CN107824013A - A kind of injection turbulent contact absorber - Google Patents
A kind of injection turbulent contact absorber Download PDFInfo
- Publication number
- CN107824013A CN107824013A CN201711268250.3A CN201711268250A CN107824013A CN 107824013 A CN107824013 A CN 107824013A CN 201711268250 A CN201711268250 A CN 201711268250A CN 107824013 A CN107824013 A CN 107824013A
- Authority
- CN
- China
- Prior art keywords
- absorption tower
- dividing plate
- injection
- gas
- spraying layer
- 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.)
- Pending
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Classifications
-
- 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
- B01D53/14—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 absorption
- B01D53/1456—Removing acid components
- B01D53/1481—Removing sulfur dioxide or sulfur trioxide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
- B01D47/12—Washers with plural different washing sections
-
- 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
- B01D53/14—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 absorption
- B01D53/1406—Multiple stage absorption
-
- 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
- B01D53/14—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 absorption
- B01D53/18—Absorbing units; Liquid distributors therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2247/00—Details relating to the separation of dispersed particles from gases, air or vapours by liquid as separating agent
- B01D2247/10—Means for removing the washing fluid dispersed in the gas or vapours
-
- 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
Abstract
The invention discloses a kind of injection turbulent contact absorber, including absorption tower body, the top of absorption tower body has gas approach and exhanst gas outlet, and the intrinsic top in absorption tower has dividing plate, and gas approach is located at the side of dividing plate, and exhanst gas outlet is located at the opposite side of dividing plate；The top of absorption tower body is separated into separate inlet flue duct and exhaust pass by dividing plate, is provided with injection turbulator in inlet flue duct, the lower section of dividing plate has gas-liquid separation pond；Homogenizing plate, spraying layer and demister are provided with exhaust pass, demister is located at the top of spraying layer, and spraying layer is located at the top of homogenizing plate.Flue gas and drop can be sufficiently mixed by the present invention in absorption tower, so as to improve the clean-up effect on absorption tower.Designed more than, can effectively reduce absorption tower height degree, and the flue gas resistance on absorption tower can be reduced, reduce the operation energy consumption on absorption tower, and the station service power consumption rate of desulphurization system.
Description
Technical field
The present invention relates to a kind of injection turbulent contact absorber, belong to flue gases purification field.
Background technology
Absorption tower is the equipment for realizing absorption operation.It is divided into three classes by the gas-liquid form that is in contact.The first kind is gas with gas
Steep scattered plate column, bubble absorbing tower, the stirring bubble absorbing tower in the liquid phase of form；Second class is that liquid is disperseed with droplet-like
Injector, spray tower in the gas phase；3rd class is that liquid moves the packed absorber contacted with gas phase and drop with membranaceous
Film absorption tower.In tower the type of flow of gas-liquid two-phase can adverse current also can cocurrent.Generally use counter-current operation, absorbent is with tower top
Addition is flowed from top to bottom, is contacted with the gas flowed from bottom to top, and the liquid for absorbing absorbent is discharged from bottom of towe, after purification
Gas from tower top discharge.So flue gas and liquid to be sufficiently mixed to the filtering that can promote flue gas in absorption tower, improve and inhale
Receive the clean-up effect of tower.
The content of the invention
It is an object of the present invention to provide a kind of injection turbulent contact absorber, flue gas and drop can be filled in absorption tower
Divide mixing, so as to improve the clean-up effect on absorption tower.
In order to solve the above technical problems, the present invention adopts the following technical scheme that：
A kind of injection turbulent contact absorber, including absorption tower body, the top of absorption tower body have gas approach and flue gas
Outlet, the intrinsic top in absorption tower have dividing plate, and gas approach is located at the side of dividing plate, and exhanst gas outlet is located at the another of dividing plate
Side；The top of absorption tower body is separated into separate inlet flue duct and exhaust pass by dividing plate, is provided with and draws in inlet flue duct
Turbulator is penetrated, the lower section of dividing plate has gas-liquid separation pond；Homogenizing plate, spraying layer and demister, demister are provided with exhaust pass
Positioned at the top of spraying layer, spraying layer is located at the top of homogenizing plate.
In a kind of foregoing injection turbulent contact absorber, injection turbulator is made up of distribution webmaster, nozzle and Venturi tube, point
Lower section with webmaster connects some nozzles, and the lower section of each nozzle is provided with a Venturi tube.
