CN207699525U - A kind of preparation facilities of carbon-rich solids cleaning products - Google Patents
A kind of preparation facilities of carbon-rich solids cleaning products Download PDFInfo
- Publication number
- CN207699525U CN207699525U CN201721250867.8U CN201721250867U CN207699525U CN 207699525 U CN207699525 U CN 207699525U CN 201721250867 U CN201721250867 U CN 201721250867U CN 207699525 U CN207699525 U CN 207699525U
- Authority
- CN
- China
- Prior art keywords
- board components
- gas distribution
- main channel
- air inlet
- carbon
- 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
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
A kind of preparation facilities of carbon-rich solids cleaning products, including the first on-board components, the second on-board components and the third on-board components that are from top to bottom successively set in vertical cavity；Material-feeding port is arranged in the top of first on-board components, and the lower section of third on-board components connects discharge channel；First on-board components include main channel and the multiple subaisles vertical with main channel and arranged side by side being embedded on main channel；Main channel and the head of subaisle are flaring type；Main channel head is equipped with multiple drainage tubes；Second on-board components include flaring type head and the upstanding sidewall for offering vent cap, and exhaust eye, the bottom-open of the second on-board components are offered on upstanding sidewall；Third on-board components include a plurality of arch gas distribution wall and the multiple tricuspid gas distribution walls vertical with arch gas distribution wall and arranged side by side being embedded on arch gas distribution wall；Arch gas distribution wall is equipped with air inlet eyelet with tricuspid gas distribution wall, and the utility model can make up the non-uniform problem of small particle coal hot-working gas distribution.
Description
Technical field
The utility model is related to coal sub-prime clean utilization fields, and in particular to a kind of preparation of carbon-rich solids cleaning products
Device.
Background technology
China is the country of a rich coal, oil-poor, few gas, and coal occupies the leading position of China's energy.As China passes through
Ji continues to develop, and in recent years because largely causing national big city haze serious using fossil energy, therefore develops cleaning, efficiently profit
Seem rather important with the project of coal resources.According to country《Energy development " 13 " is planned》With《Coal process deeply industry
Demonstration " 13 " planning》Related psychotic clearly proposes the low-order coal sub-prime clean utilization technology of clean and effective to be researched and developed.
Coal sub-prime clean utilization is one of the important channel of coal deep processing and utilization, refers to that coal is completely cutting off air or indifferent gas
Hot-working under the conditions of atmosphere generates the process of the products such as carbon-rich solids product, hydrocarbon mixture liquid, gas.Not by heating final temperature
Together, three kinds can be divided into：900~1100 DEG C are high-temperature heating, that is, are carbonized；700~900 DEG C are heated for medium temperature；500~600 DEG C are
Low-temperature heat.Coal is cleaned has coal liquifaction, natural gas from coal, coal-to-olefin, coal aromatic hydrocarbons, coal sub-prime the skills such as to utilize using technology
Art.
Domestic coal prepares cleaning solid product, mainly coal production of shaped coal, that is, utilizes the active principle in binder firing
Burning process reacts with the sulphur in coal generates other compounds progress desulfurization, and others also have coal sub-prime solid product.Closely
Coal sub-prime is developed swift and violent using technology over year, the technology developed at present have it is ten several, but the safety from operation, stability,
Long periodicity considers that master to be applied is internal thermal upright stove, which runs more ripe for lump coal.
The insufficient predicament of lump coal is brought for mechanical coal mining, upright furnace adaptation mixed coal sub-prime is promoted by developing new technology
Utilizing status is meaningful, in existing coal device for heat treating the inner member used such as patent CN201574140U that has announced and
CN1966611A, in the getter component of existing coal device for heat treating, there are a fixed gaps between two adjacent pair umbrellas, therefore can not will
Hydrocarbon mixture gas more comprehensively, largely exports, and reduces the product yield of by-product liquid, while can cause coal gas and hydrocarbon mixture
Class gas rises to the top of the vertical cavity of upright furnace, and the air that these gases are come in feed supplement storehouse, which meets, to be easy to catch fire, and occurs
Accident；In addition coal gas and hydrocarbon mixture gas can enter distribution cabins through material-feeding port, are finally discharged in air and cause seriously to pollute；Coal
Hot procedure causes gas distribution uneven because of poor air permeability, and association situation occurs, causes the cleannes of carbon-rich solids product not
It is high.
