000 description 4
- 239000002028 Biomass Substances 0.000 description 3
- 239000000567 combustion gas Substances 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000004880 explosion Methods 0.000 description 3
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000011534 incubation Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 230000002045 lasting effect Effects 0.000 description 1
- 239000011287 low-temperature tar Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000013308 plastic optical fiber Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000011269 tar Substances 0.000 description 1
- 235000021419 vinegar Nutrition 0.000 description 1
- 239000000052 vinegar Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B1/00—Retorts
- C10B1/02—Stationary retorts
- C10B1/06—Horizontal retorts
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
- C10B49/02—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
- C10B53/02—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of cellulose-containing material
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K5/00—Feeding or distributing other fuel to combustion apparatus
- F23K5/002—Gaseous fuel
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The present invention provides destructive distillation carbonization machine, has the destructive distillation carbonizing apparatus of the destructive distillation carbonization machine, is related to destructive distillation carbonization technical field.Wherein, destructive distillation carbonization machine includes horizontal material conveying device, feed arrangement and condenser, one end of horizontal material conveying device is connected with feed arrangement, the other end of device for transporting objects is equipped with oil gas vent, device for transporting objects is used to convey material from feed arrangement to oil gas vent, oil gas vent is connected with condenser, and condenser has condenser oil outlet；The outside of device for transporting objects is equipped with heating chamber, and heating chamber has hot gas inlet and heat outlet, and hot gas inlet is used to connect with hot gas feeding mechanism.The invention can solve destructive distillation carbonizing apparatus existing in the prior art can not be to the technical problem of leftover pieces continuous processing.
Description
Technical field
It is carbonized technical field the present invention relates to destructive distillation, more particularly to destructive distillation carbonization machine and is provided with the dry of the destructive distillation carbonization machine
Evaporate carbonizing apparatus.
Background technology
Retorting technique is widely used, and what use was most wide at present is the destructive distillation to biomass to coal carbonization, to olefines material
The destructive distillation of material and the retorting technique to house refuse.
Destructive distillation is carried out at a temperature of coal is placed in 550 DEG C or so, to produce low temperature tar, while can also obtain semicoke and
Low temperature coke-stove gas.By drying and dewaterings such as biomass straw, branches, add destructive distillation in carbide furnace and be carbonized, can generate biomass carbon,
Combustion gas and wood vinegar.To the isolation air heating destructive distillation of olefines material, aromatic naphtha, tar, fuel oil etc. can be produced, it is remaining dry
Evaporating carbide (breeze) can use the finely divided separation system production of superfinishing to activate high-quality charcoal.
After broken apart to the progress of luggage leftover pieces, predominantly PVC granule and plastic optical fibre, both materials can be used as
Luggage liner plate is processed, but wherein some disabled isolate mixes wherein, to carry out harmless treatment to it, the portion
It is mostly flocculence, complicated component, the fiber containing a variety of plastics and a small amount of cotton fiber to divide material.It is similar that destructive distillation carbonization is carried out to it
In the processing to olefines material, and olefines distillation apparatus is typically vertical, discontinuous production, and it is inapplicable with to these sides
The processing of corner material isolate.
The content of the invention
, can not to solve destructive distillation carbonizing apparatus existing in the prior art it is an object of the invention to provide destructive distillation carbonization machine
To the technical problem of leftover pieces continuous processing.
Destructive distillation carbonization machine, including horizontal material conveying device, feed arrangement and condenser, the one of horizontal material conveying device
End is connected with feed arrangement, and the other end of device for transporting objects is equipped with oil gas vent, device for transporting objects for by material from into
Expect that device is conveyed to oil gas vent, oil gas vent is connected with condenser, and condenser has condenser oil outlet；
The outside of device for transporting objects is equipped with heating chamber, and heating chamber has hot gas inlet and heat outlet, and hot gas inlet is used
Connected in hot gas feeding mechanism.