In a kind of foregoing injection turbulent contact absorber, Venturi tube is by the inlet tube, trunnion and anemostat group that are sequentially communicated
Into.
In a kind of foregoing injection turbulent contact absorber, the quantity of spraying layer is more than or equal to 2.
The deflector being obliquely installed is provided with a kind of foregoing injection turbulent contact absorber, in inlet flue duct at gas approach.
There is the angle more than 30 degree in a kind of foregoing injection turbulent contact absorber, between deflector and horizontal plane.
In a kind of foregoing injection turbulent contact absorber, the lower end of anemostat and the lower end of dividing plate flush.
In a kind of foregoing injection turbulent contact absorber, homogenizing plate is provided with some equally distributed through holes.
Compared with prior art, flue gas and drop can be sufficiently mixed by the present invention in absorption tower, be absorbed so as to improve
The clean-up effect of tower.Flue gas at the top of absorption tower by entering, being vigorously mixed, conducting heat, mass transfer through injection turbulator progress liquid phase
Afterwards, the atmosphere pollutions such as most of SO2, SO3 and flue dust are removed.Again through gas-liquid separation section, by a large amount of drops and cigarette in flue gas
Gas is separated.Flue gas after separation enters back into flue gas spray washing system, to remove after homogenizing plate carries out flue gas even distribution
Remaining atmosphere pollution.The flue gas of a large amount of drops is carried through high efficiency demister, after removing a large amount of drops in flue gas, neat stress
Discharged again by the net flue of tower top.Designed more than, can effectively reduce absorption tower height degree, and the cigarette on absorption tower can be reduced
Atmidometer, reduce the operation energy consumption on absorption tower, and the station service power consumption rate of desulphurization system.
Brief description of the drawings
Fig. 1 is a kind of structural representation of embodiment of the present invention；
Fig. 2 is a kind of structural representation of embodiment of injection turbulator.
Reference：1- exhanst gas outlets, 2- dividing plates, 3- gas approach, 4- absorption towers body, 5- injection turbulators, 6- gas
Liquid separate tank, 7- demisters, 8- spraying layers, 9- homogenizing plates, 10- nozzles, 11- distribution webmasters, 12- inlet tubes, 13- trunnions, 14-
Anemostat, 15- inlet flue ducts, 16- exhaust pass.
The present invention is further illustrated with reference to the accompanying drawings and detailed description.
Embodiment
Embodiments of the invention 1：As depicted in figs. 1 and 2, a kind of injection turbulent contact absorber, including absorption tower body 4, inhale
Receiving the top of tower body 4 has a gas approach 3 and exhanst gas outlet 1, and the top in absorption tower body 4 has dividing plate 2, gas approach
3 are located at the side of dividing plate 2, and exhanst gas outlet 1 is located at the opposite side of dividing plate 2；The top of absorption tower body 4 is separated into phase by dividing plate 2
Mutually independent inlet flue duct 15 and exhaust pass 16, inlet flue duct 15 is interior to be provided with injection turbulator 5, and the lower section of dividing plate 2 has gas
Liquid separate tank 6；Homogenizing plate 9, spraying layer 8 and demister 7 are provided with exhaust pass 16, demister 7 is located at the top of spraying layer 8,
Spraying layer 8 is located at the top of homogenizing plate 9.
Injection turbulator 5 is made up of distribution webmaster 11, nozzle 10 and Venturi tube, and the lower section connection of distribution webmaster 11 is some
Nozzle 10, the lower section of each nozzle 10 are provided with a Venturi tube.Venturi tube is by the inlet tube 12, the and of trunnion 13 that are sequentially communicated
Anemostat 14 forms.The quantity of spraying layer 8 is equal to 2.The deflector being obliquely installed is provided with inlet flue duct 15 at gas approach 3.
There is the angle equal to 30 degree between deflector and horizontal plane.The lower end of anemostat 14 and the lower end of dividing plate 2 flush.Homogenizing plate 9
It is provided with some equally distributed through holes.
Embodiment 2：As depicted in figs. 1 and 2, a kind of injection turbulent contact absorber, including absorption tower body 4, absorption tower body 4
Top there is gas approach 3 and exhanst gas outlet 1, the top in absorption tower body 4 has dividing plate 2, and gas approach 3 is located at dividing plate
2 side, exhanst gas outlet 1 are located at the opposite side of dividing plate 2；The top of absorption tower body 4 is separated into separate to enter by dividing plate 2
Mouth flue 15 and exhaust pass 16, inlet flue duct 15 is interior to be provided with injection turbulator 5, and the lower section of dividing plate 2 has gas-liquid separation pond 6；
Homogenizing plate 9, spraying layer 8 and demister 7 are provided with exhaust pass 16, demister 7 is located at the top of spraying layer 8, and spraying layer 8 is located at
The top of homogenizing plate 9.
