CN206526647U - A kind of assembled moving bed adsorbent equipment - Google Patents
A kind of assembled moving bed adsorbent equipment Download PDFInfo
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- CN206526647U CN206526647U CN201720177075.6U CN201720177075U CN206526647U CN 206526647 U CN206526647 U CN 206526647U CN 201720177075 U CN201720177075 U CN 201720177075U CN 206526647 U CN206526647 U CN 206526647U
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- moving bed
- activated coke
- main body
- flue gas
- bed main
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Abstract
The utility model discloses a kind of assembled moving bed adsorbent equipment, including moving bed main body, the upper end of moving bed main body is activated coke entrance, and lower end exports for activated coke, it is characterised in that：Multiple isolation sieve plates are provided with along activated coke entrance to activated coke Way out in the moving bed main body, moving bed main body is divided into multiple active coke bins by isolation sieve plate；The moving bed body top is provided with exhanst gas outlet, and bottom is provided with smoke inlet, and smoke inlet is using gradual-enlargement type structure and provided with shutter, and exhanst gas outlet uses microwell plate structure.The moving bed adsorbent equipment that the utility model is provided has cross-flow and convection adsorption effect concurrently, overcome cross-flow in the prior art, the deficiency of convection apparatus, flue gas and Contact-sorption time of the activated coke in adsorption tower can be improved, flue gas intake resistance can be reduced again, purification efficiency is improved.
Description
Technical field
The utility model belongs to environmental technology field, is related to activated coke dry method flue gas Pollutant Control Technology, and in particular to
A kind of assembled moving bed adsorbent equipment, has cross-flow and convection adsorption effect concurrently, it is adaptable to while processing contains a variety of dirts
The flue gas of thing is contaminated, the integrated purifying of the multiple pollutants such as sulphur, nitre, dioxin, mercury and dust is realized.
Background technology
Activated coke dry method flue gas Pollutant Control Technology, it is possible to achieve desulfurization denitration demercuration is dust removal integrated, can also be removed
SO3, eliminate white cigarette.The technology does not consume water substantially, saves great lot of water resources, desulfuration byproduct is high concentration SO2, it is easy to resource
Change and utilize, this is the fairly obvious flue gas pollutant control technology of new generation of an advantage.Burnt in steel, metallurgy, electric power, rubbish
The multiple fields such as burning have great application prospect.
Activated coke dry method flue gas pollutant removing main processes are that flue gas is adsorbed by activated coke adsorbent equipment
Qualified discharge after purification, is made up of three parts, and one is the adsorption reaction Tower System for removing harmful substance, and two be that regeneration activity is burnt
Tower System is regenerated, three be the activated coke conveyor system that activated coke loopy moving between adsorption reaction tower and regenerator is used.
The technical process need to configure booster fan, be purified pending flue gas feeding activated coke mobile layer after boosting, activated coke is again
The high-concentration sulfur dioxide gas separated when raw enters byproduct recovery process device, is recovered as sulfuric acid or gypsum etc. valuable
Byproduct.
Activated coke dry method flue gas pollutant removing technology, key factor is the adsorption capacity of adsorption reaction, and adsorption capacity
Height depend on the burnt absorption property of adsorbent activity, disposable dress Jiao amount of adsorbent equipment, activated coke in adsorption tower
Contact-sorption time of holdup time, flue gas to be clean and activated coke etc..
Fig. 1 and Fig. 2 are respectively the relation in activated coke and flow of flue gas direction in the prior art.Flue gas is from activated coke in Fig. 1
The side of moving direction passes through activated coke, and this is cross-flow；Flue gas passes through activated coke from the opposite of activated coke moving direction in Fig. 2,
This is convection current.Cross-flow and convection current have respective shortcoming：(1) in cross-flow equipment, flue gas and activated coke time of contact are short, absorption effect
Rate is relatively low；(2) in convection apparatus, flue gas intake resistance is larger.
The content of the invention
The purpose of this utility model is to provide a kind of assembled moving bed adsorbent equipment, has cross-flow concurrently and convection adsorption is imitated
Really, to improve flue gas and Contact-sorption time of the activated coke in adsorption tower, while reducing flue gas intake resistance, purification effect is improved
Rate.
