CN207121568U - pyrolytic reaction device - Google Patents
pyrolytic reaction device Download PDFInfo
- Publication number
- CN207121568U CN207121568U CN201720754750.7U CN201720754750U CN207121568U CN 207121568 U CN207121568 U CN 207121568U CN 201720754750 U CN201720754750 U CN 201720754750U CN 207121568 U CN207121568 U CN 207121568U
- Authority
- CN
- China
- Prior art keywords
- heater
- pyrolysis
- mixing
- reaction device
- pyrolytic reaction
- 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
Landscapes
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The utility model discloses a kind of pyrolytic reaction device, including：Body of heater is pyrolyzed, first charging aperture is located on pyrolysis body of heater；Heating tube, heating tube are extend into pyrolysis oven body；Hydrid component, hydrid component includes multiple mixing bodies of heater and multiple agitators, each mixing body of heater is located at the lower section of pyrolysis body of heater and connected with pyrolysis body of heater, each mixing body of heater is provided with discharging opening, multiple agitators and multiple mixing bodies of heater are corresponded and set, each agitator includes the agitating shaft extending into corresponding holding furnace body, between heating tube and the upper end of agitating shaft, each agitating shaft rotates to mix the material being drained into from pyrolysis body of heater and second charging aperture in corresponding holding furnace body second charging aperture.Pyrolytic reaction device of the present utility model, the energy consumption of system can be reduced, improve the yield of reliability and pyrolytic tar.It is simultaneously simple in construction, reduce floor space to a certain extent, be easy to industrialize.
Description
Technical field
It the utility model is related to HTAC field, more particularly to a kind of pyrolytic reaction device.
Background technology
The system energy consumption of the pyrolytic reaction device of correlation technique is high, and consolidating after the material pyrolysis in pyrolytic reaction device
Itself sensible heat of state product is high, and the pyrolytic reaction device of correlation technique greatly wastes the sensible heat of solid product, so as to cause
The loss of energy.
Utility model content
The utility model is intended at least solve one of technical problem present in prior art.Therefore, the utility model carries
Go out a kind of pyrolytic reaction device, the energy consumption of system can be reduced, improve the yield of reliability and pyrolytic tar.It is simultaneously simple in construction,
Floor space can be reduced to a certain extent, be easy to industrialize.
According to the pyrolytic reaction device of the utility model embodiment, there is first charging aperture and second charging aperture, including：Heat
Body of heater is solved, the first charging aperture is located on the pyrolysis body of heater；Heating tube, the heating tube are extend into the pyrolysis oven body
To provide the material in the pyrolysis oven body pyrolysis heat；Hydrid component, the hydrid component include it is multiple mixing bodies of heater and
Multiple agitators, each mixing body of heater are located at the lower section of the pyrolysis body of heater and connected with the pyrolysis body of heater, Mei Gesuo
State mixing body of heater and be provided with discharging opening, the multiple agitator and the multiple mixing body of heater are corresponded and set, each described to stir
Mix the agitating shaft that device includes extending into the corresponding holding furnace body, the second charging aperture be located at the pyrolysis body of heater or
On the mixing body of heater, between the heating tube and the agitating shaft, each agitating shaft turns the second charging aperture
The dynamic material being drained into mixing from the pyrolysis body of heater and the second charging aperture in the corresponding holding furnace body.
According to the pyrolytic reaction device of the utility model embodiment, by setting hydrid component, so as to abundant land productivity
With the sensible heat of the solid product itself of caused high temperature after material pyrolysis in pyrolysis oven body, the energy consumption of system is effectively reduced, is carried
The yield of high reliability and pyrolytic tar.It is simultaneously simple in construction, floor space can be reduced to a certain extent, be easy to industry
Change.
According to some embodiments of the utility model, it is described mixing body of heater be two, the second charging aperture be one and
On the pyrolysis body of heater.So that the structure of pyrolytic reaction device is simple, it is easily manufactured.The position of second charging aperture is set simultaneously
The solid product being equipped with beneficial to the high temperature for enabling to discharge out of pyrolysis oven body is equably drained into two holding furnace bodies, and then
Improve the operating efficiency of pyrolytic reaction device.