Utility model content
The problems in the purpose of this utility model is that for the above-mentioned prior art, a kind of carbon-rich solids cleaning products are provided
Preparation facilities, getter efficiency can be improved, heat source gas is made to be uniformly distributed, obtained carbon-rich solids product cleannes are higher.
To achieve the goals above, the technical solution adopted in the utility model is：
Including built in the first on-board components, the second on-board components and third that are from top to bottom successively set in vertical cavity
Component；Material-feeding port is arranged in the top of first on-board components, and the lower section of the third on-board components connects discharge channel；First
On-board components include horizontally disposed main channel and the multiple subaisles vertical with main channel and arranged side by side being embedded on main channel；
Main channel and the head of subaisle are flaring type；It is provided with multiple drainage tubes on the flaring type head of main channel；Built in second
Component is at least arranged side by side two layers in vertical cavity, and each second on-board components include offering vent cap gradually
Expansion type head and the upstanding sidewall for being connected to flaring type lower head offer several exhausts on the upstanding sidewall
Eye；Second on-board components interval of same layer is arranged, the second on-board components mutual dislocation of adjacent layer；The bottom of second on-board components
Portion is opened wide；Third on-board components include horizontally disposed a plurality of arch gas distribution wall and vertical with arch gas distribution wall and inlay side by side
Multiple tricuspid gas distribution walls on arch gas distribution wall；If being provided with dried layer air inlet brick on arch gas distribution wall and tricuspid gas distribution wall, into
Air inlet eyelet is provided on gas brick.
The flaring type head of the main channel, subaisle and the second on-board components uses circular arc type or tip.
The main channel and the flaring type head of subaisle use tip, and the tip head of main channel is opened by the first triangle
Orifice plate is welded, and the tip head of subaisle is welded by the second triangle perforated panel.
Multiple oblique side walls of the subaisle flaring type head connected symmetrical dendrimer setting, oblique side wall are set as 5 layers.
It is connected by arc side plate transition between the flaring type head and upstanding sidewall of second on-board components.
The drainage tube uses up big and down small cylinder.
The exhaust eye size opened up on the upstanding sidewall of second on-board components is identical.
The air inlet eyelet connects the air inlet port being arranged to air inlet brick inner inclination, the internal diameter flaring of air inlet port or
Person is tapered.
The exhaust eye uses trapezoidal, triangle or square structure.
Second on-board components are provided at both ends with third triangle perforated panel.
Compared with prior art, the utility model has following advantageous effect：First on-board components are mainly used for collecting
The hydrocarbon mixture gas and coal gas generated in coal hot procedure, existing coal hot-working hydrocarbon mixture gas and coal-gas recovering
Device organic efficiency is relatively low, is on the one hand easy to gather hydrocarbon mixture gas and coal gas, hydrocarbon mixture gas in vertical cavity top plate portion
The air that body and coal gas are come in material-feeding port easily occur Ignition Phenomena, another aspect hydrocarbon mixture gas and coal gas through material-feeding port into
Entering coal bunker and discharges into the atmosphere and can pollute, the subaisle structure of the utility model can improve hydrocarbon mixture gas recovery rate,
The phenomenon that avoiding vertical cavity top plate from catching fire can additionally prevent hydrocarbon mixture gas and coal gas and enter coal bunker again by material-feeding port
It is discharged into air and pollutes.Several layers of the second on-board components are shifted to install in coal hot-working warm-up phase, the second on-board components
Effect is to collect hydrocarbon mixture gas and dominate heat source gas, while also also functioning to cloth effect to coal, is moved past under coal grain
There is perturbation action to coal grain in journey, play the role of loose coal seam, has the function of gas permeability between increase coal seam, structure built in second
Coal seam is split support by part, and stress is divided between making the coal seam in the neighbouring region of the second on-board components, mitigates top coal
Layer is alleviated and squeezes gap between coal grain, increase gas permeability to the actuating pressure of underlying seam.In other second on-board components
Portion can form low pressure empty region, cause to form pressure difference with adjacent same level position coal seam, gather heat source gas and hydrocarbon mixture gas
Body.Existing vertical cavity device for heat treating, bed coal seam is thicker and also coal seam be it is whole move down, between coal grain almost without
Perturbation action is particularly suitable for the coal hot-working of small particle.The arch gas distribution wall of the utility model third on-board components carries out two
Secondary gas distribution, and form cross with tricuspid gas distribution wall and be staggered, it is uneven to make up small particle coal hot-working gas distribution in this way, ensures to obtain
Obtain the carbon-rich solids cleaning products of higher quality.