Destructive distillation carbonization machine of the present invention has the beneficial effect that：
The destructive distillation carbonization machine, by by the horizontal setting of device for transporting objects, and is equipped with feed arrangement friction feeding, heating chamber
In hot gas and device for transporting objects between heat exchange, material can be realized while conveying, while heat, so as to allow material to exist
Fusing or even vaporization olefiant gas in device for transporting objects progressively, then can be by condenser for wherein condensable part
Oil outlet is discharged.So as to formed with chemical industry material, the final recycling realized to leftover pieces, the present invention is by current interval
Formula improvement of operation is continuous schedule operation, improves production efficiency, the oil gas leakage problem for generation of reloading when reducing batch operation.
Preferable technical solution, its supplementary features are：Feed arrangement includes charging power source, charging power source and charging
Axis connection, is provided with charging helical blade on the axis that feeds, the top of the helical blade that feeds is equipped with charging hopper.
By setting feed power source drive charging axis and charging helical blade to carry out feeding, it can make it that charging hopper is remote
Off normal the horizontal material conveying device in heating chamber, avoid the gas of higher temperature in horizontal material conveying device from charging
Escaped in device, influence the charging process of feed arrangement.
Further preferred technical solution, its supplementary features are：Feed arrangement and horizontal material conveying device are equipped with the
One sealing flange.
By setting the first sealing flange, the thermal loss of heating chamber to avoid the hot gas effusion in heating chamber, can be reduced,
So as to improve capacity usage ratio.
Preferable technical solution, its supplementary features are：Rotated in horizontal material conveying device and be provided with material conveying master
Axis, is disposed with feed auger blade from the feed end of horizontal material conveying device to discharge end on material conveying main spindle, stirs
Mix blade and helical blade of slagging tap.
, can be in temperature by setting feed auger blade, agitating vane, blade of slagging tap respectively on material conveying main spindle
Higher region sets the blade for adapting to the stronger material of high temperature capabilities, in temperature lower region, common blade is set, so that nothing
It need to be set up in the length whole side of material conveying main spindle and adapt to the stronger blade of high temperature capabilities, so as to reduce the system of equipment
Cause this.
Further preferred technical solution, its supplementary features are：Main shaft power source, main shaft power source and thing are further included
Expect conveying main spindle connection, material conveying main spindle is disposed through the second closing flange of horizontal material conveying device one end.
By setting the second sealing flange, the thermal loss of heating chamber to avoid the hot gas effusion in heating chamber, can be reduced,
So as to improve capacity usage ratio.
Preferable technical solution, its supplementary features are：Horizontal material conveying device is equipped with deslagging device in discharge end, goes out
Slag device includes the first tapping mechanism and the second tapping mechanism for being arranged on the lower part of the discharge end of horizontal material conveying device, the
One tapping mechanism is located at the top of the second tapping mechanism, and the first tapping mechanism includes the first cleanout door and is driven with the first cleanout door
The first of connection is slagged tap motor, and what the second tapping mechanism included the second cleanout door and was sequentially connected with the second cleanout door second slags tap
Motor.
By setting two tapping mechanisms, two tapping mechanisms can be utilized alternately to open or close, by residue from sleeping
The discharge end discharge of formula device for transporting objects.It can ensure the air-free state in horizontal material conveying device, reduce oil gas
Leakage, reduces risk of explosion.
Preferable technical solution, its supplementary features are：Condenser has cooling water inlet and hot water outlet.
By setting cooling water inlet and hot water outlet, it can constantly fill into cold water and hot water is flowed out, can
Worked continuously with allowing condenser to realize, so as to improve the cooling capacity of condenser, and then improve the possibility of volume increase.
Further preferred technical solution, its supplementary features are：Condenser also has an exhaust outlet, exhaust outlet and hot gas into
Mouth connection.
By setting exhaust outlet, uncondensable gas is sent into hot air intake, and combustor flame co-fire, so as to have
The consumption for reducing combustion gas of effect.The recycling of the incondensable gas in oil gas is also achieved at the same time.
Preferable technical solution, its supplementary features are：Heating chamber is externally provided with insulating layer.
By setting insulating layer, be conducive to improve the heat-insulating property of heating chamber, reduce the unnecessary consumption of heat, improve the energy
Utilization rate.