According to some embodiments of the utility model, the agitating shaft includes axis body and multiple blades, each blade
It is enclosed on outside on the axis body, axially spaced-apart of the multiple blade along the axis body is located on the axis body.It follows that stirring
The structure of axle is simple, while advantageously ensures that the rotation of agitating shaft to being drained into each mixing from pyrolysis body of heater and second charging aperture
The mixed effect of material in body of heater, the material for making to be drained into holding furnace body from second charging aperture are fully utilized from pyrolysis oven
The sensible heat of the solid product for the high temperature being drained into vivo in holding furnace body, and then improve the production of the pyrolytic tar of pyrolytic reaction device
Rate.
Further, the cross section of the mixing body of heater is formed as circular, the diameter of each blade and corresponding institute
The ratio stated between the diameter of the internal perisporium of mixing body of heater is 0.3-0.5.Thus, be advantageous to solid product in holding furnace body from
Gap between mixing body of heater and agitator is moved to discharging opening to discharge pyrolytic reaction device, to be drained into from second charging aperture
Material in holding furnace body provides the space of pyrolysis, so as to ensure that the production of pyrolytic tar in holding furnace body to a certain extent
Rate, and then improve the whole work efficiency of pyrolytic reaction device.
Specifically, the length of the agitating shaft is 0.5-0.7 with the ratio of the length of the corresponding mixing body of heater.By
This, can enter and ensure the mixed effect that the material in holding furnace body is drained into from pyrolysis body of heater and second charging aperture, and then ensure
The yield of pyrolytic tar in holding furnace body.
According to some embodiments of the utility model, the first longitudinal direction central axis and horizontal plane of each mixing body of heater
Between angle be 10 ° -20 °, it is described pyrolysis body of heater second longitudinal direction central axis upright in the horizontal plane.So as to
The solid product of the high temperature in pyrolysis oven body is controlled to be drained into the speed in holding furnace body and holding furnace body to a certain extent
The speed that solid product is discharged from discharging opening, it is pyrolyzed the material in pyrolytic reaction device more abundant.It can control simultaneously
The quantity of the material in holding furnace body is drained into from pyrolysis body of heater and second charging aperture, the filling rate of material in holding furnace body is existed
Between 50%~65%, so as to provide effective sky for the discharge of caused oil gas after material pyrolysis in holding furnace body
Between, and then improve the yield of the pyrolytic tar of pyrolytic reaction device.
According to some embodiments of the utility model, the center of rotation axis of the agitating shaft and the corresponding holding furnace
The first longitudinal direction centerline axis parallel of body.So that pyrolysis body of heater and second charging aperture are drained into the material mixing in holding furnace body
More uniformly, and then make to be pyrolyzed from the material that second charging aperture is drained into holding furnace body more abundant.
Alternatively, the internal perisporium of each mixing body of heater is provided with thermal insulating material materials and parts.So as to be advantageous to avoid from pyrolysis
The internal perisporium of the heat of the solid product for the high temperature that body of heater is drained into holding furnace body from mixing body of heater outwards sheds, and then improves
The heat insulation effect of mixing body of heater, the efficiency of the pyrolytic tar of material in holding furnace body can be improved to a certain extent.
Specifically, the length ratio between the pyrolysis body of heater and each mixing body of heater is 1:1—3:1.Thereby, it is possible to
Ensure that material stops that 6s-9s is more abundant to be pyrolyzed from top to bottom in pyrolysis oven body, and then improve pyrolytic reaction device
The efficiency of pyrolytic tar, while the energy consumption of system is reduced to a certain extent.
Additional aspect and advantage of the present utility model will be set forth in part in the description, partly by from following description
In become obvious, or by it is of the present utility model practice recognize.
Brief description of the drawings
Of the present utility model above-mentioned and/or additional aspect and advantage will in the description from combination accompanying drawings below to embodiment
Become obvious and be readily appreciated that, wherein：
Fig. 1 is the schematic diagram according to the pyrolytic reaction device of the utility model embodiment；
Fig. 2 is the schematic diagram according to the blade of the utility model embodiment.
Reference：
Pyrolytic reaction device 100；
First charging aperture 1；Second charging aperture 2；It is pyrolyzed body of heater 3；Heating tube 4；Hydrid component 5；Mix body of heater 51；Agitator
52；Agitating shaft 521；Axis body 521a；Blade 521b；Motor 522；Discharging opening 6；Feed screw 7；Conveying worm 8；Combustion gas is entered
Mouth 9；Air intlet 10；Exhanst gas outlet 11；Oil gas vent 12.
