CN100418613C - Circular dense phase fluidizing desulfurization apparatus - Google Patents
Circular dense phase fluidizing desulfurization apparatus Download PDFInfo
- Publication number
- CN100418613C CN100418613C CNB2006101146097A CN200610114609A CN100418613C CN 100418613 C CN100418613 C CN 100418613C CN B2006101146097 A CNB2006101146097 A CN B2006101146097A CN 200610114609 A CN200610114609 A CN 200610114609A CN 100418613 C CN100418613 C CN 100418613C
- Authority
- CN
- China
- Prior art keywords
- tower body
- cylindrical reactor
- flue gas
- reactor tower
- deflector
- 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.)
- Active
Links
Images
Landscapes
- Treating Waste Gases (AREA)
Abstract
The circular dense phase fluidizing desulfurization apparatus belongs to the field of environment engineering technology and is one improved fume desulfurizing apparatus. The desulfurizing apparatus includes square Venturi tube, stirrer, elevator, guide unit, web plate, collecting bin, humidifier, reaction region, and material distributor. The guide unit consists of material permeating hole, guide plate skeleton and guide plate. The apparatus of the present invention has smooth running, low power consumption, easy installation and production, light dust collector load lowered by the web plate, and capacity of recovering desulfurizer for reuse.
Description
Technical field
The invention belongs to field of environment engineering, particularly a kind of improvement of flue gas desulfurization device.
Background technology
The dense-phase tower flue gas desulfurization technique is a kind of semi-dry method flue gas desulfurization technique, has that flow process is simple, floor space is little, the desulfurizing agent water capacity is low, does not lump, sticking wall, do not stop up, do not have burn into and do not have advantages such as waste water generation, desulfuration efficiency and sorbent utilization height, byproduct can fully utilize.
Original dense flow absorber semidry process desulfurization reactor is square tower body, flue gas enters from reactor top, in dense flow absorber under the stirring action of chain-type agitator, the desulfurizing agent that adds is fluidized state and contacts with flue gas, have an effect, reclaim desulfurizing agent through the sack cleaner circulation then,, guarantee desulfurized effect with utilization rate that improves desulfurizing agent and the time of contact that prolongs desulfurizing agent and flue gas.
Mainly there is following problem in equipment before improving:
1, equipment energy consumption height;
2, the cylindrical reactor inner air is mobile very unreasonable;
3, cylindrical reactor row is big to the dust concentration load of deduster;
4, shaft is bigger, processing and fabricating cost height, and easily cause vibration.
Summary of the invention
The objective of the invention is in order to solve original dense-phase tower desulfurizing equipment in actual moving process, because the problem on the structural design, generation loaded down with trivial details such as complex structure, construction and manufacturing procedure, power consumption is high, vibration obviously, go out problems such as the tower dust concentration is big.
A kind of circular dense phase fluidizing desulfurization apparatus, it is characterized in that desulphurization plant comprises square Wen's cloth tube 1, agitating device 2, elevator 3, guiding device 4, web plate 5, aggregate bin 6, humidifier 7, reaction zone 8 and distributing device 9, guiding device 4 is made up of material feeding hole 10, deflector skeleton 11 and deflector 12.Establish square Wen's cloth tube 1 before the cylindrical reactor tower body inlet, flue gas fully contacts with the equally distributed desulfurizing agent material of process agitating device 2 fragmentations, enters the cylindrical reactor tower body.Flue gas flows from bottom to top in cylindrical reactor inside, and the deflector 12 by cylindrical reactor inside enters reaction zone 8 and carries out desulphurization reaction, and flue gas is discharged from the outlet that is located at cylindrical reactor top after desulfurization.When flue gas passes through cylindrical reactor inside, run into the obstruction and the collision of web plate 5, part cloud is separated from flue gas, the material feeding hole that sees through guiding device falls into aggregate bin 6, behind humidifier 7 humidifications, transport back in the smoke inlet place distributing device 9 recycling by elevator 3.
Main feature of the present invention is: reactor is cylindrical, tower body diameter 1～12m, tower height 5～60m; Flue gas earlier through Wen's cloth system with after desulfurizing agent fully contacts, enter cylindrical reactor from bottom to top, the cross section of Wen's cloth tube is square, its length of side 500～1000mm, the chain rotating speed of stirring system is 50～1000 rev/mins, chain stripe pitch 10～500mm, diameter chain 1～30mm; The inner deflector of cylindrical reactor adopts the fish scale structural design, wide 10～1000mm, long 500～15000mm, 5 °～90 ° at inclination angle; Cylindrical reactor adopts ciculation fluidized technology to combine with close technology mutually, and the inner desulfurizing agent material concentration of cylindrical reactor is at 100～800g/m
3Between; 1～3 layer of web plate filter set up in cylindrical reactor inside, web plate mesh width 0.01～1m, can the row of making to the cloud concentration of deduster by original 600g/m
3Be reduced to 300g/m
3Below; Humidifier is loaded on the cylindrical reactor bottom.
