CN207822740U - A kind of revolution bed type activated coke absorption regeneration integration multi-pollutant removing device - Google Patents
A kind of revolution bed type activated coke absorption regeneration integration multi-pollutant removing device Download PDFInfo
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- CN207822740U CN207822740U CN201721624740.8U CN201721624740U CN207822740U CN 207822740 U CN207822740 U CN 207822740U CN 201721624740 U CN201721624740 U CN 201721624740U CN 207822740 U CN207822740 U CN 207822740U
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- activated coke
- upper cover
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- 238000011069 regeneration method Methods 0.000 title claims abstract description 50
- 239000000571 coke Substances 0.000 title claims abstract description 48
- 230000008929 regeneration Effects 0.000 title claims abstract description 47
- 238000010521 absorption reaction Methods 0.000 title claims abstract description 34
- 239000003344 environmental pollutant Substances 0.000 title claims abstract description 33
- 230000010354 integration Effects 0.000 title claims abstract description 33
- 238000001179 sorption measurement Methods 0.000 claims abstract description 23
- 239000002245 particle Substances 0.000 claims abstract description 20
- 238000009826 distribution Methods 0.000 claims abstract description 5
- 239000007789 gas Substances 0.000 claims description 38
- 238000007789 sealing Methods 0.000 claims description 17
- 230000008676 import Effects 0.000 claims description 11
- 239000003546 flue gas Substances 0.000 claims description 7
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 6
- 235000019504 cigarettes Nutrition 0.000 claims description 2
- 238000013461 design Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 239000000428 dust Substances 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 239000000809 air pollutant Substances 0.000 description 1
- 231100001243 air pollutant Toxicity 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000008821 health effect Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000013011 mating Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
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- Treating Waste Gases (AREA)
Abstract
The utility model discloses a kind of revolution bed type activated coke absorption regeneration integration multi-pollutant removing devices, including：Mutually independent multiple chambers for filling adsorption particle, multiple chambers are circumferentially to distribution；Upper cover plate and lower cover, the upper cover plate and lower cover are connect with the top of the chamber and bottom end seal respectively, and the chamber can be rotated relative to the upper cover plate and lower cover；The shaft being rotatablely connected with the upper cover plate and lower cover, the shaft drive the chamber to rotate when rotating, gas inlet and N are offered on the upper cover plate2Import is provided with exhanst gas outlet and N on the lower cover2Outlet, the shaft can drive multiple chambers turn to the gas inlet and exhanst gas outlet with one of chamber and the N2Import and N2Outlet with another chamber.The revolution bed type activated coke absorption regeneration integration multi-pollutant removing device can efficiently solve the higher problem of activated coke regeneration cost.
Description
Technical field
The utility model is related to air pollutants adsorption technology fields, more specifically to a kind of revolution bed type activity
Burnt absorption regeneration integration multi-pollutant removing device.
Background technology
In recent years, China's atmosphere pollution is on the rise, and larger health effect is generated to people's daily production and life.Its
Middle coal-burning boiler, all types of industries stove etc. are the primary pollution source of atmospheric environment, are always the emphasis of environmental improvement for many years.
For response, country calls, and most domestic power plant has been carried out for NOx, dust, SO2The minimum discharge transformation of equal pollutants, takes
Obtained good result.But there is also many problems for the prior art, especially for industrial furnace, prior art complexity, energy consumption
Greatly, low, secondary pollution of removal efficiency etc..
In active coke desulphurizing technique, activated coke consumption is big, and desulphurizing activated coke must carry out regeneration treatment, with reduce at
This, and recycle Sulphur ressource.Desulphurizing activated coke regeneration method has heating to regenerate and wash two kinds of regeneration, wherein heating regeneration is extensive
Using heating regeneration needs activated coke being heated to 400 DEG C or so, and reaction temperature is high, and a large amount of dust, SO are contained in resolution gas2、
Vapor etc., while needing to completely cut off air, it is relatively high to equipment and operation operation requirement, and need to design adsorption tower and parsing
Tower, occupation area of equipment is larger, and cost is higher.
It is current those skilled in the art in conclusion how to efficiently solve the higher problem of activated coke regeneration cost
Urgent problem.
