CN103127813A - Absorbing and digesting tower - Google Patents
Absorbing and digesting tower Download PDFInfo
- Publication number
- CN103127813A CN103127813A CN2012101137322A CN201210113732A CN103127813A CN 103127813 A CN103127813 A CN 103127813A CN 2012101137322 A CN2012101137322 A CN 2012101137322A CN 201210113732 A CN201210113732 A CN 201210113732A CN 103127813 A CN103127813 A CN 103127813A
- Authority
- CN
- China
- Prior art keywords
- tower
- sedimentation basin
- assimilating
- cone
- absorbing
- 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
Links
Images
Abstract
Disclosed is an absorbing and digesting tower. Gas discharged by a gas burning chamber and other solid fuel ignition taking coal and the like as fuel is absorbed and utilized. Greenhouse gas emission is reduced, air is purified, and environment is improved and protected. The tower is a cylinder body or designed to be a cone, a frustum or space solid geometry formed by combination of the cylinder body, the cone and the frustum. Propellers, a releaser and a water blocking device are installed in the tower, and a settling pond is arranged outside a tower body.
Description
One, technical field
The present invention designs a kind of tower of assimilating.
Two, background technology
According to chemical principle, the waste gas that burning is discharged to gas combustion and other incendiary materials absorbs.Reduce greenhouse gas emission, purify air, improve environment.
Three, the content of tower is digested and assimilated in invention
The purpose of this invention:
Purpose of the present invention is to provide a kind of tower of assimilating, and utilizes chemical principle, and the waste gas with discharging after gas or other fuel combustions absorbs.In order to avoid air pollution works the mischief to the mankind and other life of the earth, reduce greenhouse gas emission.The mankind are lived in clean clean environment.
The technical scheme of assimilating tower that this invention provides;
The tower of assimilating provided by the invention is characterized in that; This tower is cylinder, the body that also can be designed to other solids such as centrum, stage body and mutually be combined by these aggregates.Assimilate the lime aqueous solution of rotational flow in tower; This solution each sedimentation basin outside tower bottom is flowed through tower.Then with the limewash clarified in sedimentation basin again Hui Xun in the absorption tower.Unabsorbed residual gas is arranged at sedimentation basin top, follows to assimilate through back of pipeline and continues digestion in tower.And constantly replenish fresh lime aqueous solution and catalyst, the chemical reaction in accelerated tower in assimilating tower.
Assimilate the brief introduction of tower
1. assimilate tower, applicable cylindricality tower body also can be designed to other geometries.Its size is determined according to putting into practice needs.Waste gas to the gas combustion chamber discharging is assimilated.
2. this tower is divided into reaction tower, outer circulation sedimentation basin etc.As adopt coal and other solid fuel ignitions, the outfit deduster of still needing.
3. constantly inject lime aqueous solution in reaction tower, circulate in tower through the screw agitate water.The annular release of waste gas after dedusting (waste gas of gas combustion chamber discharge does not need dedusting) with high-pressure pump in tower discharges, and carries out chemical reaction in tower, and namely calcium oxide and carbon dioxide reaction, generate precipitation of calcium carbonate.The top of pipeline, the interior automatic switch valve that arranges prevents liquid refluence air inlet height press pump in tower.
4. for accelerating chemical reaction, can the lime aqueous solution that flow in tower be heated or the input catalyst.
5. in tower, solution stirs by screw and Ta Nei water deflector, and it is fully mixed.
6. in reaction tower, mixing material injects sedimentation basin through the tower bottom pipeline, then other sedimentation basins of flowing through.
7. the aqueous solution of clarification adds a certain amount of lime, then the reaction tower that refluxes, and is recycling successively.
8. sedimentation basin can design a plurality of being connected according to actual needs, and still unreacted waste gas, proceed chemical reaction in back of pipeline follows reaction tower.
9. the water deflector of reaction tower inwall, more fully mix the interior aqueous solution of tower.
10. the sediment in sedimentation basin, discharge by following floss hole.Put into the things such as some chips or the rope made of hemp in the pond in solution, be convenient to adsorb the oxides such as calcium carbonate.
11. deduster is for what design take coal and other solid fuels as comburant, its quantity is decided according to the flue dust scale.The device of giving a dinner of welcome by several small-sized disjunctors consists of, and can fully clean.Bag filter is laid in deduster slag dirt exit.
12. annular release, assimilating at this has two kinds of purposes in system; If several spray nozzles are installed in the above, inject current, can make the sprayer unit of dust catcher inside; If some nozzles are installed in the above, be used in the reflection tower, be the exhaust emission device in reaction tower.
The manufacturing of annular release is to be made of the round tubular of hollow.Its size, thickness are determined according to actual needs.
Beneficial effect of the present invention
This invention can be assimilated burning to the gases such as carbon dioxide of airborne release, thereby reduces the discharging of carbon dioxide, purify air, and protection of the environment, the speed that has effectively stoped earth environment to warm strengthens health.
Four, description of drawings
Fig. 1: reaction tower schematic diagram.Wherein: 1. high-pressure pump; 2. breather line; 3. automatic switch valve; 4. liquid injection hole; 5. pump chamber; 6. screw; 7. annular release; 8. reaction tower; 9. support column; 15. water deflector.
Fig. 2: sedimentation basin schematic diagram.Wherein: 10. air-returen flue; 11. delivery port; 12. sedimentation basin; 13. switch.
Fig. 3: sedimentation basin schematic diagram.Wherein: 14. sedimentation basins.