Embodiment
Embodiment of the present utility model is described below in detail, the example of the embodiment is shown in the drawings, wherein from beginning
Same or similar element is represented to same or similar label eventually or there is the element of same or like function.Below by ginseng
The embodiment for examining accompanying drawing description is exemplary, is only used for explaining the utility model, and it is not intended that to of the present utility model
Limitation.
In description of the present utility model, it is to be understood that term " " center ", " longitudinal direction ", " length ", " on ", " under ",
The orientation or position relationship of the instruction such as " preceding ", " level ", " interior ", " outer ", " axial direction " are based on orientation shown in the drawings or position
Relation, it is for only for ease of description the utility model and simplifies description, rather than indicates or imply that signified device or element must
There must be specific orientation, with specific azimuth configuration and operation, therefore it is not intended that to limitation of the present utility model.This
Outside, " first " is defined, one or more this feature can be expressed or be implicitly included to the feature of " second ".In this reality
With in new description, unless otherwise indicated, " multiple " are meant that two or more.
Pyrolytic reaction device 100 below with reference to Fig. 1-Fig. 2 descriptions according to the utility model embodiment.
As Figure 1-Figure 2, the He of first charging aperture 1 is had according to the pyrolytic reaction device 100 of the utility model embodiment
Second charging aperture 2, pyrolytic reaction device 100 include：It is pyrolyzed body of heater 3, heating tube 4 and hydrid component 5.
Specifically, first charging aperture 1 is located on pyrolysis body of heater 3, and heating tube 4 is extend into pyrolysis body of heater 3 with to pyrolysis
Material in body of heater 3 provides pyrolysis heat.It follows that after material is entered in pyrolysis body of heater 3 by first charging aperture 1, heat
Heating tube 4 in solution body of heater 3 provides heat so that material is sufficiently pyrolyzed in pyrolysis body of heater 3 for material, and material is pyrolyzed
The solid product of oil gas and high temperature is formed afterwards.It is understood that pyrolysis body of heater 3 is provided with oil gas vent 12 so that material to be pyrolyzed
Caused oil gas quickly exports afterwards, so as to avoid tar that second pyrolysis occurs, improves the yield of pyrolytic tar.And high temperature
Solid product is stayed in pyrolysis body of heater 3.
Hydrid component 5 includes multiple mixing bodies of heater 51 and multiple agitators 52, and each body of heater 51 that mixes is located at pyrolysis body of heater 3
Lower section and connected with pyrolysis body of heater 3, each body of heater 51 that mixes is provided with discharging opening 6, multiple agitators 52 and multiple holding furnaces
Body 51, which corresponds, to be set, and each agitator 52 includes the agitating shaft 521 extending into mixing body of heater 51, and second charging aperture 2 is set
On pyrolysis body of heater 3 or mixing body of heater 51, second charging aperture 2 is between heating tube 4 and agitating shaft 521, each agitating shaft
521 rotate to mix the material being drained into from pyrolysis body of heater 3 and second charging aperture 2 in corresponding mixing body of heater 51.It follows that
It is multiple mixing bodies of heater 51 setting can also avoid to a certain extent pyrolysis body of heater 3 with mix the junction of body of heater 51 material and
The generation for the problem of solid product is accumulated and blocks pyrolytic reaction device 100, improve the reliability of pyrolytic reaction device 100.
The solid product of caused high temperature is drained into multiple mixed along pyrolysis body of heater 3 after material pyrolysis in pyrolysis body of heater 3
Material stirring in corresponding agitating shaft 521 after closing in body of heater 51 with being entered from second charging aperture 2 in multiple mixing bodies of heater 51
Dynamic lower mixing, think so as to which the solid product for the high temperature being drained into each mixing body of heater 51 discharges itself sensible heat from the second charging
The materials that mouth 2 is entered in corresponding each mixing body of heater 51 provide heats so that enter multiple mixing from second charging aperture 2
Material in body of heater 51 absorbs heat in multiple mixing bodies of heater 51 and is pyrolyzed, the solid product formed after pyrolysis and release
Solid product after itself sensible heat discharges pyrolytic reaction device 100 from the discharging opening 6 on multiple mixing bodies of heater 51.It is hereby understood that
Without external heat source in each mixing body of heater 51 of pyrolytic reaction device 100, fully produced using being pyrolyzed in body of heater 3 after material pyrolysis
The solid product of the raw high temperature sensible heat of itself, so as to significantly reduce the energy consumption of system, improve the yield of pyrolytic tar.