Utility model content
In view of this, the purpose of this utility model is to provide how dirty a kind of revolution bed type activated coke absorption regeneration integration is
Object removing means is contaminated, the structure design of the revolution bed type activated coke absorption regeneration integration multi-pollutant removing device can be effective
Ground solves the problems, such as that activated coke regeneration cost is higher.
In order to achieve the above object, the utility model provides the following technical solutions：
A kind of revolution bed type activated coke absorption regeneration integration multi-pollutant removing device, including：
Mutually independent multiple chambers for filling adsorption particle, multiple chambers are circumferentially to distribution；
Upper cover plate and lower cover, the upper cover plate and lower cover are connect with the top of the chamber and bottom end seal respectively,
And the chamber can be rotated relative to the upper cover plate and lower cover；
The shaft being rotatablely connected with the upper cover plate and lower cover, the shaft drive the chamber to rotate when rotating,
Gas inlet and N are offered on the upper cover plate2Import is provided with exhanst gas outlet and N on the lower cover2Outlet, the shaft
Can drive multiple chambers turn to the gas inlet and exhanst gas outlet with one of chamber and the N2
Import and N2Outlet with another chamber.
Preferably, in above-mentioned revolution bed type activated coke absorption regeneration integration multi-pollutant removing device, the chamber
Quantity is two, and the chamber is semi-cylindrical, and columned revolution bed is collectively formed in two chambers.
Preferably, in above-mentioned revolution bed type activated coke absorption regeneration integration multi-pollutant removing device, the chamber
Inside is from top to bottom provided with multilayer backing plate with holes, and multiple windows are provided on the side wall of the chamber and are opened and closed with the window
The sealing plate of cooperation can be extracted out the backing plate with holes by the window.
Preferably, in above-mentioned revolution bed type activated coke absorption regeneration integration multi-pollutant removing device, the sealing plate with
The backing plate with holes is fixedly connected.
Preferably, in above-mentioned revolution bed type activated coke absorption regeneration integration multi-pollutant removing device, multiple windows
Mouth from top to bottom layer distributed, and every layer of multiple windows are uniformly distributed.
Preferably, in above-mentioned revolution bed type activated coke absorption regeneration integration multi-pollutant removing device, the pad with holes
The through-hole diameter of plate is less than 50mm.
Preferably, in above-mentioned revolution bed type activated coke absorption regeneration integration multi-pollutant removing device, the upper cover plate
Bottom side and lower cover on the upside of all have annular slot, the top and bottom end of the chamber are stretched into the annular slot.
Preferably, in above-mentioned revolution bed type activated coke absorption regeneration integration multi-pollutant removing device, the shaft is logical
Bearing is crossed to be rotatablely connected with the upper cover plate and lower cover.
Revolution bed type activated coke absorption regeneration integration multi-pollutant removing device provided by the utility model include chamber,
Upper cover plate, lower cover and shaft.The quantity of its middle chamber is multiple, and chamber for filling adsorption particle, specifically may be used by adsorption particle
Think activated coke filling ball.Multiple chambers are mutual indepedent, i.e. any two chamber interior is not connected to；Multiple chambers circumferentially to
Distribution, i.e., multiple chambers are along the circumferentially distributed of circle.The end sealing of upper cover plate and chamber connects, the bottom of lower cover and chamber
End is tightly connected, and chamber can be rotated relative to upper cover plate and lower cover.I.e. upper cover plate and lower cover are fixed and more
A chamber can rotate, and so can support upper cover plate and lower cover by holder etc..
Shaft is rotatablely connected with upper cover plate and lower cover, i.e., shaft can be rotated relative to upper cover plate and lower cover, be turned
Shaft rotation drives multiple chambers while rotating when dynamic.Gas inlet and N are offered on upper cover plate2Import is provided with cigarette on lower cover
Gas exports and N2Outlet.Shaft can drive multiple chambers turn to gas inlet and exhanst gas outlet with one of chamber connect
Logical and N2Import and N2With another chamber, i.e. gas inlet and exhanst gas outlet be connected to N simultaneously with same chamber for outlet2
Import and N2Outlet is also connected to same chamber, and gas inlet and N2Import is connected to two chambers respectively.
