CN107803096A - One kind revolution bed activated coke absorption regeneration integration multi-pollutant removing device - Google Patents
One kind revolution bed activated coke absorption regeneration integration multi-pollutant removing device Download PDFInfo
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- CN107803096A CN107803096A CN201711216647.8A CN201711216647A CN107803096A CN 107803096 A CN107803096 A CN 107803096A CN 201711216647 A CN201711216647 A CN 201711216647A CN 107803096 A CN107803096 A CN 107803096A
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- chamber
- activated coke
- removing device
- upper cover
- lower cover
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/0407—Constructional details of adsorbing systems
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/102—Carbon
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0283—Flue gases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/40083—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption
- B01D2259/40086—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption by using a purge gas
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/402—Further details for adsorption processes and devices using two beds
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treating Waste Gases (AREA)
Abstract
The invention discloses one kind to turn round bed activated coke absorption regeneration integration multi-pollutant removing device, including：Separate multiple chambers for being used to fill adsorption particle, multiple chambers are circumferentially to distribution；Upper cover plate and lower cover, the upper cover plate and lower cover are connected with the top of the chamber and bottom end seal respectively, and the chamber can rotate relative to the upper cover plate and lower cover；The rotating shaft being rotatablely connected with the upper cover plate and lower cover, drive during the axis of rotation chamber to rotate, gas approach and N are offered on the upper cover plate2Import, exhanst gas outlet and N are provided with the lower cover2Outlet, the rotating shaft can drive multiple chambers turn to the gas approach and exhanst gas outlet with one of chamber and the N2Import and N2Outlet with another chamber.The revolution bed activated coke absorption regeneration integration multi-pollutant removing device can efficiently solve the problem of activated coke regeneration cost is higher.
Description
Technical field
The present invention relates to air pollutants adsorption technology field, is inhaled more specifically to one kind revolution bed activated coke
The attached integrated multi-pollutant removing device of regeneration.
Background technology
In recent years, China's atmosphere pollution is on the rise, and larger health effect is produced 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 is called, and most domestic power plant is had been carried out for NOx, dust, SO2Minimum discharge Deng pollutant is transformed, and is taken
Obtained good result.But prior art, there is also many problems, especially for industrial furnace, existing process is complicated, 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 into
This, and reclaim Sulphur ressource.Desulphurizing activated coke regeneration method has two kinds of thermal regeneration and washing regeneration, and wherein thermal regeneration is extensive
Using thermal 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 need to completely cut off air, higher is required to equipment and operation operation, and need to design adsorption tower and parsing
Tower, occupation area of equipment is larger, and cost is higher.
In summary, the problem of activated coke regeneration cost is higher how is efficiently solved, is current those skilled in the art
Urgent problem.
The content of the invention
In view of this, it is an object of the invention to provide one kind to turn round bed activated coke absorption regeneration integration multi-pollutant
Removing means, the structure design of the revolution bed activated coke absorption regeneration integration multi-pollutant removing device can be solved effectively
The problem of certainly activated coke regeneration cost is higher.
In order to achieve the above object, the present invention provides following technical scheme：
One kind revolution bed activated coke absorption regeneration integration multi-pollutant removing device, including：
Separate multiple chambers for being used to fill adsorption particle, multiple chambers are circumferentially to distribution；
Upper cover plate and lower cover, the upper cover plate and lower cover are connected with the top of the chamber and bottom end seal respectively,
And the chamber can rotate relative to the upper cover plate and lower cover；
The rotating shaft being rotatablely connected with the upper cover plate and lower cover, the chamber is driven during the axis of rotation to rotate,
Gas approach and N are offered on the upper cover plate2Import, exhanst gas outlet and N are provided with the lower cover2Outlet, the rotating shaft
Can drive multiple chambers turn to the gas approach and exhanst gas outlet with one of chamber and the N2
Import and N2Outlet with another chamber.
Preferably, in above-mentioned revolution bed activated coke absorption regeneration integration multi-pollutant removing device, the chamber
Quantity is two, and the chamber is semi-cylindrical, and two chambers are collectively forming columned revolution bed.