Above-mentioned purpose is achieved by the following technical solution：
A kind of assembled moving bed adsorbent equipment, including moving bed main body, the upper end of moving bed main body is activated coke entrance,
Lower end exports for activated coke, is sieved in the moving bed main body along activated coke entrance to activated coke Way out provided with multiple isolation
Moving bed main body is divided into multiple active coke bins by plate, isolation sieve plate；The moving bed body top is provided with exhanst gas outlet, and bottom is set
There is smoke inlet, smoke inlet is using gradual-enlargement type structure and provided with shutter, and exhanst gas outlet uses microwell plate structure.
Further, moving bed main body is cuboid.
Further, three are provided with the moving bed main body with sieve plate active coke bin spaced apart from each other is isolated, centre is
Main active coke bin, both sides are the active coke bin in side, and shutter and microwell plate structure are on the outer wall of the active coke bin in side.
Further, the gradual-enlargement type structure is exported to activated coke Way in flaring from activated coke.This design feature
The flowing diffusion for coordinating shutter to contribute to flue gas to enter after moving bed adsorbent equipment, when increasing the contact with activated coke
Between, meanwhile, adsorbent activity Jiao in moving bed is difficult to leak from smoke inlet.
Further, moving bed main body is from top to bottom divided into exhanst gas outlet section, flue gas adsorption section, smoke inlet section.
Further, the exhanst gas outlet section width is less than flue gas adsorption section.So, formed on the outside of microwell plate for dropping
Flue gas discharges the cushion space of resistance after low purification, and the cushion space is also convenient for connecting with the smoke discharging pipe located at smoke outlet
Connect.
The beneficial effects of the utility model：
1st, isolation sieve plate activated coke spaced apart from each other is used provided with multiple in the moving bed adsorbent equipment that the utility model is provided
Storehouse, each activity coke bin uses single batcher discharge, and batcher is by VFC, and speed is adjustable, and each active coke bin is all
The holdup time of activated coke can be set respectively and the optimal holdup time can be set according to flue gas condition；
2nd, the moving bed adsorbent equipment that the utility model is provided has cross-flow and convection adsorption effect concurrently, overcomes prior art
Middle cross-flow, the deficiency of convection apparatus, can improve flue gas and Contact-sorption time of the activated coke in adsorption tower, cigarette can be reduced again
Gas intake resistance, improves purification efficiency.
Brief description of the drawings
Fig. 1 is that (wherein, A is activated coke entrance to cross-flow devices schematic diagram of the prior art, and B exports for activated coke, and C is
Smoke inlet, D is exhanst gas outlet)；
Fig. 2 is that (wherein, E is activated coke entrance or exhanst gas outlet to convection device schematic diagram of the prior art, and F is activity
Jiao outlet or smoke inlet)；
Fig. 3 is the utility model schematic device (wherein, 1, activated coke entrance；2nd, activated coke is exported；3rd, smoke inlet
Section；4th, exhanst gas outlet section；5th, flue gas adsorption section；6th, main active coke bin；7th, the active coke bin in side；8th, the smoke inlet of blind shaped；
9th, microwell plate；10th, sieve plate is isolated；11st, cushion space).
Embodiment
The technical solution of the utility model is specifically introduced below in conjunction with the accompanying drawings.
A kind of assembled moving bed adsorbent equipment as shown in Figure 3, including moving bed main body, one end of moving bed main body is
Activated coke entrance 1, the other end is to be provided with three in activated coke outlet 2, the moving bed main body to be spaced from each other with isolation sieve plate 10
Active coke bin, isolation sieve plate 10 is perpendicular to activated coke entrance 1 and activated coke outlet 2, active coke bin 6 based on centre, and both sides are
Side activity coke bin 7, smoke inlet 1 and exhanst gas outlet 2 are located at the outside of the active coke bin 7 in side；The nearly activated coke of moving bed main body
Outlet is between smoke inlet section and exhanst gas outlet section provided with exhanst gas outlet section 4 provided with smoke inlet section 3, nearly activated coke entrance
Flue gas adsorption section 5, the side of the smoke inlet section is provided with smoke inlet 8, and smoke inlet is using gradual-enlargement type structure and provided with hundred
Leaf window；The outside of the exhanst gas outlet section is provided with the structure of microwell plate 9 discharged for flue gas, simultaneously because exhanst gas outlet 4 width of section
Less than flue gas adsorption section 5, the outside of microwell plate 9 forms the cushion space 11 that resistance is discharged for reducing flue gas after purification, is also convenient for
It is connected with the smoke discharging pipe located at smoke outlet.Smoke inlet contributes to flue gas to enter using gradual-enlargement type respective outer side edges shutter
Flowing diffusion after moving bed adsorbent equipment, increase and the time of contact of activated coke.