Injection turbulator 5 is made up of distribution webmaster 11, nozzle 10 and Venturi tube, and the lower section connection of distribution webmaster 11 is some
Nozzle 10, the lower section of each nozzle 10 are provided with a Venturi tube.Venturi tube is by the inlet tube 12, the and of trunnion 13 that are sequentially communicated
Anemostat 14 forms.The quantity of spraying layer 8 is equal to 3.The deflector being obliquely installed is provided with inlet flue duct 15 at gas approach 3.
There is the angle equal to 35 degree between deflector and horizontal plane.The lower end of anemostat 14 and the lower end of dividing plate 2 flush.Homogenizing plate 9
It is provided with some equally distributed through holes.
Embodiment 3：As depicted in figs. 1 and 2, a kind of injection turbulent contact absorber, including absorption tower body 4, absorption tower body 4
Top there is gas approach 3 and exhanst gas outlet 1, the top in absorption tower body 4 has dividing plate 2, and gas approach 3 is located at dividing plate
2 side, exhanst gas outlet 1 are located at the opposite side of dividing plate 2；The top of absorption tower body 4 is separated into separate to enter by dividing plate 2
Mouth flue 15 and exhaust pass 16, inlet flue duct 15 is interior to be provided with injection turbulator 5, and the lower section of dividing plate 2 has gas-liquid separation pond 6；
Homogenizing plate 9, spraying layer 8 and demister 7 are provided with exhaust pass 16, demister 7 is located at the top of spraying layer 8, and spraying layer 8 is located at
The top of homogenizing plate 9.
Injection turbulator 5 is made up of distribution webmaster 11, nozzle 10 and Venturi tube, and the lower section connection of distribution webmaster 11 is some
Nozzle 10, the lower section of each nozzle 10 are provided with a Venturi tube.Venturi tube is by the inlet tube 12, the and of trunnion 13 that are sequentially communicated
Anemostat 14 forms.The quantity of spraying layer 8 is equal to 3.The deflector being obliquely installed is provided with inlet flue duct 15 at gas approach 3.
There is the angle equal to 40 degree between deflector and horizontal plane.The lower end of anemostat 14 and the lower end of dividing plate 2 flush.Homogenizing plate 9
It is provided with some equally distributed through holes.
A kind of operation principle of embodiment of the present invention：Injection turbulator 5 is the turbulent diffusion using jet, is made not
Two fluids with pressure is mutually mixed, and triggers the fluid machinery and mix reaction equipment of energy exchange.Injection turbulator 5 is led
To be made up of distribution pipe network 11, nozzle 10, inlet tube 12, trunnion 13 and anemostat 14.Into before device, high pressure slurries are with very high
Speed projected from nozzle 10, into inlet tube 12, due to the turbulent diffusion of jet, negative pressuren zone is formed in inlet tube 12
Domain, and roll up the low-pressure injection fluid around inhaling and momentum-exchange occurs.Working fluid and driving fluid are mixed mixing in trunnion,
Momentum, heat and mass exchange are carried out, it is gradually balanced in flow process medium velocity, also with the rise of pressure during this.Fluid
Out enter anemostat 14 from mixing chamber, pressure will continue to raise because flowing velocity slows down.In the exit of anemostat 14, mixing
The pressure of fluid is higher than the pressure of driving fluid when entering receiving chamber.Therefore, the pressure of the driving fluid of diffusion chamber outlet is relatively inhaled
Pressure before entrance will be higher by a lot.
Claims (8)
1. a kind of injection turbulent contact absorber, it is characterised in that including absorption tower body (4), the top of absorption tower body (4) has
Gas approach (3) and exhanst gas outlet (1), the top in absorption tower body (4) have dividing plate (2), and gas approach (3) is located at dividing plate
(2) side, exhanst gas outlet (1) are located at the opposite side of dividing plate (2)；The top of absorption tower body (4) is separated into phase by dividing plate (2)
Mutually independent inlet flue duct (15) and exhaust pass (16), inlet flue duct (15) is interior to be provided with injection turbulator (5), dividing plate (2)
Lower section has gas-liquid separation pond (6)；Homogenizing plate (9), spraying layer (8) and demister (7), demister are provided with exhaust pass (16)
(7) it is located at the top of spraying layer (8), spraying layer (8) is located at the top of homogenizing plate (9).