Hot gas feeding mechanism and any of the above-described destructive distillation carbonization are provided with it is another object of the present invention to provide a kind of
Machine, hot gas feeding mechanism are combustor, and hot air intake is connected with combustor.
The destructive distillation carbonizing apparatus, all technique effects not only with above-mentioned destructive distillation carbonization machine.And burnt by setting
Machine, can utilize the burning of the fuel such as externally input methanol to realize and convey hot gas to heating chamber, conversion can also be utilized to be formed
Uncondensable gas burn, mixed with fuel flame carry out second-time burning so that leftover pieces can be converted.
Brief description of the drawings
, below will be to specific in order to illustrate more clearly of the specific embodiment of the invention or technical solution of the prior art
Embodiment or attached drawing needed to be used in the description of the prior art are briefly described, it should be apparent that, in describing below
Attached drawing is some embodiments of the present invention, for those of ordinary skill in the art, before not making the creative labor
Put, other attached drawings can also be obtained according to these attached drawings.
Fig. 1 is the front view of the destructive distillation carbonization machine of the embodiment of the present invention one；
Fig. 2 is the top view of Fig. 1；
Fig. 3 is the left view of Fig. 1；
Fig. 4 is the front view of the destructive distillation carbonizing apparatus of the embodiment of the present invention one；
Fig. 5 is the top view of Fig. 4；
Fig. 6 is the left view of Fig. 4.
The implication that reference numeral used represents in each embodiment is as follows：1- charging retarders；2- charging hoppers；3- adds
Expect axis；4- main shaft retarders；5- horizontal material conveying devices；6- material conveying main spindles；7- feed auger blades；8- paddles
Piece；9- slags tap blade；10- bases；11- hot gas inlets；12- heat outlets；13- insulating layers；14- first slags tap motor；15-
One cleanout door；The second cleanout doors of 16-；17- oil gas vents；18- condensers；The first sealing flanges of 20-；21- spindle motors；22-
Feed helical blade；The second sealing flanges of 23-；24- combustors；25- charging motors；26- second slags tap motor；27- exhaust outlets；
28- condenser oil outlets.
Embodiment
Technical scheme is clearly and completely described below in conjunction with attached drawing, it is clear that described implementation
Example is part of the embodiment of the present invention, instead of all the embodiments.Based on the embodiments of the present invention, ordinary skill
Personnel's all other embodiments obtained without making creative work, belong to the scope of protection of the invention.
Embodiment one
As shown in Figure 1-Figure 3, the present embodiment provides a kind of destructive distillation carbonization machine, including horizontal material conveying device 5, charging dress
Put with condenser 18, wherein, horizontal material conveying device 5, feed arrangement can be installed on base 10 on, horizontal material conveying
One end of device 5 is connected with feed arrangement, and the other end of device for transporting objects is equipped with oil gas vent 17, and device for transporting objects is used for
Material is conveyed from feed arrangement to oil gas vent 17, oil gas vent 17 is connected with condenser 18, and condenser 18 has condenser
Oil outlet 28；
The outside of device for transporting objects is equipped with heating chamber, and heating chamber has hot gas inlet 11 and heat outlet 12, and hot gas enters
Mouth 11 is used to connect with hot gas feeding mechanism, and heat outlet 12 is used for the air after being heated to horizontal material conveying device 5 is defeated
Go out.Wherein, hot gas inlet 11 and heat outlet 12 are preferably disposed on the both ends on incubation cavity length direction, to realize to heating chamber
Space making full use of and device for transporting objects made full use of.
The destructive distillation carbonization machine, by by the horizontal setting of device for transporting objects, and is equipped with feed arrangement friction feeding, heating chamber
In hot gas and device for transporting objects between heat exchange, material can be realized while conveying, while heat, so as to allow material to exist
Fusing or even vaporization olefiant gas in device for transporting objects progressively, then can be by condenser for wherein condensable part
Oil outlet 28 is discharged.So as to formed with chemical industry material, the final recycling realized to leftover pieces.
Particularly, feed arrangement includes charging power source, and charging power source is charging motor 25 and the retarder 1 that feeds
Combination, charging retarder 1 are connected with charging axis 3, and charging helical blade 22 is provided with the axis 3 that feeds, charging helical blade 22
Top is equipped with charging hopper 2.