Meanwhile the structure of pyrolytic reaction device 100 is simple, floor space can be reduced to a certain extent, be easy to industrialize.
According to the pyrolytic reaction device 100 of the utility model embodiment, by setting hydrid component 5, so as to abundant
The sensible heat of the solid product itself of caused high temperature after ground is pyrolyzed using material in pyrolysis oven body 3, it is effectively reduced the energy of system
Consumption, improve the yield of reliability and pyrolytic tar.It is simultaneously simple in construction, floor space can be reduced to a certain extent, be easy to
Industrialization.
According to some embodiments of the utility model, mixing body of heater 51 is two, and second charging aperture 2 is one and is being pyrolyzed
On body of heater 3.So that the structure of pyrolytic reaction device 100 is simple, it is easily manufactured.The position of second charging aperture 2 is provided with simultaneously
Mixed beneficial to enabling the solid product of the high temperature of discharge out of pyrolysis body of heater 3 to be equably drained into two in bodies of heater 51, and then
Improve the operating efficiency of pyrolytic reaction device 100.
Alternatively, agitator 52 also includes motor 522, and motor 522 coordinates with agitating shaft 521 to drive 521 turns of agitating shaft
It is dynamic.When the velocity of rotation of motor 522 is in 20r/min-30r/min, can ensure agitator 52 to from pyrolysis body of heater 3 and second
Charging aperture 2 is drained into the mixed effect of the material in each mixing body of heater 51.Preferably, the velocity of rotation of motor 522 is
24.5r/min-28.7r/min。
According to some embodiments of the utility model, agitating shaft 521 includes axis body 521a and multiple blade 521b, Mei Geye
It is enclosed on outside piece 521b on axis body 521a, axially spaced-aparts of multiple blade 521b along axis body 521a is located on axis body 521a.Thus may be used
Know, the structure of agitating shaft 521 is simple, while advantageously ensures that the rotation of agitating shaft 521 to from pyrolysis body of heater 3 and second charging aperture
2 are drained into the mixed effect of the material in mixing body of heater 51, make to fill from the material that second charging aperture 2 is drained into mixing body of heater 51
Divide the sensible heat of the solid product of high temperature of the ground using being drained into out of pyrolysis body of heater 3 in mixing body of heater 51, and then raising pyrolysis is anti-
Answer the yield of the pyrolytic tar of device 100.
Further, the cross section for mixing body of heater 51 is formed as circular, when each blade 521b diameter mixes with corresponding
The ratio between the diameter of the internal perisporium of body of heater 51 is closed when be 0.3-0.5, is advantageous to mix solid product in body of heater 51 from mixing
The gap closed between body of heater 51 and agitator 52 is moved to discharging opening 6 to discharge pyrolytic reaction device 100, is from second charging aperture
2 materials being drained into mixing body of heater 51 provide the space of pyrolysis, so as to ensure that heat in mixing body of heater 51 to a certain extent
The yield of tar is solved, and then improves the whole work efficiency of pyrolytic reaction device 100.Preferably, each blade 521b diameter
Ratio between the diameter for the internal perisporium for mixing body of heater 51 is 0.32-0.46.
Specifically, when the ratio of length of the length of agitating shaft 521 with mixing body of heater 51 is 0.5-0.7, can enter to protect
The mixed effect for the material being drained into from pyrolysis body of heater 3 and second charging aperture 2 in mixing body of heater 51 is demonstrate,proved, and then ensures mixing body of heater
The yield of pyrolytic tar in 51.Further, the ratio of length of the length of agitating shaft 521 with mixing body of heater 51 is 0.56-
0.65。
Specifically, when it is each mixing body of heater 51 first longitudinal direction central axis and horizontal plane between angle be 10 ° -20 °,
The second longitudinal direction central axis upright of body of heater 3 is pyrolyzed when horizontal plane, the height in pyrolysis body of heater 3 can be controlled to a certain extent
The speed that the solid product in speed and mixing body of heater 51 that the solid product of temperature is drained into mixing body of heater 51 is discharged from discharging opening 6
Degree, is pyrolyzed the material in pyrolytic reaction device 100 more abundant.It can control and be fed from pyrolysis body of heater 3 and second simultaneously
Mouth 2 is drained into the quantity of the material in mixing body of heater 51, makes the filling rate of material in mixing body of heater 51 between 50%~65%,
So as to provide effective space for the discharge of caused oil gas after material pyrolysis in mixing body of heater 51, and then improve pyrolysis
The yield of the pyrolytic tar of reaction unit 100.Further, between the first longitudinal direction central axis and horizontal plane that mix body of heater 51
Angle be 11.4 ° -19.2 °.