2. a kind of injection turbulent contact absorber according to claim 1, it is characterised in that injection turbulator (5) is by distribution net
(11), nozzle (10) and Venturi tube composition are managed, the lower section of distribution webmaster (11) connects some nozzles (10), each nozzle (10)
Lower section be provided with a Venturi tube.
3. a kind of injection turbulent contact absorber according to claim 2, it is characterised in that Venturi tube is entered by what is be sequentially communicated
Mouth pipe (12), trunnion (13) and anemostat (14) composition.
A kind of 4. injection turbulent contact absorber according to claim 2, it is characterised in that the quantity of spraying layer (8) be more than or
Person is equal to 2.
A kind of 5. injection turbulent contact absorber according to claim 2, it is characterised in that inlet flue duct (15) interior gas approach
(3) place is provided with the deflector being obliquely installed.
6. a kind of injection turbulent contact absorber according to claim 5, it is characterised in that have between deflector and horizontal plane
Angle more than 30 degree.
7. a kind of injection turbulent contact absorber according to claim 5, it is characterised in that the lower end of anemostat (14) and dividing plate
(2) lower end flushes.
8. a kind of injection turbulent contact absorber according to claim 5, it is characterised in that homogenizing plate (9) is provided with some equal
The through hole of even distribution.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711268250.3A CN107824013A (en) | 2017-12-05 | 2017-12-05 | A kind of injection turbulent contact absorber |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711268250.3A CN107824013A (en) | 2017-12-05 | 2017-12-05 | A kind of injection turbulent contact absorber |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107824013A true CN107824013A (en) | 2018-03-23 |
Family
ID=61641544
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711268250.3A Pending CN107824013A (en) | 2017-12-05 | 2017-12-05 | A kind of injection turbulent contact absorber |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107824013A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110841393A (en) * | 2019-11-29 | 2020-02-28 | 黄予欣 | Smoke removing method, moxibustion therapeutic device and tobacco smoke purifier |
| CN111780296A (en) * | 2020-06-09 | 2020-10-16 | 青岛海尔空调电子有限公司 | Air conditioning unit with spray cooling system |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR1373735A (en) * | 1963-08-02 | 1964-10-02 | Babcock & Wilcox Co | Device for contacting gases and liquids |
| CN1171747A (en) * | 1994-11-04 | 1998-01-28 | 环境关注国际有限公司 | Venturi scrubber and method with optimized remote spray |
| CN204799049U (en) * | 2015-05-19 | 2015-11-25 | 青岛科技大学 | Wet process micron order particulate matter entrapment air purification device |
| CN105916838A (en) * | 2013-11-15 | 2016-08-31 | 斯塔米卡邦有限公司 | An apparatus and method for particulate capture from gas streams and a method of removing soluble particulate from a gas |
| CN207576089U (en) * | 2017-12-05 | 2018-07-06 | 中国华电科工集团有限公司 | A kind of injection turbulent contact absorber |
-
2017
- 2017-12-05 CN CN201711268250.3A patent/CN107824013A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR1373735A (en) * | 1963-08-02 | 1964-10-02 | Babcock & Wilcox Co | Device for contacting gases and liquids |
| CN1171747A (en) * | 1994-11-04 | 1998-01-28 | 环境关注国际有限公司 | Venturi scrubber and method with optimized remote spray |
| CN105916838A (en) * | 2013-11-15 | 2016-08-31 | 斯塔米卡邦有限公司 | An apparatus and method for particulate capture from gas streams and a method of removing soluble particulate from a gas |
| CN204799049U (en) * | 2015-05-19 | 2015-11-25 | 青岛科技大学 | Wet process micron order particulate matter entrapment air purification device |
| CN207576089U (en) * | 2017-12-05 | 2018-07-06 | 中国华电科工集团有限公司 | A kind of injection turbulent contact absorber |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110841393A (en) * | 2019-11-29 | 2020-02-28 | 黄予欣 | Smoke removing method, moxibustion therapeutic device and tobacco smoke purifier |
| CN110841393B (en) * | 2019-11-29 | 2021-08-24 | 黄予欣 | Smoke removing method, moxibustion therapeutic device and tobacco smoke purifier |
| CN111780296A (en) * | 2020-06-09 | 2020-10-16 | 青岛海尔空调电子有限公司 | Air conditioning unit with spray cooling system |
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