It is first when using revolution bed type activated coke absorption regeneration integration multi-pollutant removing device provided by the utility model
First rotating shaft, make gas inlet and exhanst gas outlet with one of chamber and N2Import and N2Outlet and another
Chamber, flue gas pending at this time enter one of chamber through gas inlet, after the adsorption particle processing in chamber
It is discharged from exhanst gas outlet.Meanwhile through N2Import fills N into another chamber2, the gas being filled with is through N2Outlet discharge, is realized with this
Regeneration to the indoor adsorption particle of another chamber.When the indoor adsorption particle of chamber that processing is connected to gas inlet needs to regenerate
When, it can be rotated further shaft, the chamber being connected to originally with gas inlet is made to turn to and N2Inlet communication.Such as above-mentioned institute
It states, using multiple during revolution bed type activated coke absorption regeneration integration multi-pollutant removing device provided by the utility model
Chamber alternate treatment flue gas and can pour N2Regeneration, it is not necessary to which individually designed adsorption tower and Analytic Tower again greatly reduce activated coke
Regeneration cost.
Description of the drawings
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only
It is some embodiments of the utility model, for those of ordinary skill in the art, in the premise not made the creative labor
Under, other drawings may also be obtained based on these drawings.
Fig. 1 is the revolution bed type activated coke absorption regeneration integration multi-pollutant removing dress that the utility model embodiment provides
The vertical view set；
Fig. 2 is the revolution bed type activated coke absorption regeneration integration multi-pollutant removing dress that the utility model embodiment provides
The sectional view set；
Fig. 3 is the revolution bed type activated coke absorption regeneration integration multi-pollutant removing dress that the utility model embodiment provides
The front view set.
In fig. 1-3：
1- upper cover plates, 2-N2Import, 3- shafts, 4- gas inlets, 5- chambers, 6- adsorption particles, 7-N2Outlet, 8- flue gases
Outlet, 9- backing plates with holes, 10- sealing plates.
Specific implementation mode
The purpose of this utility model is to provide a kind of revolution bed type activated coke absorption regeneration integration multi-pollutant removings
The structure design of device, the revolution bed type activated coke absorption regeneration integration multi-pollutant removing device can efficiently solve work
The property higher problem of coke regeneration cost.
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
The every other embodiment obtained, shall fall within the protection scope of the present invention.
In the description of the present invention, it should be understood that term "upper", "lower", "front", "rear", " left side " and " right side "
The orientation or positional relationship of equal instructions is to be based on the orientation or positional relationship shown in the drawings, and is merely for convenience of describing this practicality newly
Type and simplified description, particular orientation must be had, with specific orientation structure by not indicating or implying the indicated position or element
At and operation, therefore should not be understood as the limitation of the utility model.In addition, term " first ", " second " are used for description purposes only,
It is not understood to indicate or imply relative importance.
- Fig. 3 is please referred to Fig.1, how dirty the revolution bed type activated coke absorption regeneration integration that the utility model embodiment provides is
It includes chamber 5, upper cover plate 1, lower cover and shaft 3 to contaminate object removing means.The quantity of its middle chamber 5 is multiple, and chamber 5 is for filling out
Adsorption particle 6 is filled, adsorption particle 6 is specifically as follows activated coke filling ball.Multiple chambers 5 are mutual indepedent, i.e. any two chamber 5
Inside is not connected to；Multiple chambers 5 are circumferentially to distribution, i.e., multiple chambers 5 are along the circumferentially distributed of circle.Upper cover plate 1 and chamber
The end sealing of room 5 connects, and lower cover is connect with the bottom end seal of chamber 5, and chamber 5 can be relative to upper cover plate 1 under
Cover board rotates.I.e. upper cover plate 1 and lower cover are fixed and multiple chambers 5 can rotate, and can so pass through the supports such as holder
Upper cover plate 1 and lower cover.
Shaft 3 is rotatablely connected with upper cover plate 1 and lower cover, i.e., shaft 3 can turn relative to upper cover plate 1 and lower cover
Dynamic, shaft 3 drives multiple chambers 5 while rotating when rotating.Gas inlet 4 and N2 imports 2, lower cover are offered on upper cover plate 1
On be provided with exhanst gas outlet 8 and N2 outlet 7.Shaft 3 can drive multiple chambers 5 to turn to gas inlet 4 and exhanst gas outlet 8
It is connected to one of chamber 5 and N2 imports 2 and the outlets N2 7 is connected to another chamber 5, i.e., gas inlet 4 and flue gas go out
Mouth 8 is connected to N2 imports simultaneously 2 with same chamber 5 and the outlets N2 7 are also connected to same chamber 5, and gas inlet 4 and N2 imports
2 are connected to two chambers 5 respectively.