According to some embodiments of the utility model, the center of rotation axis of agitating shaft 521 and corresponding mixing body of heater 51
First longitudinal direction centerline axis parallel.So that the material that pyrolysis body of heater 3 and second charging aperture 2 are drained into mixing body of heater 51 mixes
Close more uniformly, and then make from second charging aperture 2 be drained into mixing body of heater 51 in material be pyrolyzed it is more abundant.It is preferred that
Ground, the center of rotation axis of agitating shaft 521 overlap with the first longitudinal direction central axis of corresponding mixing body of heater 51.
Alternatively, pyrolytic reaction device 100 can also include two feed screws 7, and two feed screws 7 are set respectively
At first charging aperture 1 and second charging aperture 2.Enter it follows that extraneous material is delivered to first by two feed screws 7
Material mouth 1 and second charging aperture 2, consequently facilitating the charging of material.
Alternatively, pyrolytic reaction device 100 can also include multiple conveying worms 8, multiple conveying worms 8 with it is multiple
Mix body of heater 51 and correspond setting, conveying worm 8 is located at the discharging opening 6 on mixing body of heater 51.So as to discharge
Solid product at mouth 6 is delivered to the outside of pyrolytic reaction device 100, avoids solid product to a certain extent in discharging opening 6
Accumulate and block discharging opening 6.
Alternatively, the internal perisporium for mixing body of heater 51 is provided with thermal insulating material materials and parts.So as to be advantageous to avoid from the pyrolysis row of body of heater 3
The internal perisporium entered to heat from the mixing body of heater 51 of the solid product of the high temperature in mixing body of heater 51 outwards sheds, and then improves
The heat insulation effect of body of heater 51 is mixed, the efficiency of the pyrolytic tar of material in mixing body of heater 51 can be improved to a certain extent.
Alternatively, heating tube 4 is heat accumulation type radiant tube.So that the thermal efficiency of heating tube 4 is high, stable, reliability
It is high.It is understood that when heating tube 4 is heat accumulation type radiant tube, it is pyrolyzed on body of heater 3 and is additionally provided with fuel gas inlet 9, air intlet
10 and exhanst gas outlet 11, the thermal efficiency and reliability in heat accumulation type radiant tube are thereby may be ensured that, and then ensure heating tube 4 for heat
Material in solution body of heater 3 provides sufficient heat to be pyrolyzed.The temperature of the wherein tube wall of heat accumulation type radiant tube is adjusted by combustion gas
(not shown) control of valve.
Alternatively, oil gas vent 12 is multiple that multiple oil gas vents 12 are in the side of pyrolysis body of heater 3 and multiple mixing bodies of heater 51
It is spaced apart on wall.So as to improve the efficiency that oil gas vent 12 exports oil gas, tar is more efficiently avoided to occur secondary
Cracking, improve the yield of pyrolytic tar.Preferably, multiple external oil-gas pipelines (not shown) of oil gas vent 12, multiple oil gas
Oil gas is oriented to same oil gas general export (not shown) by pipeline.So that the structure of pyrolytic reaction device 100 is simple, work
Efficiency high.
Specifically, when the length ratio between pyrolysis body of heater 3 and each mixing body of heater 51 is 1:1-3:When 1, thing can be ensured
Material stops that 6s-9s is more abundant to be pyrolyzed from top to bottom in pyrolysis body of heater 3, and then improves the heat of pyrolytic reaction device 100
The efficiency of tar is solved, while reduces the energy consumption of system to a certain extent.
According to the method for pyrolysis of the pyrolytic reaction device 100 of the utility model embodiment, pyrolytic reaction device is according to this
The pyrolytic reaction device 100 of utility model above-described embodiment, method for pyrolysis comprises the following steps：
S1：Material is delivered in pyrolysis body of heater 3 by first charging aperture 1, control heating tube 4 works with to being pyrolyzed body of heater
Material in 3 provides pyrolysis heat.So that the material entered from first charging aperture 1 in pyrolysis body of heater 3 can be in pyrolysis oven
Sufficiently it is pyrolyzed in body 3, ultimately forms the solid product of oil gas and high temperature.