Major advantage of the present invention is:
1, utilize ciculation fluidized technology and dense-phase tower technology to combine.Use the inside reactor desulfurizing agent material concentration of ciculation fluidized technology to be 100g/m merely
3Below, use the inside reactor desulfurizing agent material concentration 600～800g/m of dense flow absorber technology merely
3, two kinds of technology in conjunction with post-reactor inside desulfurizing agent material concentration at 100～800g/m
3Between, help the abundant reaction of desulfurizing agent and flue gas, improve the utilization ratio of desulfurizing agent simultaneously;
2, humidifier is loaded on the cylindrical reactor bottom.Reduce desulfurizing agent material shipping height, save energy consumption;
3, stir distribution device and put the reactor outside, ad hoc system is square Wen's cloth system, plays the effect of the stirring of desulfurizing agent material, cloth and reuse.Utilize venturi principle, the state that makes the desulfurizing agent material enter tower body is the atomizing shape, agitating device is positioned over the cylindrical reactor outside, shaft size after the improvement is reduced, be convenient to processing and installation, avoided simultaneously because shaft is installed in the vibration problems in the running that causes on the reactor;
4, set up the web plate filter in cylindrical reactor inside.Fluidized reaction carries out in cylindrical reactor, can stop part cloud by web plate, reduces the burden of deduster, can reclaim desulfurizing agent simultaneously, and the hole that makes it to fall into deflector recycles;
5, add deflector in the cylindrical reactor bottom.Because its special structure makes that not only can enter cylindrical reactor to flue gas plays guide functions, guarantees simultaneously can be fallen into collection bucket, recycle and reuse by the desulfurizing agent material under the web plate obstruct.
Description of drawings
Fig. 1 is an apparatus structure front view of the present invention
The square Wen's cloth tube of 1-; The 2-agitating device; The 3-elevator; 4-guiding device (forming) by 10,11,12; The 5-web plate; The 6-aggregate bin; The 7-humidifier; The 8-reaction zone; The 9-distributing device; The 10-material feeding hole; 11-deflector skeleton; The 12-deflector;
Fig. 2 is the deflector partial enlarged drawing
Fig. 3 is the vertical view of cylindrical reactor
Fig. 4 is the stirring system sectional view
Fig. 5 is Wen's principle schematic
The specific embodiment
As shown in Figure 1, reactor is cylindrical tower body, and flue gas enters inside reactor from bottom to top and carries out desulphurization reaction.The gas approach place establishes square Wen's cloth system (being made up of square Wen's cloth tube, agitating device and distributing device), and agitating device fully disperses the desulfurizing agent material, makes it to mix with flue gas equably, enters cylindrical reactor inside together.Behind the deflector water conservancy diversion, desulfurizing agent material and flue gas are at inside reactor generation desulphurization reaction, and the state of inside reactor desulfurizing agent material and flue gas has guaranteed fully carrying out of desulphurization reaction between ciculation fluidized and close phase two states.Inside reactor is established the web plate filter, and holding back material feeding hole that partial desulfurization agent material makes it to see through guiding device, to fall into aggregate bin recycling, and the web plate filter has guaranteed that also row descends to the cloud concentration of deduster, alleviates the burden of deduster simultaneously.Flue gas drains into deduster by the top outlet behind desulphurization reaction.
As shown in Figure 2, guiding device is made up of deflector skeleton, deflector and material feeding hole.Deflector adopts the design of fish scale type, tilts to be dislocatedly distributed on the deflector skeleton, and the flue gas that enters reaction zone is played guide functions.Stopped the desulfurizing agent material that settles down by web plate and can fall into aggregate bin by material feeding hole.
As shown in Figure 3, square Wen's cloth system is made up of square Wen's cloth tube, agitating device and distributing device.The desulfurizing agent material is scattered in the stirring system through distributing device, after stirring by the abundant mixing of stirring chain, by square Wen's cloth tube input reaction zone.According to venturi principle, because the reducing effect of Venturi tube and cylindrical reactor, desulfurizing agent material and flue gas will enter cylindrical reactor inside in the mode of approximate winding-up, make the mixing of desulfurizing agent material and flue gas disperse exposure level to be strengthened, and ensure that desulphurization reaction fully carries out.