Preferably, in above-mentioned revolution bed 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 with the side wall of the chamber and are opened and closed with the window
The shrouding of cooperation, the backing plate with holes can be extracted out by the window.
Preferably, in above-mentioned revolution bed activated coke absorption regeneration integration multi-pollutant removing device, the shrouding with
The backing plate with holes is fixedly connected.
Preferably, in above-mentioned revolution bed activated coke absorption regeneration integration multi-pollutant removing device, multiple windows
Mouth layer distributed, and every layer of multiple windows are uniformly distributed from top to bottom.
Preferably, in above-mentioned revolution bed 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 activated coke absorption regeneration integration multi-pollutant removing device, the upper cover plate
Bottom side and lower cover on the upside of be respectively provided with annular slot, the top and bottom of the chamber are stretched into the annular slot.
Preferably, in above-mentioned revolution bed activated coke absorption regeneration integration multi-pollutant removing device, the rotating shaft is led to
Bearing is crossed to be rotatablely connected with the upper cover plate and lower cover.
Revolution bed activated coke absorption regeneration integration multi-pollutant removing device provided by the invention includes chamber, upper lid
Plate, lower cover and rotating shaft.The quantity of its middle chamber is multiple, and chamber is used to fill adsorption particle, and adsorption particle is specifically as follows
Activated coke filling ball.Multiple chambers are separate, i.e. any two chamber interior does not connect；Multiple chambers circumferentially to point
Cloth, 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
It is tightly connected, and chamber can rotate relative to upper cover plate and lower cover.I.e. upper cover plate and lower cover are fixed and multiple
Chamber can rotate, and so can support upper cover plate and lower cover by support etc..
Rotating shaft is rotatablely connected with upper cover plate and lower cover, i.e. rotating shaft can rotate relative to upper cover plate and lower cover, turn
Axle drives multiple chambers while rotated when rotating.Gas approach and N are offered on upper cover plate2Import, cigarette is provided with lower cover
Gas exports and N2Outlet.Rotating shaft can drive multiple chambers turn to gas approach and exhanst gas outlet with one of chamber connect
Logical and N2Import and N2Outlet connects while N with another chamber, i.e. gas approach and exhanst gas outlet with same chamber2
Import and N2Outlet also connects with same chamber, and gas approach and N2Import connects with two chambers respectively.
During using revolution bed activated coke absorption regeneration integration multi-pollutant removing device provided by the invention, turn first
Turn axle, make gas approach and exhanst gas outlet with one of chamber and N2Import and N2Outlet with another chamber
Connection, now pending flue gas enter one of chamber through gas approach, from cigarette after the adsorption particle processing in chamber
Gas outlet discharge.Meanwhile through N2Import fills N into another chamber2, the gas being filled with is through N2Outlet discharge, is realized to another with this
The regeneration of adsorption particle in one chamber.When the adsorption particle in the chamber that processing connects with gas approach needs regeneration,
Rotating shaft can be rotated further, the chamber for making to connect with gas approach originally turns to and N2Inlet communication.It is as described above, make
It can be handed over multiple chambers during revolution bed activated coke absorption regeneration integration multi-pollutant removing device provided by the invention
For processing flue gas and pour N2Regeneration, it is not necessary to individually designed adsorption tower and Analytic Tower again, greatly reduce activated coke regeneration cost.
Brief description of the drawings
In order to illustrate more clearly about the embodiment of the present invention or technical scheme of the prior art, below will be to embodiment or existing
There is the required accompanying drawing used in technology description to be briefly described, it should be apparent that, drawings in the following description are only this
Some embodiments of invention, for those of ordinary skill in the art, on the premise of not paying creative work, can be with
Other accompanying drawings are obtained according to these accompanying drawings.
Fig. 1 is revolution bed activated coke absorption regeneration integration multi-pollutant removing device provided in an embodiment of the present invention
Top view；
Fig. 2 is revolution bed activated coke absorption regeneration integration multi-pollutant removing device provided in an embodiment of the present invention
Sectional view；
Fig. 3 is revolution bed activated coke absorption regeneration integration multi-pollutant removing device provided in an embodiment of the present invention
Front view.