The revolution bed type activated coke absorption regeneration integration multi-pollutant removing dress provided using the utility model embodiment
When setting, rotating shaft 3 first makes that gas inlet 4 and exhanst gas outlet 8 are connected to one of chamber 5 and N2 imports 2 and N2 go out
Mouth 7 is connected to another chamber 5, and flue gas pending at this time enters one of chamber 5 through gas inlet 4, through in chamber 5
Adsorption particle 6 handle after from exhanst gas outlet 8 be discharged.Meanwhile N is filled into another chamber 5 through N2 imports 22, the gas that is filled with
Through 7 discharge of the outlets N2, the regeneration to the adsorption particle 6 in another chamber 5 is realized with this.When processing is connected to gas inlet 4
Chamber 5 in adsorption particle 6 need regeneration when, shaft 3 can be rotated further, make 5 turns of the chamber being connected to originally with gas inlet 4
It moves to N2 imports 2 and is connected to.It is as described above, use revolution bed type activated coke absorption regeneration one provided by the utility model
Multiple chambers 5 alternate treatment flue gas and can pour N during body multi-pollutant removing device2Regeneration, it is not necessary to individually designed again
Adsorption tower and Analytic Tower greatly reduce activated coke regeneration cost.
In order to simplify structure, the quantity of chamber 5 can be two, and two chambers 5 are semi-cylindrical, two chambers 5
Columned revolution bed is collectively formed.It so only needs two chambers 5 to be alternately connected to gas inlet 4, also easily facilitates
Driving revolution bed rotation.Certainly, the quantity of chamber 5 may be three or more, be not limited thereto.
When 6 usage time of adsorption particle is long to be regenerated, adsorption particle 6 is needed replacing.It is adsorbed for the ease of replacing
The inside of particle 6, chamber 5 can from top to bottom be provided with multilayer backing plate 9 with holes, and multiple windows are provided on the side wall of chamber 5
With the sealing plate 10 with window opening and closing cooperation, backing plate 9 with holes can be extracted out by window.Wherein, sealing plate 10 can block window
Mouthful, every layer of 9 top of backing plate with holes is filled with adsorption particle 6, sealing plate 10 open after can by window by backing plate 9 with holes and its
The adsorption particle 6 of upside is extracted out, and backing plate 9 with holes is inserted into 5 inside of chamber again after replacing adsorption particle 6.
Further, sealing plate 10 can be fixedly connected with backing plate 9 with holes, and such sealing plate 10 can be arranged with backing plate 9 with holes
For drawer type, the movement of sealing plate 10 and backing plate 9 with holes can be realized by pull.Certainly, sealing plate 10 may be set to be door-plate
Shape is realized opening and closing of fault by rotating sealing plate 10, is not limited thereto.
As shown in figure 3, in above-described embodiment, multiple windows from top to bottom layer distributed, and every layer of multiple windows are uniform
Distribution, i.e. every layer of multiple windows are circumferentially uniformly distributed.Certainly, multiple windows can arbitrarily arrange, and be not limited thereto.
In another embodiment, the through-hole diameter of backing plate 9 with holes is more than 50mm, and the diameter for the activated coke filler so filled is small
In 50mm, to prevent activated coke filler from exposing.Certainly, the through-hole on backing plate 9 with holes can have any shape, and not make herein
It limits.
In order to realize that the sealing of upper cover plate 1 and lower cover and 5 diameter of chamber, the bottom side of upper cover plate 1 have annular slot, chamber
The top of room 5 is stretched into the annular slot of upper cover plate 1；The upside of lower cover has annular slot, and lower cover is stretched into the bottom end of chamber 5
In the annular slot of plate, so by the mating of annular slot and upper and lower cover plates, to prevent the leakage of gas.Annular slot
Inside it is also provided with sealing ring etc..The depth of annular slot can be 4-8mm, be specifically as follows 5mm, be not limited thereto.
Further, shaft 3 is rotatablely connected by bearing and upper cover plate 1 and lower cover, to reduce the frictional force of shaft 3,
Reduce abrasion.