Claims (5)
1. circular dense phase fluidizing desulfurization apparatus, it is characterized in that desulphurization plant comprises square Wen's cloth tube (1), agitating device (2), elevator (3), guiding device (4), web plate (5), aggregate bin (6), humidifier (7), reaction zone (8) and distributing device (9), guiding device (4) is made up of material feeding hole (10), deflector skeleton (11) and deflector (12); Humidifier (7) is located at the bottom of cylindrical reactor tower body; Establish square Wen's cloth tube (1) before the cylindrical reactor tower body inlet, flue gas is located fully to contact at agitating device (2) with the equally distributed desulfurizing agent material of process agitating device (2) fragmentation, and the flue gas that contains the desulfurizing agent material continues to enter the cylindrical reactor tower body via square Wen's cloth tube (1); Flue gas flows from bottom to top in cylindrical reactor tower body inside, and the deflector (12) by cylindrical reactor tower body inside enters reaction zone (8) and carries out desulphurization reaction, and flue gas is discharged from the outlet that is located at cylindrical reactor tower body top after desulfurization; When flue gas passes through cylindrical reactor tower body inside, run into the obstruction and the collision of web plate (5), part cloud is separated from flue gas, the material feeding hole that sees through guiding device falls into aggregate bin (6), behind humidifier (7) humidification, transported back in the smoke inlet place distributing device (9) recyclingly by elevator (3), all the other cloud are then arranged to deduster.
2. circular dense phase fluidizing desulfurization apparatus as claimed in claim 1 is characterized in that close phase reactor is described cylindrical reactor tower body, tower body diameter 1～12m, tower height 5～60m; The cross section of Wen's cloth tube is square, its length of side 500～1000mm; The chain rotating speed of agitating device is 50～1000 rev/mins, chain stripe pitch 10～500mm, diameter chain 1～30mm.
3. circular dense phase fluidizing desulfurization apparatus as claimed in claim 1 is characterized in that the inner deflector of cylindrical reactor tower body adopts the fish scale structural design, the wide 10～1000mm of deflector, long 500～15000mm, 5 °～90 ° at inclination angle.
4. circular dense phase fluidizing desulfurization apparatus as claimed in claim 1 is characterized in that cylindrical reactor tower body inside establishes 1～3 layer of web plate, the width 0.01～1m of mesh on the web plate, the row of making to the cloud concentration of deduster by original 600g/m
3Be reduced to 300g/m
3Below.
5. circular dense phase fluidizing desulfurization apparatus as claimed in claim 1 is characterized in that the cylindrical reactor tower body adopts ciculation fluidized technology to combine with close technology mutually, and the inner desulfurizing agent material concentration of cylindrical reactor tower body is at 100～800g/m
3Between.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006101146097A CN100418613C (en) | 2006-11-17 | 2006-11-17 | Circular dense phase fluidizing desulfurization apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006101146097A CN100418613C (en) | 2006-11-17 | 2006-11-17 | Circular dense phase fluidizing desulfurization apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1973967A CN1973967A (en) | 2007-06-06 |
| CN100418613C true CN100418613C (en) | 2008-09-17 |
Family
ID=38124488
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2006101146097A Active CN100418613C (en) | 2006-11-17 | 2006-11-17 | Circular dense phase fluidizing desulfurization apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100418613C (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101773774B (en) * | 2010-03-19 | 2012-06-27 | 北京科技大学 | Dense-phase circulating fluidized flow absorber desulfurization device |
| CN101920164B (en) * | 2010-06-12 | 2012-09-19 | 北京科技大学 | Horizontal dense-phase circulating fluidizing dry-tower desulfurization device |
| CN107596798B (en) * | 2017-10-31 | 2024-06-07 | 中冶赛迪技术研究中心有限公司 | Pre-dedusting, desulfurizing and denitrating integrated treatment device and method |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1307926A (en) * | 2000-12-15 | 2001-08-15 | 清华大学 | Dry cyclic suspension bed fume desulfurizing process and system |
| US6290921B1 (en) * | 1999-11-03 | 2001-09-18 | Foster Wheeler Enegeria Oy | Method and apparatus for binding pollutants in flue gas |
| US6508994B1 (en) * | 1998-05-18 | 2003-01-21 | ABB Fläkt AB | Method and apparatus for cleaning flue gases |
| US20030019356A1 (en) * | 2001-07-12 | 2003-01-30 | Hansjorg Herden | Process and device for cleaning combustion flue gases |
| CN1425491A (en) * | 2002-12-09 | 2003-06-25 | 武汉凯迪电力股份有限公司 | Composite Circulation fluidized dry desulfurization process for flue gas and desalfurizing reaction tower |