In fig. 1-3：
1- upper cover plates, 2-N2Import, 3- rotating shafts, 4- gas approach, 5- chambers, 6- adsorption particles, 7-N2Outlet, 8- flue gases
Outlet, 9- backing plates with holes, 10- shroudings.
Embodiment
It is an object of the invention to provide one kind to turn round bed activated coke absorption regeneration integration multi-pollutant removing device,
The structure design of the revolution bed activated coke absorption regeneration integration multi-pollutant removing device can efficiently solve activated coke
The problem of regeneration cost is higher.
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Site preparation describes, it is clear that described embodiment is only part of the embodiment of the present invention, rather than whole embodiments.It is based on
Embodiment in the present invention, those of ordinary skill in the art are obtained every other under the premise of creative work is not made
Embodiment, belong to the scope of protection of the invention.
In the description of the invention, it is to be understood that term " on ", " under ", "front", "rear", " left side " and " right side " etc. refer to
The orientation or position relationship shown is based on orientation shown in the drawings or position relationship, is for only for ease of the description present invention and simplifies
Description, rather than the position or element of instruction or hint meaning must have particular orientation, be formed and be operated with specific orientation,
Therefore it is not intended that the limitation of the present invention.In addition, term " first ", " second " be only used for describe purpose, and it is not intended that
Instruction implies relative importance.
Refer to Fig. 1-Fig. 3, revolution bed activated coke absorption regeneration integration multi-pollutant provided in an embodiment of the present invention
Removing means includes chamber 5, upper cover plate 1, lower cover and rotating shaft 3.The quantity of its middle chamber 5 is multiple, and chamber 5, which is used to fill, to be inhaled
Attached particle 6, adsorption particle 6 are specifically as follows activated coke filling ball.Multiple chambers 5 are separate, i.e., inside any two chamber 5
Do not connect；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 5
End sealing is connected, and lower cover is connected with the bottom end seal of chamber 5, and chamber 5 can turn relative to upper cover plate 1 and lower cover
It is dynamic.I.e. upper cover plate 1 and lower cover are fixed and multiple chambers 5 can rotate, and can so pass through support etc. and support upper cover plate 1
And lower cover.
Rotating shaft 3 is rotatablely connected with upper cover plate 1 and lower cover, i.e. rotating shaft 3 can turn relative to upper cover plate 1 and lower cover
Dynamic, rotating shaft 3 drives multiple chambers 5 while rotated when rotating.Gas approach 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.Rotating shaft 3 can drive that multiple chambers 5 turn to gas approach 4 and exhanst gas outlet 8 is equal
Connected with one of chamber 5 and N2 imports 2 and N2 outlets 7 connect with another chamber 5, i.e., gas approach 4 and flue gas go out
Mouth 8 connects with same chamber 5 while N2 imports 2 and N2 outlets 7 also connect with same chamber 5, and gas approach 4 and N2 imports
2 connect with two chambers 5 respectively.
During using revolution bed activated coke absorption regeneration integration multi-pollutant removing device provided in an embodiment of the present invention,
Rotating shaft 3 first, makes that gas approach 4 and exhanst gas outlet 8 connect with one of chamber 5 and N2 imports 2 and N2 outlets are 7 equal
Connected with another chamber 5, now pending flue gas enters one of chamber 5 through gas approach 4, through the suction in chamber 5
Attached particle 6 is discharged after handling from exhanst gas outlet 8.Meanwhile fill N into another chamber 5 through N2 imports 22, the gas being filled with is through N2
The discharge of outlet 7, the regeneration to the adsorption particle 6 in another chamber 5 is realized with this.When the chamber that processing connects with gas approach 4
When adsorption particle 6 in room 5 needs regeneration, rotating shaft 3 can be rotated further, the chamber 5 for making to connect with gas approach 4 originally turns to
Connected with N2 imports 2.It is as described above, it is how dirty using revolution bed activated coke absorption regeneration integration provided by the invention
Multiple chambers 5 alternate treatment flue gas and can pour N during dye thing removing means2Regeneration, it is not necessary to again individually designed 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
It is collectively forming columned revolution bed.So only need two chambers 5 alternately to be connected with gas approach 4, also easily facilitate
Driving revolution bed rotates.Certainly, the quantity of chamber 5 can also be three or more, be not limited thereto.