Further, the drainage tube of the utility model uses up big and down small cylinder, can reduce gas flow rate, make air-flow
In solid particle obtain natural subsidence, effectively reduce in hydrocarbon mixture gas band dirt problem.
Further, pass through arc between the flaring type head and the second upstanding sidewall of the second on-board components of the utility model
Side plate transition connects, and arc side plate advantageously reduces energy loss in heat source gas uphill process.
Description of the drawings
The overall structure diagram of Fig. 1 the utility model；
The structural schematic diagram of the first on-board components of Fig. 2 the utility model；
The structural schematic diagram of the second on-board components of Fig. 3 the utility model；
The structural schematic diagram of Fig. 4 the utility model third on-board components.
In attached drawing：The first on-board components of 1-；The second on-board components of 2-；3- third on-board components；The main channels 101-；102- pairs
Channel；103- drainage tubes；The oblique side walls of 104-；105- the first triangle perforated panels；106- the second triangle perforated panels；The vertical chambers of 107-
Body；The first upstanding sidewalls of 108-；201- vent caps；202- area of space；203- is vented eye；204- arc side plates；205-
Three triangle perforated panels；The second upstanding sidewalls of 206-；301- arch gas distribution walls；302- tricuspid gas distribution walls；303- air inlet eyelets.
Specific implementation mode
The following describes the utility model in further detail with reference to the accompanying drawings.
Embodiment 1
Referring to Fig. 1-4, the utility model, which is directed to, is applied to grain size in 30mm mixed coals below, and grain size is more in 15mm or more
When, which includes vertical cavity 107, and vertical cavity 107 is connected component, is from top to bottom followed successively by material-feeding port, structure built in first
Part 1, the second on-board components 2, third on-board components 3 and discharge channel；107 bottom of vertical cavity is provided with third on-board components
3, tricuspid gas distribution wall 302 is provided in third on-board components 3, and tricuspid gas distribution wall 302 is set as several, 302 side of tricuspid gas distribution wall
The air inlet eyelet 303 that haves three layers is arranged in wall, by air inlet eyelet 303 by fuel gas and air delivery to air inlet eyelet 303, sends out
So that coal is reached 650 DEG C -700 DEG C after raw internal combustion and hot-working decomposition occurs, discharge channel is arranged in 303 lower section of tricuspid gas distribution wall.
Arch gas distribution wall 301 is additionally provided in third on-board components 3, the setting of arch gas distribution wall 301 at least 2 is being encircleed
301 side wall of shape gas distribution wall is provided with 2 layers of air inlet eyelet 303, by air inlet eyelet 303 by fuel gas and air delivery to air inlet
In eyelet 303, coal is set to reach 650 DEG C of -700 DEG C of generation hot-working decomposition, the hydrocarbon mixture gas that hot-working generates after internal combustion occurs
Body and heat source gas gradually rise up at the second on-board components 2, finally rise to 1 lower port of the first on-board components through drainage tube
The 103 vertical cavitys 107 of discharge, in the first on-board components 1 setting of drainage tube 103 become larger from bottom to top.Tricuspid gas distribution wall
302 and arch gas distribution wall 301 in be respectively provided with air inlet eyelet 303, aperture is gradual from inside to outside for the air inlet port of air inlet eyelet 303
Become larger.