Each embodiment is described by the way of progressive in this specification, the highlights of each of the examples are with other
The difference of embodiment, just to refer each other for identical similar portion between each embodiment.
The foregoing description of the disclosed embodiments enables professional and technical personnel in the field to realize or use this practicality new
Type.Various modifications to these embodiments will be apparent to those skilled in the art, and determine herein
The General Principle of justice can be realized in other embodiments without departing from the spirit or scope of the present utility model.Cause
This, the utility model is not intended to be limited to the embodiments shown herein, and is to fit to and principles disclosed herein
The widest range consistent with features of novelty.
Claims (8)
1. a kind of revolution bed type activated coke absorption regeneration integration multi-pollutant removing device, which is characterized in that including：
Mutually independent multiple chambers (5) for filling adsorption particle (6), multiple chambers (5) are circumferentially to distribution；
Upper cover plate (1) and lower cover, the upper cover plate (1) and lower cover respectively with the top of the chamber (5) and bottom end seal
Connection, and the chamber (5) can be rotated relative to the upper cover plate (1) and lower cover；
The shaft (3) being rotatablely connected with the upper cover plate (1) and lower cover, the shaft (3) drive the chamber when rotating
(5) it rotates, offers gas inlet (4) and N2 imports (2) on the upper cover plate (1), being provided with flue gas on the lower cover goes out
Mouth (8) and the outlets N2 (7), the shaft (3) can drive multiple chambers (5) to turn to the gas inlet (4) and cigarette
Gas outlet (8) is connected to one of chamber (5) and the N2 imports (2) and the outlets N2 (7) connect with another chamber (5)
It is logical.
2. revolution bed type activated coke absorption regeneration integration multi-pollutant removing device according to claim 1, feature
It is, the quantity of the chamber (5) is two, and the chamber (5) is semi-cylindrical, and two chambers (5) are collectively formed
Columned revolution bed.
3. revolution bed type activated coke absorption regeneration integration multi-pollutant removing device according to claim 1, feature
It is, the inside of the chamber (5) is from top to bottom provided with multilayer backing plate with holes (9), is provided on the side wall of the chamber (5)
Multiple windows and the sealing plate (10) coordinated with window opening and closing can be extracted out the backing plate (9) with holes by the window.
4. revolution bed type activated coke absorption regeneration integration multi-pollutant removing device according to claim 3, feature
It is, the sealing plate (10) is fixedly connected with the backing plate (9) with holes.
5. revolution bed type activated coke absorption regeneration integration multi-pollutant removing device according to claim 3, feature
It is, multiple windows from top to bottom layer distributed, and every layer of multiple windows are uniformly distributed.
6. revolution bed type activated coke absorption regeneration integration multi-pollutant removing device according to claim 3, feature
It is, the through-hole diameter of the backing plate (9) with holes is less than 50mm.
7. revolution bed type activated coke absorption regeneration integration multi-pollutant removing device according to claim 1, feature
It is, annular slot, the top and bottom end of the chamber (5) is all had on the upside of the bottom side of the upper cover plate (1) and lower cover
It stretches into the annular slot.
8. revolution bed type activated coke absorption regeneration integration multi-pollutant removing device according to claim 1, feature
It is, the shaft (3) is rotatablely connected by bearing and the upper cover plate (1) and lower cover.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721624740.8U CN207822740U (en) | 2017-11-28 | 2017-11-28 | A kind of revolution bed type activated coke absorption regeneration integration multi-pollutant removing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721624740.8U CN207822740U (en) | 2017-11-28 | 2017-11-28 | A kind of revolution bed type activated coke absorption regeneration integration multi-pollutant removing device |
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| Publication Number | Publication Date |
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| CN207822740U true CN207822740U (en) | 2018-09-07 |
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ID=63385571
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107803096A (en) * | 2017-11-28 | 2018-03-16 | 国电环境保护研究院 | One kind revolution bed activated coke absorption regeneration integration multi-pollutant removing device |
-
2017
- 2017-11-28 CN CN201721624740.8U patent/CN207822740U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107803096A (en) * | 2017-11-28 | 2018-03-16 | 国电环境保护研究院 | One kind revolution bed activated coke absorption regeneration integration multi-pollutant removing device |
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