By setting charging power source drive charging axis 3 and charging helical blade 22 to carry out feeding, it can cause charging material
Bucket 2 is located away the horizontal material conveying device 5 in heating chamber, avoids the gas of the higher temperature in horizontal material conveying device 5
Body is escaped from feed arrangement, influences the charging process of feed arrangement.
Further particularly, feed arrangement is connected by the first sealing flange 20 with horizontal material conveying device 5.Its
In, charging hole is equipped with the first sealing flange 20, to ensure that material can be smoothly entered in horizontal material conveying device 5.
By setting the first sealing flange 20, the heat damage of heating chamber to avoid the hot gas effusion in heating chamber, can be reduced
Lose, so as to improve capacity usage ratio.
Particularly, rotated in horizontal material conveying device 5 and be provided with material conveying main spindle 6, wherein, installation material conveying
The bearing of main shaft 6 can be located at the both ends of horizontal material conveying device 5, so that the problem of advantageously reducing bearing present position,
Improve the service life of bearing.Set gradually on material conveying main spindle 6 from the feed end of horizontal material conveying device 5 to discharge end
There are feed auger blade 7, agitating vane 8 and helical blade of slagging tap.
By setting feed auger blade 7, agitating vane 8, blade 9, Ke Yi of slagging tap respectively on material conveying main spindle 6
The higher region of temperature sets the blade for adapting to the stronger material of high temperature capabilities, in temperature lower region, sets common blade, from
The stronger blade of high temperature capabilities is adapted to without being set up in the length whole side of material conveying main spindle 6, is set so as to reduce
Standby manufacture cost.
Further particularly, 6 power source of main shaft has been further included, 6 power source of main shaft is spindle motor in the present embodiment
21 are connected with the combination of main shaft retarder 4, spindle motor 21 with main shaft retarder 4, main shaft retarder 4 and material conveying main spindle 6
Connection, material conveying main spindle 6 are disposed through the second closing flange of 5 one end of horizontal material conveying device.
By setting the second sealing flange 23, the heat damage of heating chamber to avoid the hot gas effusion in heating chamber, can be reduced
Lose, so as to improve capacity usage ratio.
Particularly, horizontal material conveying device 5 is equipped with deslagging device in discharge end, and deslagging device includes being arranged on horizontal
The first tapping mechanism and the second tapping mechanism of the lower part of the discharge end of device for transporting objects 5, the first tapping mechanism are located at second
The top of tapping mechanism, the first tapping mechanism include the first cleanout door 15 and slag tap with the first of the first cleanout door 15 drive connection
Motor 14, what the second tapping mechanism included the second cleanout door 16 and was sequentially connected with the second cleanout door 16 second slags tap motor 26.
By setting two tapping mechanisms, two tapping mechanisms can be utilized alternately to open or close, by residue from sleeping
The discharge end discharge of formula device for transporting objects 5.It can ensure the air-free state in horizontal material conveying device 5, reduce oil
Gas leaks outside, and reduces risk of explosion.
Particularly, condenser 18 has cooling water inlet and hot water outlet, can by setting cooling water inlet and hot water outlet
Constantly to fill into cold water and enable hot water to flow out, condenser can be allowed to realize and worked continuously, so as to improve condensation
The cooling capacity of device, and then improve the possibility of volume increase.
Further particularly, condenser 18 also has exhaust outlet 27, and exhaust outlet 27 is connected with hot air intake.Specifically,
One threeway is set in condenser collection port position, and a mouth connects the condenser pipe in condenser, and a mouth is fuel-displaced for condenser
Mouthfuls 28, oil droplet is condensed for collecting, another mouth is exhaust outlet 27, for connecting pipe to firing hot air intake.
By setting exhaust outlet 27, uncondensable gas is sent into hot air intake, and combustor flame co-fire, so that
Effectively reduce the consumption of combustion gas.The recycling of the incondensable gas in oil gas is also achieved at the same time.