1 layer of second on-board components 2 is arranged in 107 middle part of vertical cavity, and multiple, structure built in second is arranged in the second on-board components 2
Setting exhaust eye 203 on second upstanding sidewall 206, air passage may be configured as square hole, trapezoidal hole or tri-angle-holed etc. in part 2.
107 inner top of vertical cavity is provided with material-feeding port, and vertical cavity 107 is internally provided with the first on-board components 1, second
On-board components 2, third on-board components 3 and discharge channel.
First on-board components, 1 structure includes main channel 101, subaisle 102, drainage tube 103, the first triangle perforated panel 105
And the second triangle perforated panel 106；Main channel 101 by the combination of side wall 108 that flaring type head and two vertical directions are arranged and
At, mouth down, from top to bottom acute angle mouth becomes larger；Drainage tube 103 and the acute angle shape top being set on main channel 101 connect
Connect, drainage tube 103 from bottom to top becomes larger, subaisle 102 by a flaring type head and several oblique side walls 104 combination and
At it is 5 layers that oblique side wall 104, which is symmetrical arranged,；Several is arranged with main channel 101 for subaisle 102 and vertical inlay is welded.
Second on-board components 2 are by flaring type head, two curved walls, 204, two the second upstanding sidewalls 206 and two
Third triangle perforated panel 205 is composed, the mouth down on flaring type head, and opening from top to bottom becomes larger and two curved sides
Plate 204 welds, and two arc side plates 204 and two the second upstanding sidewalls 206 weld.The open at its lower end of second on-board components 2.
Third on-board components 3 include tricuspid gas distribution wall 302, arch gas distribution wall 301 and air inlet brick, tricuspid gas distribution wall 302
Side wall wall be provided with air inlet brick, air inlet brick is provided with air inlet eyelet 303, in third on-board components 3 air inlet eyelet 303 with it is external
Vent line is connected to, and arch gas distribution wall 301 and 302 cross of tricuspid gas distribution wall are staggered setting, and arch gas distribution wall 301 is provided with air inlet
Eyelet 303, arch gas distribution wall 301 are communicated with 302 air flue of tricuspid gas distribution wall.Air inlet eyelet 303 is obliquely installed, air inlet eyelet
303 and the angle of horizontal plane are 35 ° -55 °, and the cross sectional shape of air inlet eyelet 303 is ellipse.
The technological process that carbon-rich solids cleaning products are prepared using the utility model mixed coal is as follows：
Mixed coal enters vertical cavity 107 by material-feeding port, by the first on-board components 1, subsequently into the second on-board components 2,
It is divided in the mixed coal that the second on-board components 2 move down, the second on-board components 2 play disturbance effect to coal grain, there is loose mixed coal grain
Effect, is supported part coal seam using the second on-board components 2, reduces the pressure to 2 lower section coal seam of the second on-board components, while energy
Perturbation action is played to mixed coal grain, finally enters third on-board components 3,3 parts, arch cloth are divided by arch gas distribution wall 301
Gas wall 301 also functions to perturbation action to mixed coal grain, and loose mixed coal grain is when by the air inlet eyelet 303 of arch gas distribution wall 301
Internal combustion, which occurs, for the fuel gas and air that mixed coal is come in the conveying of air inlet eyelet 303 makes mixed coal be thermally decomposed, in arch gas distribution wall
Temperature is 500-600 DEG C at 301, and last mixed coal enters between tricuspid gas distribution wall 303, the gas come in using air inlet eyelet 303
Internal combustion, generating 650 DEG C of -700 DEG C or so temperature makes coal that hot-working decomposition occur, and finally passes through discharge channel and vertical cavity is discharged
107。
Mixed coal reacts at third on-board components 3, generates high temperature heat source gas and high temperature hydrocarbon mixture gas, due to
Other processing units are connected below discharge channel, air resistance is excessive, therefore high temperature heat source gas and high temperature hydrocarbon mixture gas to
Coal moving direction inversely rises, to the second on-board components 2, since the second on-board components 2 generate low pressure at area of space 202
Area, heat source gas are gathered in area of space 202 with high temperature hydrocarbon mixture, gather pressure and are more than 202 attachment gas of area of space