In one particular arrangement, the moving bed main body is cuboid (10m × 3m × 23m).
The utility model provide moving bed adsorbent equipment in provided with three with isolation sieve plate active coke bin spaced apart from each other,
Each activity coke bin uses single batcher discharge, and batcher is by VFC, and speed is adjustable, and each active coke bin can divide
Not She Ding activated coke holdup time and optimal holdup time can be set according to flue gas condition.The movement that the utility model is provided
Bed adsorbent equipment has cross-flow and convection adsorption effect concurrently, overcomes cross-flow in the prior art, the deficiency of convection apparatus, can improve
Flue gas and Contact-sorption time of the activated coke in adsorption tower, flue gas intake resistance can be reduced again, improve purification efficiency.
The effect of above-described embodiment is only that explanation essentiality content of the present utility model, but does not limit this practicality with this
New protection domain.It will be understood by those within the art that, the technical solution of the utility model can be repaiied
Change or equivalent substitution, without departing from the essence and protection domain of technical solutions of the utility model.
Claims (6)
1. a kind of assembled moving bed adsorbent equipment, including moving bed main body, the upper end of moving bed main body is activated coke entrance, under
Hold and exported for activated coke, it is characterised in that：Along activated coke entrance to activated coke Way out provided with many in the moving bed main body
Moving bed main body is divided into multiple active coke bins by individual isolation sieve plate, isolation sieve plate；The moving bed body top goes out provided with flue gas
Mouthful, bottom is provided with smoke inlet, and smoke inlet is using gradual-enlargement type structure and provided with shutter, and exhanst gas outlet is hardened using micropore
Structure.
2. assembled moving bed adsorbent equipment according to claim 1, it is characterised in that：Moving bed main body is cuboid.
3. assembled moving bed adsorbent equipment according to claim 2, it is characterised in that：It is provided with the moving bed main body
Three with isolation sieve plate active coke bin spaced apart from each other, active coke bin based on centre, both sides are the active coke bin in side, shutter
With microwell plate structure on the outer wall of the active coke bin in side.
4. according to any described assembled moving bed adsorbent equipments of claim 1-3, it is characterised in that：The gradual-enlargement type structure
Exported from activated coke to activated coke Way in flaring.
5. according to any described assembled moving bed adsorbent equipments of claim 1-3, it is characterised in that：Moving bed main body is by upper
Exhanst gas outlet section, flue gas adsorption section, smoke inlet section are divided under.
6. according to any described assembled moving bed adsorbent equipment of claim 5, it is characterised in that：The exhanst gas outlet section is wide
Degree is less than flue gas adsorption section.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720177075.6U CN206526647U (en) | 2017-02-27 | 2017-02-27 | A kind of assembled moving bed adsorbent equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720177075.6U CN206526647U (en) | 2017-02-27 | 2017-02-27 | A kind of assembled moving bed adsorbent equipment |
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| Publication Number | Publication Date |
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| CN206526647U true CN206526647U (en) | 2017-09-29 |
Family
ID=59919583
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| Application Number | Title | Priority Date | Filing Date |
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| CN201720177075.6U Active CN206526647U (en) | 2017-02-27 | 2017-02-27 | A kind of assembled moving bed adsorbent equipment |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106669359A (en) * | 2017-02-27 | 2017-05-17 | 国电科学技术研究院 | Adsorption device for combined movable bed |
-
2017
- 2017-02-27 CN CN201720177075.6U patent/CN206526647U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106669359A (en) * | 2017-02-27 | 2017-05-17 | 国电科学技术研究院 | Adsorption device for combined movable bed |
| CN106669359B (en) * | 2017-02-27 | 2022-08-02 | 国电科学技术研究院有限公司 | Combined moving bed adsorption device |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 210000 Qixia, Jiangsu province Wen Dong Dong Road, No. 1, No. Patentee after: National Electric Science and Technology Research Institute Co., Ltd. Address before: 210000 Qixia, Jiangsu province Wen Dong Dong Road, No. 1, No. Patentee before: Guodian Science and Technology Research Institute |