Particularly, heating chamber is externally provided with insulating layer 13.By setting insulating layer 13, be conducive to improve the insulation of heating chamber
Performance, reduces the unnecessary consumption of heat, improves energy utilization rate.
Embodiment two
As Figure 4-Figure 6, the present embodiment provides it is another object of the present invention to provide a kind of destructive distillation carbonizing apparatus,
Be provided with hot gas feeding mechanism and any of the above-described destructive distillation carbonization machine, which is combustor, hot gas inlet 11 with
Combustor 24 connects.Specifically, combustor bocca is placed in hot gas inlet 11, the gas meeting and combustion discharged from exhaust outlet 27
One combust of burning machine flame.
The destructive distillation carbonizing apparatus, all technique effects not only with above-mentioned destructive distillation carbonization machine.And burnt by setting
Machine, can utilize the burning of the fuel such as externally input methanol to realize and convey hot gas to heating chamber, conversion can also be utilized to be formed
Uncondensable gas burn, mixed with fuel flame carry out second-time burning so that leftover pieces can be converted.
The operating principle of the present embodiment is：
These luggage leftover pieces isolates are put into feeding device from charging hopper 2, pass through motor 25 and the charging of feeding
Retarder 1 drives charging axis 3 and charging helical blade 22 to be transported to the inlet of horizontal material conveying device 5.
Main shaft retarder 4 drives material conveying main spindle 6 to rotate, and feed auger blade 7 will be located at horizontal material conveying device 5
The isolate of feed zone be transported in bringing-up section, material is slowly fed from right to left by agitating vane 8, progressively heat.
Methanol burner is connected with hot gas inlet 11, lasting hot gas is imported in heating chamber, and in horizontal material conveying device 5
Material is heated, and remaining hot gas is discharged from heat outlet 12, at this time about 50 DEG C of outlet temperature.
Material constantly carries out destructive distillation during from feed end to discharge end, produces oil vapour, and oil vapour goes out from oil gas
Mouthfuls 17 are exported by pipeline, and condensing into oil droplet from condenser oil outlet 28 by the cooling of condenser 18 flows out.Wherein oil gas contains
A part of incondensible gas, which is imported into hot air intake through exhaust outlet 27 and serves as fuel, with combustor
One combust of flame.
It is unable to vaporize liquefied material residue, the position of the first cleanout door 15 is transported to by helical blade of slagging tap.This
Shi Qidong first slags tap motor 14, and the first cleanout door 15 is opened, and above-mentioned residue falls into area of slagging tap；Then first slags tap 14 band of motor
Dynamic first cleanout door 15 is closed, and is restarted second and is slagged tap motor 26, and the second cleanout door 16 is opened, and discharges residue, i.e. carbon black.Two
Cleanout door alternately opens the door, closes the door, and ensure that the air-free state in destructive distillation carbonization machine, prevents oil gas from leaking outside, and reduces risk of explosion.
In the description of the present invention, it is necessary to explanation, term " " center ", " on ", " under ", "left", "right", " vertical ",
The orientation or position relationship of the instruction such as " level ", " interior ", " outer " be based on orientation shown in the drawings or position relationship, merely to
Easy to describe the present invention and simplify description, rather than instruction or imply signified device or element must have specific orientation,
With specific azimuth configuration and operation, therefore it is not considered as limiting the invention.In addition, term " first ", " second ",
" the 3rd " is only used for description purpose, and it is not intended that instruction or hint relative importance.
In the description of the present invention, it is necessary to illustrate, unless otherwise clearly defined and limited, term " installation ", " phase
Even ", " connection " should be interpreted broadly, for example, it may be being fixedly connected or being detachably connected, or be integrally connected；Can
To be mechanical connection or be electrically connected；It can be directly connected, can also be indirectly connected by intermediary, Ke Yishi
Connection inside two elements.For the ordinary skill in the art, with concrete condition above-mentioned term can be understood at this
Concrete meaning in invention.