When resistance, heat source gas continues the reverse mixed coal direction of motion with high temperature hydrocarbon mixture gas and rises at the first on-board components 1, heat
Source gas and hydrocarbon mixture gas enter 1 bottom-open mouth of the first on-board components, are discharged by drainage tube 103, while the
In one on-board components 1 subaisle 102 gap between oblique side wall 104 is set can be by remaining hydrocarbon mixture between subaisle 102
Gas recycles, and hydrocarbon mixture gas and heat source gas on the one hand can be avoided to gather in 107 top plate portion of vertical cavity and caught fire now
As hydrocarbon mixture and heat source gas on the other hand can be avoided to enter through material-feeding port and cause uncontrollable discharge in air.
Embodiment 2
Referring to Fig. 1-4, the utility model mixed coal prepares the device of carbon-rich solids cleaning products, mixed for grain size 30mm or less
Coal, when wherein 15mm or less coals content is more, apparatus structure includes vertical cavity 107, and vertical cavity 107 is connected component, by upper
Material-feeding port, the first on-board components 1, the second on-board components 2, third on-board components 3 and discharge channel are followed successively by under and.
107 bottom of vertical cavity is provided with third on-board components 3, tricuspid gas distribution wall is provided in third on-board components 3
302, tricuspid gas distribution wall 302 is set as several, tricuspid gas distribution wall side wall 302 is provided with three layers of air inlet eyelet 303, by combustible gas
Body reaches 650 DEG C of -700 DEG C of generation hot-working decomposition, tricuspid with coal in air delivery to air inlet eyelet 303, is made after generation internal combustion
The discharge channel is arranged in 302 lower section of gas distribution wall.Arch gas distribution wall 301, arch gas distribution wall are additionally provided in third on-board components 3
301 settings at least 3,2 layers of air inlet eyelet 303 are provided in 301 side wall of arch gas distribution wall, will be flammable by air inlet eyelet 303
Gas and in air delivery to air inlet eyelet 303, then internal combustion, which occurs, makes coal reach 650-700 DEG C of generation hot-working decomposition,
After the hydrocarbon mixture gas and heat source gas generated at third on-board components 3 rises at the second on-board components 2 and gathers, continue on
It rises to 1 lower port of the first on-board components and vertical cavity 107 is discharged via drainage tube 103；
Aperture gradually becomes from inside to outside in the duct of setting air inlet eyelet 303 in tricuspid gas distribution wall 302 and arch gas distribution wall 201
It is small；
The second on-board components of setting upper layer and lower layer 2 at the middle part of vertical cavity 107, the second on-board components of lower layer 2 be arranged it is multiple,
2 the second on-board components of lower layer 2 of the second on-board components of upper layer are 1 few, and the second on-board components of upper layer and lower layer 2 shift to install；
The first on-board components 1, the second on-board components 2,3 structure of third on-board components in vertical cavity is as follows：
First on-board components, 1 structure includes：Main channel 101, subaisle 102, drainage tube 103, the first triangle perforated panel 105
With the second triangle perforated panel 106；Main channel 101 with by flaring type head and two vertical directions setting side wall 105 combine and
At, mouth down, from top to bottom mouth becomes larger；Subaisle 102 is composed of flaring type head and several oblique side walls 104, tiltedly
Sidewall symmetry is set as 10 layers (are symmetrical arranged and refer to each 10 oblique side walls in both sides)；6 pairs are arranged with main channel 101 in subaisle 102
Channel 102, which is vertically inlayed, to be welded, and main channel 101 is respectively provided with triangle perforated panel with 102 both ends of subaisle and is welded, point
The flaring type head of type also uses circular arc type superstructure；
Second on-board components 2 are by flaring type head, two curved walls, 204, two the second upstanding sidewalls 206 and two
Three triangle perforated panels 205 are composed, and 202 both ends of area of space and the third triangle perforated panel 205 of the second on-board components 2 weld
It connects.Acute angle mouth down, 2 split shed of the second on-board components from top to bottom become larger, and 2 lower end of the second on-board components is open ports；
At least 3 rows are set on flaring type head and are vented eye 203, air passage 201 is provided on upstanding sidewall 206, air passage 201 is arranged
At least 1 row, the symmetrical acute angle shape top in both sides may be alternatively provided as arch superstructure.