When the usage time of adsorption particle 6 is long to be regenerated, it is necessary to change adsorption particle 6.Adsorbed for the ease of changing
Particle 6, the inside of chamber 5 can from top to bottom be provided with multilayer backing plate 9 with holes, multiple windows is provided with the side wall of chamber 5
With the shrouding 10 coordinated with window opening and closing, backing plate 9 with holes can be extracted out by window.Wherein, shrouding 10 can block window
Mouthful, every layer of top of backing plate with holes 9 be filled with adsorption particle 6, after the unlatching of shrouding 10 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 the inside of chamber 5 again after changing adsorption particle 6.
Further, shrouding 10 can be fixedly connected with backing plate 9 with holes, and such shrouding 10 can be set with backing plate 9 with holes
It is the movement that shrouding 10 and backing plate 9 with holes can be achieved by pull for drawer type.Certainly, shrouding 10 is it can also be provided that door-plate
Shape, opening and closing of fault is realized by rotating shrouding 10, is not limited thereto.
As shown in figure 3, in above-described embodiment, multiple windows layer distributed, and every layer of multiple windows are uniform from top to bottom
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
Limit.
In order to realize the sealing of upper cover plate 1 and lower cover and the diameter of chamber 5, the bottom side of upper cover plate 1 has 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 of chamber 5
In the annular slot of plate, coordinate thus by the grafting 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, rotating shaft 3 is rotatablely connected by bearing and upper cover plate 1 and lower cover, to reduce the frictional force of rotating shaft 3,
Reduce abrasion.
Each embodiment is described by the way of progressive in this specification, what each embodiment stressed be and other
The difference of embodiment, between each embodiment identical similar portion mutually referring to.
The foregoing description of the disclosed embodiments, professional and technical personnel in the field are enable to realize or using the present invention.
A variety of modifications to these embodiments will be apparent for those skilled in the art, as defined herein
General Principle can be realized in other embodiments without departing from the spirit or scope of the present invention.Therefore, it is of the invention
The embodiments shown herein is not intended to be limited to, and is to fit to and principles disclosed herein and features of novelty phase one
The most wide scope caused.
Claims (8)
1. one kind revolution bed activated coke absorption regeneration integration multi-pollutant removing device, it is characterised in that including：
Separate multiple chambers (5) for being used to fill adsorption particle (6), multiple chambers (5) are circumferentially to distribution；
Upper cover plate (1) and lower cover, the upper cover plate (1) and the lower cover top with the chamber (5) and bottom end seal respectively
Connection, and the chamber (5) can rotate relative to the upper cover plate (1) and lower cover；
The rotating shaft (3) being rotatablely connected with the upper cover plate (1) and lower cover, the rotating shaft (3) drive the chamber when rotating
(5) rotate, offer gas approach (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 N2 outlets (7), the rotating shaft (3) can drive multiple chambers (5) to turn to the gas approach (4) and cigarette
Gas outlet (8) connects with one of chamber (5) and the N2 imports (2) and N2 outlets (7) connect with another chamber (5)
It is logical.
2. revolution bed activated coke absorption regeneration integration multi-pollutant removing device according to claim 1, its feature
It is, the quantity of the chamber (5) is two, and the chamber (5) is semi-cylindrical, and two chambers (5) are collectively forming
Columned revolution bed.
3. revolution bed activated coke absorption regeneration integration multi-pollutant removing device according to claim 1, its feature
It is, the inside of the chamber (5) is from top to bottom provided with multilayer backing plate with holes (9), is provided with the side wall of the chamber (5)
Multiple windows and the shrouding (10) coordinated with window opening and closing, the backing plate (9) with holes can be extracted out by the window.
4. revolution bed activated coke absorption regeneration integration multi-pollutant removing device according to claim 3, its feature
It is, the shrouding (10) is fixedly connected with the backing plate (9) with holes.
5. revolution bed activated coke absorption regeneration integration multi-pollutant removing device according to claim 3, its feature
It is, multiple windows layer distributed, and every layer of multiple windows are uniformly distributed from top to bottom.