S2：Material is delivered in multiple mixing bodies of heater 51 by second charging aperture 2 after the scheduled time, control is each stirred
Axle 521 is mixed to rotate to mix the material being drained into from pyrolysis body of heater 3 and second charging aperture 2 in each mixing body of heater 51.So that
The solid product for the high temperature being drained into from pyrolysis body of heater 3 in each mixing body of heater 51 discharges itself sensible heat and thought from second charging aperture
2 materials entered in corresponding each mixing body of heater 51 provide heat so that enter multiple holding furnaces from second charging aperture 2
Material in body 51 absorbs heat in multiple mixing bodies of heater 51 and is pyrolyzed.
S3：Material after pyrolysis discharges pyrolytic reaction device 100 by the discharging opening 3 on each mixing body of heater 51.Thus
Understand, the solid product that is formed after pyrolysis and discharge the solid product after itself sensible heat from the discharging openings on multiple mixing bodies of heater 51
6 discharge pyrolytic reaction devices 100.
According to the method for pyrolysis of the pyrolytic reaction device 100 of the utility model embodiment, pyrolysis oven can be fully utilized
The sensible heat of the solid product itself of caused high temperature, the system for being effectively reduced pyrolytic reaction device 100 after material is pyrolyzed in body 3
Energy consumption, improve the yield of pyrolytic tar.
Structure below with reference to Fig. 1-Fig. 2 to the pyrolytic reaction device 100 according to one specific embodiment of the utility model
It is described in detail.It should be understood that following explanations only have it is exemplary, those of ordinary skill is reading this reality
After new following technical proposals, it is clear that can to technical scheme therein either some technical characteristics be combined or
Replace, modification, this is also fallen within the protection domain required by the utility model.
As Figure 1-Figure 2, first charging aperture 1, the are had according to the pyrolytic reaction device 100 of the utility model embodiment
Two charging apertures 2, discharging opening 6, fuel gas inlet 9, air intlet 10, exhanst gas outlet 11 and oil gas vent 12.Pyrolytic reaction device 100
Also include：It is pyrolyzed body of heater 3, heating tube 4, hydrid component 5, feed screw 7 and conveying worm 8.
Specifically, first charging aperture 1 and second charging aperture 2 are each provided on pyrolysis body of heater 3.Feed screw 7 is two
And it is respectively provided at first charging aperture 1 and second charging aperture 2.Heating tube 4 is extend into pyrolysis body of heater 3 with pyrolysis body of heater 3
Material provide pyrolysis heat.Heating tube 4 is heat accumulation type radiant tube, and the temperature of the tube wall of heating tube 4 passes through gas control valve control
System is at 900 DEG C -1000 DEG C.
Hydrid component 5 includes two cross sections for circular mixing body of heater 51 and two agitators 52.Two mixing bodies of heater
51 and two agitators 52 correspond and set.
Each mixing body of heater 51 is located at the lower section of pyrolysis body of heater 3 and connected with pyrolysis body of heater 3, and each mix sets on body of heater 51
There is a discharging opening 6, a conveying worm 8 is provided with each discharging opening 6.The internal perisporium of each mixing body of heater 51, which is provided with, to be protected
Adiabator part.The length ratio being pyrolyzed between body of heater 3 and each mixing body of heater 51 is 1.2:1.It is pyrolyzed the second longitudinal direction center of body of heater 3
Angle of the axis between horizontal plane, each first longitudinal direction central axis and horizontal plane for mixing body of heater 51 is 20 °, so as to
Two mixing bodies of heater 51 form inverted V-shaped.
Agitator 52 includes the agitating shaft 521 extending into corresponding mixing body of heater 51 and coordinated with agitating shaft 521 to drive
The motor 522 that dynamic agitating shaft 521 rotates, the velocity of rotation of motor 522 is 25r/min.Second charging aperture 2 is located at the He of heating tube 4
Between two agitating shafts 521.
The length of agitating shaft 521 is 0.6 with the ratio of the length of corresponding mixing body of heater 51, the rotation of each agitating shaft 521
The first longitudinal direction central axis for turning central axis with corresponding mixing body of heater 51 overlaps.Agitating shaft 521 includes axis body 521a and more
It is enclosed on axis body 521a on outside individual blade 521b, each blade 521b to drive rotation by axis body 521a, multiple blade 521b are along axle
Body 521a axially spaced-apart is located on axis body 521a.The diameter of internal perisporium of each blade 521b diameter with mixing body of heater 51 it
Between ratio be 0.45.Motor 522 drive agitating shaft 521 rotate with mix from pyrolysis body of heater 3 and second charging aperture 2 be drained into it is mixed
Close the material in body of heater 51.