Air passage 201 may be configured as square hole, trapezoidal hole or tri-angle-holed etc..
3 structure of third on-board components includes tricuspid gas distribution wall 302, arch gas distribution wall 301, air inlet brick, tricuspid gas distribution wall 302
Air inlet brick is arranged in side wall wall, and air inlet brick is provided with air inlet eyelet 303, air inlet eyelet 303 and external aeration in third on-board components 3
Pipeline connection, arch gas distribution wall 301 and 302 cross of tricuspid gas distribution wall are staggered setting, and arch gas distribution wall 301 is provided with air inlet eyelet
303, arch gas distribution wall 301 is communicated with tricuspid gas distribution wall air flue 302.Air inlet eyelet 303 and the angle of horizontal plane are 35 ° -55 °,
And the cross sectional shape of air inlet eyelet 303 is ellipse.
The technological process that carbon-rich solids cleaning products are prepared using the utility model mixed coal is as follows：
Mixed coal enters vertical cavity 107 by material-feeding port, by the first on-board components 1, subsequently into the second on-board components 2,
Mixed coal is moved down by being divided into two parts by the second on-board components 2 when the second on-board components 2, in moving process, the
Two on-board components 2 have perturbation action to mixed coal grain, and fluffing action can be played between mixed coal grain, finally enter structure built in third
Part 3, mixed coal is divided into 4 parts when arch gas distribution wall 301 by third on-board components 3, is also risen in mixed coal cutting procedure
It is acted on to loose mixed coal layer, the combustible gas conveyed at 301 air inlet eyelet 303 of arch gas distribution wall and in air inlet eyelet 303
Body and air internal combustion are thermally decomposed, at arch gas distribution wall 301 temperature be 600 DEG C, last mixed coal be divided into again 7 parts into
Between entering tricuspid gas distribution wall 302, the fuel gas and air internal combustion come in using air inlet eyelet 303, generating 700 DEG C of temperature makes coal send out
Heat processing is decomposed, and finally passes through discharge channel and vertical cavity 107 is discharged.
Mixed coal reacts at third on-board components 3 generates high temperature heat source gas and high temperature hydrocarbon mixture gas, due to
Other processing units are connected below discharge channel, air resistance is excessive, therefore high temperature heat source gas and high temperature hydrocarbon mixture gas to
Mixed coal moving direction inversely rises to 2 lower layer of the second on-board components, since 2 inside of the second on-board components forms area of space 202
Cause to generate low-pressure area, heat source gas is assembled with high temperature hydrocarbon mixture in this area of space 202, gathers pressure and is more than space region
When 202 attachment air resistance of domain, two sharp edges are provided with vent cap 201 in the second on-board components 2, are opened with two upstanding sidewalls 206
There is an exhaust eye 203, heat source gas and high temperature hydrocarbon mixture gas continue to rise to the by exhaust eye 203 and vent cap 201
Area of space 202 in two on-board components 2 passes through vent cap 201 and exhaust eye 203, the heat source of the second on-board components of upper layer 2
Gas continues the reverse coal direction of motion with high temperature hydrocarbon mixture and rises at the first on-board components 1, heat source gas and high temperature mixing
Hydrocarbon gas enters the open ports of 1 bottom of the first on-board components, is discharged by drainage tube 103, while structure built in first
Between oblique side wall 104 on the one hand remaining hydrocarbon mixture gas high efficiente callback between subaisle 102 can be avoided standing by gap in part 1
107 top plate portion hydrocarbon mixture gas of formula cavity and heat source gas gather generation Ignition Phenomena, on the other hand can avoid hydrocarbon mixture
Class product and heat source gas enter air through material-feeding port and pollute.