Finally it should be noted that：The above embodiments are only used to illustrate the technical solution of the present invention., rather than its limitations；To the greatest extent
Pipe is described in detail the present invention with reference to foregoing embodiments, it will be understood by those of ordinary skill in the art that：Its according to
Can so modify to the technical solution described in foregoing embodiments, either to which part or all technical characteristic into
Row equivalent substitution, such as：
(1) in embodiment 1, be feed power source and main shaft power source selection be motor and retarder combination, actually
Other power sources such as hydraulic motor can also be selected, can also realize same effect as needed；
And these modifications or replacement, the essence of appropriate technical solution is departed from various embodiments of the present invention technical solution
Scope.
Claims (10)
1. destructive distillation carbonization machine, it is characterised in that including horizontal material conveying device, feed arrangement and condenser, the horizontal thing
One end of material conveying device is connected with feed arrangement, and the other end of the device for transporting objects is equipped with oil gas vent, the material
Conveying device is used to convey material from the feed arrangement to the oil gas vent, and the oil gas vent connects with the condenser
Logical, the condenser has condenser oil outlet；
The outside of the device for transporting objects is equipped with heating chamber, and the heating chamber has hot gas inlet and heat outlet, the heat
Gas entrance is used to connect with hot gas feeding mechanism.
2. destructive distillation carbonization machine according to claim 1, it is characterised in that the feed arrangement includes charging power source, institute
Charging power source and charging axis connection are stated, charging helical blade, the upper of helical blade that feed are installed on the charging axis
Side is equipped with charging hopper.
3. destructive distillation carbonization machine according to claim 2, it is characterised in that the feed arrangement is conveyed with the horizontal material
Device is equipped with the first sealing flange.
4. according to the destructive distillation carbonization machine described in claim 1 or 2 or 3, it is characterised in that the horizontal material conveying device transfer
Move and be provided with material conveying main spindle, from the feed end of the horizontal material conveying device to discharge end on the material conveying main spindle
It is disposed with feed auger blade, agitating vane and helical blade of slagging tap.
5. destructive distillation carbonization machine according to claim 4, it is characterised in that further included main shaft power source, the main shaft moves
Power source is connected with the material conveying main spindle, and the material conveying main spindle is disposed through described horizontal material conveying device one end
Second closing flange.
6. according to the destructive distillation carbonization machine any one of claim 1,2,3,5, it is characterised in that the horizontal material conveying
Device is equipped with deslagging device in discharge end, and the deslagging device includes the discharge end for being arranged on the horizontal material conveying device
The first tapping mechanism and the second tapping mechanism of lower part, first tapping mechanism are located at the top of second tapping mechanism,
What first tapping mechanism included the first cleanout door and was sequentially connected with the first cleanout door first slags tap motor, and described second goes out
What slag mechanism included the second cleanout door and was sequentially connected with the second cleanout door second slags tap motor.
7. according to the destructive distillation carbonization machine any one of claim 1,2,3,5, it is characterised in that the condenser has cold
Water inlet and hot water outlet.
8. destructive distillation carbonization machine according to claim 7, it is characterised in that the condenser also has exhaust outlet, the row
Gas port is connected with hot air intake.
9. according to the destructive distillation carbonization machine any one of claim 1,2,3,5,8, it is characterised in that the heating chamber peripheral hardware
There is insulating layer.
10. destructive distillation carbonizing apparatus, it is characterised in that be provided with any one of hot gas feeding mechanism and claim 1-9
Destructive distillation carbonization machine, the hot gas feeding mechanism are combustor, and the hot air intake is connected with combustor.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810000773.8A CN108018051A (en) | 2018-01-02 | 2018-01-02 | Destructive distillation carbonization machine and destructive distillation carbonizing apparatus |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810000773.8A CN108018051A (en) | 2018-01-02 | 2018-01-02 | Destructive distillation carbonization machine and destructive distillation carbonizing apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108018051A true CN108018051A (en) | 2018-05-11 |
Family
ID=62071179
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810000773.8A Pending CN108018051A (en) | 2018-01-02 | 2018-01-02 | Destructive distillation carbonization machine and destructive distillation carbonizing apparatus |
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| CN (1) | CN108018051A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2021011979A1 (en) * | 2019-07-25 | 2021-01-28 | Next Generation Elements Gmbh | Thermochemical processing method and processing installation designed therefor |
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