Using the pyrolytic reaction device 100 of the utility model embodiment to Indonesia's lignite (coal analysis such as table 1) and Wen Jia
Beam length flame coal (coal analysis such as table 2) is pyrolyzed, wherein the material entered from first charging aperture 1 in pyrolysis body of heater 3 is print
Buddhist nun's lignite, two materials mixed in body of heater 51 is drained into as the good beam length flame coal of temperature from second charging aperture 2, the heat obtained after pyrolysis
The yield distribution for solving tar is as shown in table 3.
Table 1：Indonesia's Brown Coal analysis
Table 2：The good beam length flame coal coal coal analysis of temperature
Table 3：Indonesia's lignite and Wen Jia beam lengths flame coal pyrolysis yield distribution
From table 3 it can be seen that make Indonesia's lignite pyrolysis in the pyrolysis body of heater 3 of pyrolytic reaction device 100, in two mixing
It is pyrolyzed warm family's beam length flame coal in body of heater 51, thermal decomposition product tar yield is up to 8.2%, is the 96.5% of aluminium rice steamer oil content, is
System energy consumption reduces 10-25%.
It is common for this area according to other compositions of the pyrolytic reaction device 100 of the utility model embodiment and operation
All it is known for technical staff, is not detailed herein.
In the description of this specification, reference term " one embodiment ", " some embodiments ", " illustrative examples ",
The description of " example ", " specific example " or " some examples " etc. means to combine specific features, the knot that the embodiment or example describe
Structure, material or feature are contained at least one embodiment or example of the present utility model.In this manual, to above-mentioned art
The schematic representation of language is not necessarily referring to identical embodiment or example.Moreover, description specific features, structure, material or
Person's feature can combine in an appropriate manner in any one or more embodiments or example.
While there has been shown and described that embodiment of the present utility model, it will be understood by those skilled in the art that：
These embodiments can be carried out with a variety of changes, modification in the case where not departing from principle and objective of the present utility model, replaced
And modification, the scope of the utility model are limited by claim and its equivalent.
Claims (9)
- A kind of 1. pyrolytic reaction device, it is characterised in that the pyrolytic reaction device has first charging aperture and second charging aperture, The pyrolytic reaction device includes：Body of heater is pyrolyzed, the first charging aperture is located on the pyrolysis body of heater；Heating tube, the heating tube are extend into the pyrolysis oven body to provide the material in the pyrolysis oven body pyrolysis heat Amount；Hydrid component, the hydrid component include multiple mixing bodies of heater and multiple agitators, and each mixing body of heater is located at institute State the lower section of pyrolysis body of heater and connected with the pyrolysis body of heater, each mixing body of heater is provided with discharging opening, the multiple stirring Device and the multiple mixing body of heater are corresponded and set, and each agitator includes extending into the corresponding holding furnace body Agitating shaft, the second charging aperture be located at it is described pyrolysis body of heater or it is described mixing body of heater on, the second charging aperture is located at Between the heating tube and the agitating shaft, each agitating shaft is rotated to mix from the pyrolysis body of heater and described second Material mouth is drained into the material in the corresponding holding furnace body.
- 2. pyrolytic reaction device according to claim 1, it is characterised in that the body of heater that mixes is two, described second Charging aperture is one and on the pyrolysis body of heater.
- 3. pyrolytic reaction device according to claim 1, it is characterised in that the agitating shaft includes axis body and multiple leaves Piece, each blade are enclosed on the axis body outside, and axially spaced-apart of the multiple blade along the axis body is located at the axis body On.
- 4. pyrolytic reaction device according to claim 3, it is characterised in that the cross section of the mixing body of heater is formed as round Shape, the ratio between the diameter of each blade and the diameter of the internal perisporium of the corresponding mixing body of heater is 0.3-0.5.
- 5. pyrolytic reaction device according to claim 1, it is characterised in that the length of the agitating shaft with it is corresponding described The ratio for mixing the length of body of heater is 0.5-0.7.