6. revolution bed activated coke absorption regeneration integration multi-pollutant removing device according to claim 3, its feature
It is, the through-hole diameter of the backing plate (9) with holes is less than 50mm.
7. revolution bed activated coke absorption regeneration integration multi-pollutant removing device according to claim 1, its feature
It is, annular slot, the top and bottom of the chamber (5) is respectively provided with the upside of the bottom side of the upper cover plate (1) and lower cover
Stretch into the annular slot.
8. revolution bed activated coke absorption regeneration integration multi-pollutant removing device according to claim 1, its feature
It is, the rotating 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 |
|---|---|---|---|
| CN201711216647.8A CN107803096A (en) | 2017-11-28 | 2017-11-28 | One kind revolution bed activated coke absorption regeneration integration multi-pollutant removing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711216647.8A CN107803096A (en) | 2017-11-28 | 2017-11-28 | One kind revolution bed activated coke absorption regeneration integration multi-pollutant removing device |
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| Publication Number | Publication Date |
|---|---|
| CN107803096A true CN107803096A (en) | 2018-03-16 |
Family
ID=61590358
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711216647.8A Pending CN107803096A (en) | 2017-11-28 | 2017-11-28 | One kind revolution bed activated coke absorption regeneration integration multi-pollutant removing device |
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| CN (1) | CN107803096A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108939912A (en) * | 2018-08-15 | 2018-12-07 | 西安热工研究院有限公司 | One kind being based on helicoid combined desulfurization and denitration arrangement system |
| CN109695891A (en) * | 2018-05-30 | 2019-04-30 | 中电华创(苏州)电力技术研究有限公司 | One kind dividing the rotary clarifier in storehouse and flue gas purification system |
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| CN201681634U (en) * | 2010-03-18 | 2010-12-22 | 中国船舶重工集团公司第七一八研究所 | Self-running dehydrogenation device provided with breather holes and interlayered housing |
| CN205517117U (en) * | 2016-01-25 | 2016-08-31 | 浙江吴越人家新材料有限公司 | Active carbon exhaust treatment device |
| US20160271556A1 (en) * | 2015-03-20 | 2016-09-22 | Seibu Giken Co., Ltd. | Gas recovery concentration apparatus |
| CN207822740U (en) * | 2017-11-28 | 2018-09-07 | 国电环境保护研究院有限公司 | A kind of revolution bed type activated coke absorption regeneration integration multi-pollutant removing device |
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2017
- 2017-11-28 CN CN201711216647.8A patent/CN107803096A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
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| JPH0691128A (en) * | 1992-09-14 | 1994-04-05 | Mitsubishi Heavy Ind Ltd | Continuous gas separation and recovery device |
| CN201681634U (en) * | 2010-03-18 | 2010-12-22 | 中国船舶重工集团公司第七一八研究所 | Self-running dehydrogenation device provided with breather holes and interlayered housing |
| US20160271556A1 (en) * | 2015-03-20 | 2016-09-22 | Seibu Giken Co., Ltd. | Gas recovery concentration apparatus |
| CN205517117U (en) * | 2016-01-25 | 2016-08-31 | 浙江吴越人家新材料有限公司 | Active carbon exhaust treatment device |
| CN207822740U (en) * | 2017-11-28 | 2018-09-07 | 国电环境保护研究院有限公司 | A kind of revolution bed type activated coke absorption regeneration integration multi-pollutant removing device |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109695891A (en) * | 2018-05-30 | 2019-04-30 | 中电华创(苏州)电力技术研究有限公司 | One kind dividing the rotary clarifier in storehouse and flue gas purification system |
| CN108939912A (en) * | 2018-08-15 | 2018-12-07 | 西安热工研究院有限公司 | One kind being based on helicoid combined desulfurization and denitration arrangement system |
| CN108939912B (en) * | 2018-08-15 | 2024-01-23 | 西安热工研究院有限公司 | Combined desulfurization and denitrification arrangement system based on rotation |
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Address after: 210031 Pudong Road, Pukou District, Jiangsu, No. 10, No. Applicant after: National Electric Environmental Protection Research Institute Co., Ltd. Address before: 210000 Pudong Road, Pukou District, Jiangsu, No. 10, No. Applicant before: State Power Environmental Protection Research Institute |