| CN1537668A (en) * | 2003-10-23 | 2004-10-20 | 武汉凯迪电力股份有限公司 | Multiple reaction integrated process for desulfuizing from fume by dry method and its system |
-
2006
- 2006-11-17 CN CNB2006101146097A patent/CN100418613C/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6508994B1 (en) * | 1998-05-18 | 2003-01-21 | ABB Fläkt AB | Method and apparatus for cleaning flue gases |
| US6290921B1 (en) * | 1999-11-03 | 2001-09-18 | Foster Wheeler Enegeria Oy | Method and apparatus for binding pollutants in flue gas |
| CN1307926A (en) * | 2000-12-15 | 2001-08-15 | 清华大学 | Dry cyclic suspension bed fume desulfurizing process and system |
| US20030019356A1 (en) * | 2001-07-12 | 2003-01-30 | Hansjorg Herden | Process and device for cleaning combustion flue gases |
| CN1425491A (en) * | 2002-12-09 | 2003-06-25 | 武汉凯迪电力股份有限公司 | Composite Circulation fluidized dry desulfurization process for flue gas and desalfurizing reaction tower |
| CN1537668A (en) * | 2003-10-23 | 2004-10-20 | 武汉凯迪电力股份有限公司 | Multiple reaction integrated process for desulfuizing from fume by dry method and its system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1973967A (en) | 2007-06-06 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102872712B (en) | Semi-dry-process desulfurization apparatus | |
| CN112221340B (en) | Integrated method for desulfurizing and dedusting by humidifying circulation semidry method outside tower | |
| CN104959018A (en) | Device and method for redesulfuration with desulfurization ash | |
| CN100467100C (en) | Circulating suspension state dried method desulfurizing technology and special purpose desulfurizing tower thereof | |
| CN102847422B (en) | Apparatus for desulfurizing smoke through ammonia process | |
| CN105126460A (en) | Desulphurization dedusting integrated half-dry type swirl desulfurization tower | |
| CN104258721A (en) | Low-energy-consumption and ultraclean-emission flue gas desulfurization method and device | |
| CN100418613C (en) | Circular dense phase fluidizing desulfurization apparatus | |
| KR20140091538A (en) | Dual-chamber multi-absorption wet flue desulfurization device | |
| CN200980986Y (en) | Circulation fluidized bed dry method smoke desulphurizing device | |
| CN210229598U (en) | High efficiency nanometer calcium carbonate desulphurization unit | |
| CN113144771B (en) | Flue gas deacidification dust removal integrated device based on close coherent tower | |
| CN202844869U (en) | Desulfurization equipment adopting semi-dry method | |
| CN200998641Y (en) | Compact-phase circulation fluidization desulfurization equipment | |
| CN206604374U (en) | A kind of desulfurizing tower | |
| CN100460047C (en) | Circulation fluidized bed dry method flue gas desulfur device | |
| CN201439047U (en) | Recycling material fluidization conveying device of semi-dry desulphurization system | |
| CN215310895U (en) | Flue gas deacidification dust removal integrated device based on dense-phase dry tower | |
| CN102228781B (en) | SDFGD (semi-dry flue gas desulfurization) device | |
| CN210699539U (en) | Turn-back desulfurizing tower with tray on one side | |
| CN101920164B (en) | Horizontal dense-phase circulating fluidizing dry-tower desulfurization device | |
| CN201260936Y (en) | Wet flue gas desulfurization absorption tower slurry pool | |
| CN201711091U (en) | Horizontal drying tower flue gas desulfurizing device adopting dense-phase circulating fluidization | |
| CN203507814U (en) | Efficient circulating fluidized bed desulfurizer | |
| CN201912889U (en) | Flue gas desulfurization reactor for downlink recirculating fluidized bed |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C53 | Correction of patent of invention or patent application | ||
| CB03 | Change of inventor or designer information |
Inventor after: Song Cunyi Inventor after: Wang Li Inventor after: Qian Dayi Inventor after: Xing Yi Inventor after: Liu Jianchao Inventor before: Song Cunyi Inventor before: Wang Li Inventor before: Qian Dayi Inventor before: Liu Jianchao |
|
| COR | Change of bibliographic data |
Free format text: CORRECT: INVENTOR; FROM: SONG CUNYI WANG LI QIAN DAYI LIU JIANCHAO TO: SONG CUNYI WANG LI QIAN DAYI XING YI LIU JIANCHAO |
|
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: BEIJING BEIKE ENVIRONMENTAL ENGINEERING CO.,LTD. Assignor: University of Science and Technology Beijing Contract record no.: 2011990000943 Denomination of invention: Circular dense phase fluidizing desulfurization apparatus Granted publication date: 20080917 License type: Exclusive License Open date: 20070606 Record date: 20110928 |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20221107 Address after: Room A-4645, Building 3, No. 20 Yong'an Road, Shilong Economic Development Zone, Mentougou District, Beijing, 102308 Patentee after: BEIJING BEIKE ENVIRONMENTAL ENGINEERING CO.,LTD. Address before: 100083 No. 30, Haidian District, Beijing, Xueyuan Road Patentee before: University OF SCIENCE AND TECHNOLOGY BEIJING |
|
| TR01 | Transfer of patent right |