- 6. pyrolytic reaction device according to claim 1, it is characterised in that in the first longitudinal direction of each mixing body of heater Angle between mandrel line and horizontal plane is 10 ° -20 °, and the second longitudinal direction central axis upright of the pyrolysis body of heater is in the water Plane.
- 7. pyrolytic reaction device according to claim 1, it is characterised in that the center of rotation axis of the agitating shaft and phase The first longitudinal direction centerline axis parallel for the mixing body of heater answered.
- 8. pyrolytic reaction device according to claim 1, it is characterised in that set on the internal perisporium of each mixing body of heater There are thermal insulating material materials and parts.
- 9. the pyrolytic reaction device according to any one of claim 1-8, it is characterised in that the pyrolysis body of heater and each Length ratio between the mixing body of heater is 1:1—3:1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720754750.7U CN207121568U (en) | 2017-06-26 | 2017-06-26 | pyrolytic reaction device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720754750.7U CN207121568U (en) | 2017-06-26 | 2017-06-26 | pyrolytic reaction device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207121568U true CN207121568U (en) | 2018-03-20 |
Family
ID=61615662
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720754750.7U Active CN207121568U (en) | 2017-06-26 | 2017-06-26 | pyrolytic reaction device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207121568U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107267171A (en) * | 2017-06-26 | 2017-10-20 | 北京神雾电力科技有限公司 | Pyrolytic reaction device and its method for pyrolysis |
-
2017
- 2017-06-26 CN CN201720754750.7U patent/CN207121568U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107267171A (en) * | 2017-06-26 | 2017-10-20 | 北京神雾电力科技有限公司 | Pyrolytic reaction device and its method for pyrolysis |
| CN107267171B (en) * | 2017-06-26 | 2024-04-12 | 北京恒丰亚业科技发展有限公司 | Pyrolysis reaction device and pyrolysis method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104946279B (en) | Swinging heat stepwise biomass continuous pyrolysis equipment | |
| CN103842101B (en) | Reciprocating reactor and methods for thermal decomposition of carbonaceous feedstock | |
| CN206385084U (en) | A kind of continous way charging and solid and gas are automatically separated the carbonizing plant of reduction and gaseous charcoal processed | |
| CN204485863U (en) | A kind of two-way stirring formula heating reactor | |
| CN104031668B (en) | A kind of method and apparatus of oil shale comprehensive utilization | |
| CN104312602B (en) | Continuous carbonization furnace for waste wood chips | |
| CN207121568U (en) | pyrolytic reaction device | |
| CN201334633Y (en) | Asphalt modifying equipment using rubber powder | |
| CN207121563U (en) | Pyrolysis reactor furnace | |
| CN207121569U (en) | Pyrolysis reactor | |
| CN205328955U (en) | End gasifier is changeed to annular | |
| CN103773404B (en) | A kind of Combined type multiplex produces material fast charring equipment and its carbonizing method | |
| CN111675214A (en) | Preparation system of palm-based artificial graphite | |
| CN201697447U (en) | Calcining device of nano-grade WO3/TiO2 functional materials | |
| CN107267171A (en) | Pyrolytic reaction device and its method for pyrolysis | |
| CN206887021U (en) | Pyrolysis coupling electricity generation system | |
| CN206597482U (en) | A kind of raw material temperature control type dissolution equipment of composite heat transfer | |
| CN206887020U (en) | It is pyrolyzed generating means | |
| CN205505620U (en) | High moisture dry material device with single spiral feeding device | |
| CN205856406U (en) | Sawdust high-temperature gasification stove | |
| CN209685690U (en) | A kind of stacked pyrolysis reaction device of high thermal conversion rate | |
| CN104087316B (en) | Rotating bed dry distillation furnace | |
| CN113817580A (en) | Partitioned stirring dry type anaerobic fermentation system | |
| CN1749222A (en) | Heating mixer for producing granular compound fertilizer | |
| CN107163988A (en) | The gasification installation of calorific value biological mass combustable gas in preparation |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20201123 Address after: 102209 226, 2nd floor, building 71, 30 Litang Road, Changping District, Beijing Patentee after: Beijing Hengfeng Yaye Technology Development Co., Ltd Address before: 102200 Beijing city Changping District Machi Town kamis Road No. 18 building 201 room 2 Patentee before: BEIJING SHENWU POWER TECHNOLOGY Co.,Ltd. |
|
| TR01 | Transfer of patent right |