Fig. 4: deduster schematic diagram.Wherein: 16 ventholes; 17. water inlet; 18. spray nozzle; 19. advance mouth; The dirt mouth 20. slag tap; 21. slag dirt general export; 22. switch valve; 26. annular release; 27. cloth bag placing position.
Fig. 5: release schematic diagram.Wherein: 23. flue dust entrances; 24. circulating line; 25. venthole, or water jet placing position.
Five, the specific embodiment
1. with the waste gas that discharges after gas combustion, inject in reaction tower by compression pump and annular release.
2. the water inlet of lime aqueous solution by reaction tower injected in tower.
3. start screw, stir current.
4. be used for if this is assimilated tower the waste gas that cleaning forms with solid fuel ignitions such as coals, need first to remove solid dust by deduster, then just inject and digest and assimilate tower.
5. sink by outer circulation and decide the pond precipitation, the liquid limewash of unreacted waste gas and clarification is recycling.
6. sedimentation basin is taked multi stage precipitation, and first sedimentation basin should be little, plays the effect of the flow velocity that first reduces water.
Claims (5)
1. assimilate tower, it is characterized in that: this tower is cylinder, also can be designed to cone, stage body, and the space multistory solid that is mutually combined by these solids; Propeller is installed in tower body, release, water deflector, tower body design sedimentation basin outward.
2. the tower of assimilating according to claim 1, is characterized in that: be suitable for propeller in tower and be used as power.
3. assimilate according to claim 1 tower, it is characterized in that: annular release is installed in tower.
4. the tower of assimilating according to claim 1, is characterized in that: design in tower and work as hydrophone.
5. the tower of assimilating according to claim 1, is characterized in that: use the assembly of cylinder and centrum to be sedimentation basin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012101137322A CN103127813A (en) | 2011-11-22 | 2012-04-10 | Absorbing and digesting tower |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110387407 | 2011-11-22 | ||
| CN201110387407.0 | 2011-11-22 | ||
| CN2012101137322A CN103127813A (en) | 2011-11-22 | 2012-04-10 | Absorbing and digesting tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103127813A true CN103127813A (en) | 2013-06-05 |
Family
ID=48488647
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012101137322A Pending CN103127813A (en) | 2011-11-22 | 2012-04-10 | Absorbing and digesting tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103127813A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104560644A (en) * | 2014-12-22 | 2015-04-29 | 朱永彪 | Anaerobic power generation and gas supply station with film mixed wattle and steel structure |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101406804A (en) * | 2008-09-09 | 2009-04-15 | 刘启杰 | High-efficient purification treatment device for flue tail gas of fuel oil cremator |
-
2012
- 2012-04-10 CN CN2012101137322A patent/CN103127813A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101406804A (en) * | 2008-09-09 | 2009-04-15 | 刘启杰 | High-efficient purification treatment device for flue tail gas of fuel oil cremator |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104560644A (en) * | 2014-12-22 | 2015-04-29 | 朱永彪 | Anaerobic power generation and gas supply station with film mixed wattle and steel structure |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CA2897415C (en) | Marine exhaust gas scrubber | |
| CN204582902U (en) | A kind of waste gas absorption spray equipment | |
| CN103127813A (en) | Absorbing and digesting tower | |
| CN112707523A (en) | Industrial sewage treatment device easy to form polluted gas | |
| CN106139873A (en) | A kind of desulfurization by lime gypsum method device | |
| CN106000143A (en) | Use method of special preparation device for boiler flue gas desulfurization tower repair agent | |
| CN109316918A (en) | A kind of ship tail gas desulphurization denitration dedusting subtracts carbon technique and device | |
| CN204320095U (en) | A kind of flue gas blender being applied to desulphurization denitration | |
| CN204891496U (en) | Boats and ships tail gas PM2. 5 remove device | |
| CN205495324U (en) | High -efficient simple and easy medical msw incineration purifier | |
| CN103848498A (en) | Atomizing aeration tank | |
| CN106606909B (en) | Supergravity ship flue gas purification system device and application thereof | |
| CN102814116A (en) | All-time interval rotary spray drying waste incineration flue gas purification device | |
| CN210522217U (en) | Gas boiler flue gas purification equipment | |
| CN113731171A (en) | Marine carbon dioxide washing tower, spraying, washing and absorbing system and method | |
| CN208839388U (en) | A kind of aqueous vapor mixed flow microbubble generator | |
| CN105126508A (en) | Water mist -based marine exhaust gas PM2.5 removal device | |
| CN202762286U (en) | Full-period rotation spray drying waste incineration flue gas cleaning device | |
| CN105888784A (en) | Automotive exhaust gas treating device | |
| CN207137647U (en) | A kind of emission-control equipment | |
| CN107803125B (en) | Combined gas-liquid fusion device of serial venturi tube | |
| CN205903792U (en) | Lime stone gypsum method desulphurization unit | |
| CN206325350U (en) | The emission-control equipment that a kind of chemical industry processing is produced | |
| CN201263963Y (en) | Venturi type desulphurization and emission reduction device by atomized lime siphoning method | |
| CN200985329Y (en) | Device for preventing and eliminating scum from crusting in anaerobic reaction tank |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C53 | Correction of patent of invention or patent application | ||
| CB02 | Change of applicant information |
Address after: Grain Bureau of Anhui Province Wang Fu Road Station 236000 Fuyang City Yingzhou District Applicant after: Zhu Yongbiao Address before: 236300 Jiao Town, Funan County, Anhui Province Applicant before: Zhu Yongbiao |
|
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20130605 |
|
| RJ01 | Rejection of invention patent application after publication |