Obvious above-mentioned case is only clearly to illustrate to be made case, not be limited embodiment, for described
For the those of ordinary skill of field, other various forms of variations or variation can also be made on the basis of the above description, this
In all embodiments can not be enumerated, thus extending obvious variation or changes and still falls within the utility model
Protection domain.
Claims (10)
1. a kind of preparation facilities of carbon-rich solids cleaning products, it is characterised in that：Including being from top to bottom successively set on vertical chamber
The first on-board components (1), the second on-board components (2) in body (107) and third on-board components (3)；First on-board components
(1) material-feeding port is arranged in top, and the lower section of the third on-board components (3) connects discharge channel；
First on-board components (1) include horizontally disposed main channel (101) and vertical with main channel (101) and be embedded in side by side
Multiple subaisles (102) on main channel (101)；Main channel (101) and the head of subaisle (102) are flaring type；
Multiple drainage tubes (103) are provided on the flaring type head of main channel (101)；
Second on-board components (2) are at least arranged side by side two layers in vertical cavity (107), and each second on-board components (2)
Include offering the flaring type head of vent cap (201) and being connected to the upstanding sidewall of flaring type lower head, it is described
Upstanding sidewall on offer several exhaust eye (203)；The second on-board components (2) interval setting of same layer, adjacent layer
Second on-board components (2) mutual dislocation；The bottom-open of second on-board components (2)；
Third on-board components (3) include horizontally disposed a plurality of arch gas distribution wall (301) and vertical with arch gas distribution wall (301)
And it is embedded in multiple tricuspid gas distribution walls (302) on arch gas distribution wall (301) side by side；Arch gas distribution wall (301) and tricuspid gas distribution
Wall (302) if on be provided with dried layer air inlet brick, air inlet eyelet (303) is provided on air inlet brick.
2. the preparation facilities of carbon-rich solids cleaning products according to claim 1, it is characterised in that：Main channel (101), pair are logical
Road (102) and the flaring type head of the second on-board components (2) use circular arc type or tip.
3. the preparation facilities of carbon-rich solids cleaning products according to claim 1, it is characterised in that：Main channel (101) and pair
The flaring type head in channel (102) uses tip, and the tip head of main channel (101) is welded by the first triangle perforated panel (105)
It connects, the tip head of subaisle (102) is welded by the second triangle perforated panel (106).
4. the preparation facilities of carbon-rich solids cleaning products according to claim 3, it is characterised in that：Subaisle (102) flaring
Multiple oblique side walls (104) of type head connected symmetrical dendrimer setting, oblique side wall (104) are set as 5 layers.
5. the preparation facilities of carbon-rich solids cleaning products according to claim 1, it is characterised in that：Second on-board components
(2) pass through arc side plate (204) transition between flaring type head and upstanding sidewall to connect.
6. the preparation facilities of carbon-rich solids cleaning products according to claim 1, it is characterised in that：The drainage tube
(103) up big and down small cylinder is used.
7. the preparation facilities of carbon-rich solids cleaning products according to claim 1, it is characterised in that：Second on-board components (2)
Upstanding sidewall on exhaust eye (203) size for opening up it is identical.
8. the preparation facilities of carbon-rich solids cleaning products according to claim 1, it is characterised in that：The air inlet eyelet
(303) air inlet port being arranged to air inlet brick inner inclination, the internal diameter flaring or tapered of air inlet port are connected.
9. the preparation facilities of carbon-rich solids cleaning products according to claim 1, it is characterised in that：The exhaust eye
(203) trapezoidal, triangle or square structure are used.
10. the preparation facilities of carbon-rich solids cleaning products according to claim 1, it is characterised in that：Built in described second
Component (2) is provided at both ends with third triangle perforated panel (205).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721250867.8U CN207699525U (en) | 2017-09-27 | 2017-09-27 | A kind of preparation facilities of carbon-rich solids cleaning products |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721250867.8U CN207699525U (en) | 2017-09-27 | 2017-09-27 | A kind of preparation facilities of carbon-rich solids cleaning products |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207699525U true CN207699525U (en) | 2018-08-07 |
Family
ID=63021237
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721250867.8U Active CN207699525U (en) | 2017-09-27 | 2017-09-27 | A kind of preparation facilities of carbon-rich solids cleaning products |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207699525U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107858163A (en) * | 2017-09-27 | 2018-03-30 | 榆林煤化工产业促进中心 | A kind of mixed coal prepares the device of carbon-rich solids cleaning products |
-
2017
- 2017-09-27 CN CN201721250867.8U patent/CN207699525U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107858163A (en) * | 2017-09-27 | 2018-03-30 | 榆林煤化工产业促进中心 | A kind of mixed coal prepares the device of carbon-rich solids cleaning products |
| CN107858163B (en) * | 2017-09-27 | 2024-02-20 | 榆林煤化工产业促进中心 | Device for preparing carbon-rich solid cleaning product by mixing coal |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107286969A (en) | A kind of pyrolysis oven based on packed bed pulverized coal pyrolysis, pyrolysis installation and pyrolytic process | |
| CN103557517B (en) | The method and apparatus of living beings second pyrolysis | |
| CN107474860A (en) | A kind of porous media external-heat carbonization furnace | |
| CN207699525U (en) | A kind of preparation facilities of carbon-rich solids cleaning products | |
| CN111072028A (en) | Tubular carbonization-activation integrated furnace and using method | |
| CN203757694U (en) | Energy reservation, emission reduction and efficient combustion biomass boiler | |
| CN202214340U (en) | Continuous gasification and tar removing device for biomass moving bed | |
| CN102443445B (en) | Process and device for continuously gasifying biomass and simultaneously removing tar in moving bed | |
| CN208234847U (en) | A kind of biomass carbonated destructive distillation purification recovery device | |
| CN206929792U (en) | Suitable for the tertiary air blowing system of biomass incinerator thorax | |
| CN206094096U (en) | Small -size garbage pyrolytic gasifier | |
| CN2457159Y (en) | Tubular type movable bed dry distillation carbide furnace | |
| CN108504369A (en) | A kind of biomass carbonated destructive distillation purification recovery device and method | |
| CN107858163A (en) | A kind of mixed coal prepares the device of carbon-rich solids cleaning products | |
| CN104896480B (en) | A kind of bilingual processing unit of rubbish | |
| CN206093990U (en) | Vertical type fire tube boiler | |
| CN203036668U (en) | Fire coal steam combustion-supporting furnace | |
| CN212102000U (en) | High-yield and energy-saving production system of activated carbon carbonization furnace | |
| CN103897710B (en) | A kind of upright furnace coking chamber with interior air collecting chamber | |
| CN108728172A (en) | A kind of aditus structure and the biomass gasifying furnace containing the aditus structure | |
| CN208414331U (en) | A kind of fixed bed slag gasification furnace handling biomass fuel | |
| CN201971784U (en) | Primary dust remover | |
| CN204268465U (en) | A kind of gas fired-boiler | |
| CN202047006U (en) | Environment-friendly energy-saving carbon-burning shaft kiln of combustion gas generation chamber | |
| CN102219403A (en) | Environmental-protection and energy-saving gas generation chamber carbon-burning shaft kiln |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |