CN209714738U - A kind of efficient aerodynamic emulsification flue gas desulfurization device - Google Patents
A kind of efficient aerodynamic emulsification flue gas desulfurization device Download PDFInfo
- Publication number
- CN209714738U CN209714738U CN201920327448.2U CN201920327448U CN209714738U CN 209714738 U CN209714738 U CN 209714738U CN 201920327448 U CN201920327448 U CN 201920327448U CN 209714738 U CN209714738 U CN 209714738U
- Authority
- CN
- China
- Prior art keywords
- gas
- flue gas
- liquid
- circulatory pool
- agitating paddle
- 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.)
- Expired - Fee Related
Links
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 54
- 239000003546 flue gas Substances 0.000 title claims abstract description 54
- 238000006477 desulfuration reaction Methods 0.000 title claims abstract description 49
- 230000023556 desulfurization Effects 0.000 title claims abstract description 42
- 238000004945 emulsification Methods 0.000 title abstract description 14
- 239000007788 liquid Substances 0.000 claims abstract description 84
- 239000007789 gas Substances 0.000 claims abstract description 52
- 230000003009 desulfurizing effect Effects 0.000 claims abstract description 32
- 238000003756 stirring Methods 0.000 claims description 34
- 238000000926 separation method Methods 0.000 claims description 30
- 230000003028 elevating effect Effects 0.000 claims description 3
- 230000001804 emulsifying effect Effects 0.000 claims description 3
- 238000006243 chemical reaction Methods 0.000 abstract description 3
- 239000000839 emulsion Substances 0.000 abstract description 2
- 239000002002 slurry Substances 0.000 abstract 1
- 239000012530 fluid Substances 0.000 description 28
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 8
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 8
- 230000000694 effects Effects 0.000 description 7
- 239000007921 spray Substances 0.000 description 7
- 239000005864 Sulphur Substances 0.000 description 5
- 238000010586 diagram Methods 0.000 description 5
- 238000004804 winding Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 239000000779 smoke Substances 0.000 description 4
- 238000005507 spraying Methods 0.000 description 4
- 229910052717 sulfur Inorganic materials 0.000 description 4
- 239000011593 sulfur Substances 0.000 description 4
- 230000008859 change Effects 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 2
- 238000000151 deposition Methods 0.000 description 2
- 230000008092 positive effect Effects 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000003340 mental effect Effects 0.000 description 1
- 238000011017 operating method Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model provides a kind of efficient aerodynamic emulsification flue gas desulfurization device, including desulfurizing tower and circulatory pool.Gas outlet is equipped at the top of desulfurizing tower, desulfurization tower bottom is equipped with liquid outlet, and desulfurizing tower side is respectively equipped with air inlet and inlet.Liquid outlet passes through first pipe and circulatory pool connection, circulatory pool passes through second pipe and inlet connection, it is connected to circulating pump, circulatory pool and desulfurizing tower on second pipe, liquid circulation loop is formed by first pipe, second pipe and circulating pump, is equipped with agitating device inside circulatory pool.A kind of efficient aerodynamic of the utility model emulsifies flue gas desulfurization device, using the circulating pump or loop slurry of small flow, increases the specific surface area of liquid grain in the emulsion of desulfurization reaction zone, that is, can reach very high desulfuration efficiency.
Description
Technical field
The utility model belongs to frame for movement technical field, sets more particularly, to a kind of emulsification flue gas desulfurization of efficient aerodynamic
It is standby.
Background technique
Raw material in combustion, can continue to generate sulfur-containing smoke gas, dirty in the various gaseous states impacted to air quality
It contaminates in object, the quantity of sulfur dioxide is maximum, influences most wide.As industrial continuous expansion and people are to the increasingly heavy of environmental protection
Depending on requiring the desulfurization process of flue gas higher and higher.Desulfurizer refers to the device of sulphur in removing raw material.Sulfur method generally divides
For dry desulfurization and wet desulphurization two major classes.Dry desulfurization device is generally hollow circle tube equipment, built-in iron oxide, silica gel,
The absorption plants such as active carbon.
Current widely applied flue gas desulfurization device is wet desulfurizing process, and flue gas desulfurization device is most of by desulfurization
Spray equipment is set in tower, desulfurizing agent is sprayed by spray equipment, carries out desulphurization reaction after flue gas and desulfurization agent.But due to
The gas flow rate that sulfur-containing smoke gas enters desulfurizing tower is fast, when the contact for the desulfurizing agent for spraying sulfur-containing smoke gas and spraying device of desulfurizing tower
Between it is short, and the nozzle of spray equipment easily blocks, and causes desulfuration efficiency low.
Cooperate at least partially through desulfurizing tower and circulatory pool, using Pneumatic emulsifying desulfurization principle, realizes flue gas desulfurization, but desulfurization
System complex and circulation is insufficient, operating procedure is cumbersome and desulfuration efficiency is low, and operating cost is high, is unfavorable for promoting and applying.
Summary of the invention
Problem to be solved in the utility model is to provide a kind of desulfurizer；Especially structure is simple, circulating effect is good, takes off
A kind of efficient aerodynamic that sulphur efficiency is high and production cost is low emulsifies flue gas desulfurization device.
In order to solve the above technical problems, the technical solution adopted in the utility model is: a kind of efficient aerodynamic emulsification flue gas is de-
Sulphur equipment, including desulfurizing tower and circulatory pool, the desulfurizing tower top are equipped with gas outlet, and the desulfurization tower bottom is equipped with liquid outlet,
The desulfurizing tower side is respectively equipped with air inlet and inlet, and the liquid outlet passes through first pipe and the circulatory pool connection,
The circulatory pool is connected to circulating pump by second pipe and the inlet connection on the second pipe, the circulatory pool and
The desulfurizing tower forms liquid circulation loop, the circulation by the first pipe, the second pipe and the circulating pump
Agitating device is equipped with inside pond, the agitating device includes stirring rod and agitating paddle, and the stirring rod is elevating lever, the stirring
Bar one end connects the agitating paddle, and the stirring rod other end connects driving motor, the agitating paddle include the first agitating paddle and
Second agitating paddle, first agitating paddle are opening towards the U-shaped of the circulatory pool bottom direction, and second agitating paddle is opening
Towards the U-shaped of the circulatory pool top-direction, first agitating paddle is placed in second agitating paddle top, the agitating paddle and institute
Stirring rod is stated to be fixedly connected.
Further, the desulfurizing tower successively includes equal gas chamber, clean room and gas-liquid separation chamber, the gas from bottom to top
Liquid outlet, the air inlet and the clean room described in connection are distinguished in room from bottom to top, and the clean room joins respectively from bottom to top
Lead to the equal gas chamber, the inlet and the gas-liquid separation chamber, the gas-liquid separation chamber distinguishes net described in connection from bottom to top
Change room and the gas outlet.
Further, cyclone is equipped in the clean room.
Further, the cyclone includes the first cyclone and the second cyclone, first cyclone and described the
Two cyclone parallelly distribute ons, first cyclone and second cyclone are placed in the inlet lower part.
Further, the cyclone includes shell, and the enclosure interior is equipped with blade, and the blade is spiral shape, institute
State blade be it is multiple, the blade is evenly distributed in the shell in winding staircase shape.
Further, gas-liquid separator is equipped in the gas-liquid separation room.
Further, the gas-liquid separator includes separator body, and the separator body is hollow cylinder, described
Separator body be equipped with open-work, the open-work be it is multiple, the open-work is evenly distributed in the separator body.
Further, the liquid outlet passes through the second vertebra by the first centrum and the equal gas chamber connection, the equal gas chamber
Body and clean room's connection, the clean room pass through third centrum and gas-liquid separation chamber's connection, the gas-liquid separation chamber
Pass through the 4th centrum and the gas outlet connection.
Further, the equal gas chamber, the clean room and the gas-liquid separation chamber are cylindrical body, and the equal gas chamber is straight
Diameter is greater than clean room's diameter, and the equal gas chamber diameter is less than gas-liquid separation chamber's diameter.
Further, air-introduced machine is equipped at the air inlet.
The utility model has the advantages and positive effects of: by the way that agitating device is arranged in circulatory pool, can promote and follows
The abundant circulation of ring liquid, gas increase after being stirred by cyclone with smoke contacts area, and the efficiency that unit liquid measure traps SO2 is aobvious
It writes and increases, be sufficiently mixed gas-liquid by cyclone high speed rotary-cut circulation fluid, improve desulfuration efficiency.
1, the utility model structure is simple, and circulation fluid enters clean room by inlet, flows from above to below, and flue gas is by air inlet
Mouth enters equal gas chamber, flows from bottom to top, and flue gas accelerates rotation to rise, contact with the circulation fluid of whereabouts, shape after cyclone
At emulsification liquid layer.Emulsification liquid layer is continuously shredded by flue gas, is sufficiently mixed gas-liquid, mass-transfer efficiency multiplication, with conventional spray
It drenches desulfurization and improves several times compared to desulfuration efficiency, effectively prevent blocking the situation for causing desulfurization effect low because of spray head.
2, the swirler blades of the utility model are spiral shape, are distributed in the shell in winding staircase shape, flue gas can be made in eddy flow
Generate strong rotating turbulence movement in device, gas flow drop is brought to contacting with inner walls and be removed by air-flow, is effectively improved
The case where gas outlet flue gas drop is carried secretly.
3, the gas-liquid separator of the utility model is cylindrical body, and separator body inner wall is encountered when flue gas is entered by open-work
Face and rotate, generate centrifugal force and so that gas-liquid separation is more thorough improve flue gas mass dryness fraction, purified flue gas is discharged into atmosphere, takes off
Circulation fluid after sulphur introduces circulatory pool through liquid outlet, recycles, and the utility model is easy to operate, and operating cost is low, conducive to pushing away
Wide application.
4, the utility model can promote the abundant circulation of circulation fluid, improve de- by the way that agitating device is arranged in circulatory pool
Sulphur efficiency.Agitating device structure is simple, novel in design ingenious, and opening is equipped on the same stirring rod towards opposite two
U-shaped agitating paddle can make circulation fluid stirring more abundant.Stirring while agitating paddle can be moved up and down along stirring rod is prevented
Only circulation fluid deposits, and drives circulation fluid circulation, mixing effect inside circulatory pool good.
Detailed description of the invention
Fig. 1 is the utility model embodiment overall structure diagram
Fig. 2 is the agitating device structural schematic diagram of the utility model embodiment
Fig. 3 is the structural schematic diagram of the desulfurizing tower of the utility model embodiment
Fig. 4 is the structural schematic diagram of the cyclone of the utility model embodiment
Fig. 5 is the structure of gas liquid separator schematic diagram of the utility model embodiment
In figure:
| 1, gas outlet | 2, desulfurizing tower | 3, air inlet |
| 4, air-introduced machine | 5, liquid outlet | 6, first pipe |
| 7, circulatory pool | 8, circulating pump | 9, agitating device |
| 10, second pipe | 11, inlet | 12, driving motor |
| 13, stirring rod | 14, the first agitating paddle | 15, the second agitating paddle |
| 16, gas-liquid separation chamber | 17, clean room | 18, equal gas chamber |
| 19, the first centrum | 20, the second centrum | 21, cyclone |
| 22, third centrum | 23, gas-liquid separator | 24, the 4th centrum |
| 25, blade | 26, shell | 27, separator body |
| 28, open-work |
Specific embodiment
The utility model embodiment is described further with reference to the accompanying drawing:
As shown in Figure 1, a kind of efficient aerodynamic emulsifies flue gas desulfurization device, including desulfurizing tower 2 and circulatory pool 7.Desulfurizing tower 2 pushes up
Portion is equipped with gas outlet 1, and 2 bottom of desulfurizing tower is equipped with liquid outlet 5, and 2 side of desulfurizing tower is respectively equipped with air inlet 3 and inlet 11.Out
Liquid mouth 5 passes through second pipe 10 and 11 connection of inlet, second pipe by first pipe 6 and 7 connection of circulatory pool, circulatory pool 7
It is connected to circulating pump 8 on 10, is equipped with air-introduced machine 4 at air inlet 3.Circulatory pool 7 and desulfurizing tower 2 pass through first pipe 6, second pipe 10
Liquid circulation loop is formed with circulating pump 8.Agitating device 9 is equipped with inside circulatory pool 7.
As shown in Fig. 2, agitating device 9 includes stirring rod 13 and agitating paddle, 13 one end of stirring rod connects agitating paddle, stirring rod
13 other ends connect driving motor 12.Agitating paddle includes the first agitating paddle 14 and the second agitating paddle 15, and the first agitating paddle 14 is to open
For mouth towards the U-shaped of 7 bottom direction of circulatory pool, the second agitating paddle 15 is U-shaped, first agitating paddle of the opening towards 7 top-direction of circulatory pool
14 are placed in 15 top of the second agitating paddle, and agitating paddle is fixedly connected with stirring rod 13.Opening is installed on the same stirring rod 13
Towards two opposite U-shaped agitating paddles, circulation fluid stirring can be made more abundant.Stirring rod 13 is elevating lever, and agitating paddle can be along
Stirring while stirring rod 13 moves up and down, prevents circulation fluid from depositing, and drives 7 inside circulation fluid of circulatory pool circulation, stirring
Effect is good.
As shown in figure 3, desulfurizing tower 2 successively includes equal gas chamber 18, clean room 17 and gas-liquid separation chamber 16 from bottom to top.Gas
Connection liquid outlet 5, air inlet 3 and clean room 17 are distinguished from bottom to top in room 18.The equal gas chamber of connection is distinguished from bottom to top in clean room 17
18, inlet 11 and gas-liquid separation chamber 16.Connection clean room 17 and gas outlet 1 are distinguished from bottom to top by gas-liquid separation chamber 16.
Preferably, liquid outlet 5 is by the first centrum 19 and equal 18 connection of gas chamber, and equal gas chamber 18 is by the second centrum 20 and only
Change 17 connection of room, clean room 17 passes through the 4th centrum by third centrum 22 and 16 connection of gas-liquid separation chamber, gas-liquid separation chamber 16
24 with 1 connection of gas outlet.Equal gas chamber 18, clean room 17 and gas-liquid separation chamber 16 are cylindrical body, and equal 18 diameter of gas chamber is greater than net
Change 17 diameter of room, equal 18 diameter of gas chamber is less than 16 diameter of gas-liquid separation chamber.
Cyclone 21 is equipped in clean room 17.Cyclone 21 includes the first cyclone and the second cyclone, the first cyclone
With the second cyclone parallelly distribute on, the first cyclone and the second cyclone are placed in 11 lower part of inlet.
As shown in figure 4, cyclone 21 includes shell 26, blade 25 is equipped with inside shell 26, blade 25 is spiral shape, blade
25 is multiple, and blade 25 is evenly distributed in shell 26 in winding staircase shape, this structure can be such that flue gas generates in cyclone 21 strongly
Rotating turbulence movement, gas flow drop brought to contacting with 26 inner wall of shell by air-flow and is removed, and is effectively improved 1 flue gas of gas outlet
The case where drop is carried secretly.
Gas-liquid separator 23 is equipped in gas-liquid separation chamber 16.As shown in figure 5, gas-liquid separator 23 includes separator body
27, separator body 27 is hollow cylinder, and separator body 27 is equipped with open-work 28, open-work 28 be it is multiple, open-work 28 is uniform
It is distributed in separator body 27.Flue gas is encountered 27 inner wall of separator body and is rotated when being entered by open-work 28, generate from
Mental and physical efforts improve flue gas mass dryness fraction so that gas-liquid separation is more thorough.
The course of work of the present embodiment is as follows:
Circulating pump 8 is squeezed into the circulation fluid in circulatory pool 7 to desulfurizing tower 2 by circulatory pool 7, by the inlet 11 of desulfurizing tower 2
Into clean room 17, circulation fluid is flowed from above to below.Former flue gas passes through pipeline to desulfurizing tower 2, by desulfurizing tower by air-introduced machine 4
2 air inlets 3 enter the equal gas chamber 18 of desulfurizing tower 2, and flue gas flows from bottom to top.When flue gas passes through cyclone 21, air-flow is in winding staircase
Strong rotating turbulence movement is generated under the action of shape helical blade 25, flue gas will accelerate rotation to rise.In the position of cyclone 21
It sets, former flue gas is contacted with the circulation fluid of whereabouts, and flue gas high speed rotary-cut circulation fluid, circulation fluid is chopped into, and gas-liquid continues mutually to collide,
Circulation fluid grain the more is cut the more broken, and gas-liquid is sufficiently mixed, and since gas has certain power, certain quantity of fluid can be held up,
Therefore one layer of certain thickness stable emulsification liquid layer can be formed.Emulsification liquid layer is continuously shredded by flue gas, fills gas-liquid
Divide mixing, mass-transfer efficiency multiplication, the desulfuration efficiency raising several times compared with routinely spraying desulfurization.
Stirring rod 13 rotates under the drive of driving motor 12, so that height while stirring rod 13 is rotated along central axes
Rise, agitating paddle is fixedly connected on stirring rod 13, the first agitating paddle 14 and the second agitating paddle 15 under the drive of stirring rod 13,
Agitation cycle liquid, so that material is sprung up up and down, reaction is abundant.
Since circulation fluid is constantly added, gas towing force is limited, therefore the emulsification liquid layer originally formed will be added below
The circulation fluid entered replaces, and forms new emulsification liquid layer, so recycles, to reach the desulfurization effect of continuous high-efficient.Meanwhile in flue gas
SO2 contact and be absorbed with the fine liquid grain of circulation fluid in emulsification liquid layer, due to the specific surface area ratio of the liquid grain in emulsion
Rise the modes such as moisture film, spray it is big several times to tens times, therefore unit liquid measure traps the efficiency of SO2 and significantly increases.It is net after desulfurization
When flue gas enters separator body 27 by open-work, because separator body 27 is cylindrical body, flue gas encounters separator body 27
Inner wall and rotate, generate centrifugal force, realize gas-liquid separation.Purified flue gas is discharged into atmosphere by gas outlet 1, following after desulfurization
Ring liquid introduces circulatory pool 7 through liquid outlet 5, recycles.
Utility model has the advantages and positive effects of: the utility model structure is simple, and circulation fluid is entered by inlet
Clean room flows from above to below, and flue gas enters equal gas chamber by air inlet, flows from bottom to top, and flue gas accelerates after cyclone
Rotation rises, and contacts with the circulation fluid of whereabouts, forms emulsification liquid layer.Emulsification liquid layer is continuously shredded by flue gas, makes gas-liquid
It is sufficiently mixed, mass-transfer efficiency multiplication, desulfuration efficiency improves several times compared with routinely spraying desulfurization, effectively prevents blocking because of spray head
Lead to the situation that desulfurization effect is low.
The swirler blades of the utility model are spiral shape, are distributed in the shell in winding staircase shape, flue gas can be made in cyclone
Interior to generate strong rotating turbulence movement, gas flow drop is brought to contacting with inner walls and be removed by air-flow, is effectively improved out
The case where port flue gas drop is carried secretly.
The gas-liquid separator of the utility model is cylindrical body, and separator body inner wall is encountered when flue gas is entered by open-work
And rotate, centrifugal force is generated so that gas-liquid separation is more thorough and improves flue gas mass dryness fraction, and purified flue gas is discharged into atmosphere, desulfurization
Circulation fluid afterwards introduces circulatory pool through liquid outlet, recycles, and the utility model is easy to operate, and operating cost is low, is conducive to promote
Using.
The utility model can promote the abundant circulation of circulation fluid, improve desulfurization by the way that agitating device is arranged in circulatory pool
Efficiency.Agitating device structure is simple, novel in design ingenious, and opening is equipped on the same stirring rod towards two opposite U
Type agitating paddle can make circulation fluid stirring more abundant.Stirring while agitating paddle can be moved up and down along stirring rod, prevents
Circulation fluid deposition drives circulation fluid circulation, mixing effect inside circulatory pool good.
One embodiment of the utility model is described in detail above, but the content is only the utility model
Preferred embodiment should not be considered as limiting the scope of the present invention.It is all to be made according to application scope of the utility model
All the changes and improvements etc., should still belong within the patent covering scope of the utility model.
Claims (10)
1. a kind of efficient aerodynamic emulsifies flue gas desulfurization device, including desulfurizing tower and circulatory pool, it is characterised in that: the desulfurization tower top
Portion is equipped with gas outlet, and the desulfurization tower bottom is equipped with liquid outlet, and the desulfurizing tower side is respectively equipped with air inlet and inlet, institute
Liquid outlet is stated by first pipe and the circulatory pool connection, the circulatory pool passes through second pipe and the inlet connection,
It is connected to circulating pump, the circulatory pool and the desulfurizing tower on the second pipe and passes through the first pipe, the second pipe
Liquid circulation loop is formed with the circulating pump, agitating device is equipped with inside the circulatory pool, the agitating device includes stirring
Bar and agitating paddle, the stirring rod are elevating lever, and described stirring rod one end connects the agitating paddle, and the stirring rod other end connects
Driving motor is connect, the agitating paddle includes the first agitating paddle and the second agitating paddle, and first agitating paddle is that opening is followed towards described
Cisterna ambiens bottom direction it is U-shaped, second agitating paddle is opening towards the U-shaped of the circulatory pool top-direction, first stirring
Paddle is placed in second agitating paddle top, and the agitating paddle is fixedly connected with the stirring rod.
2. a kind of efficient aerodynamic according to claim 1 emulsifies flue gas desulfurization device, it is characterised in that: the desulfurizing tower is certainly
It is lower and on successively include equal gas chamber, clean room and gas-liquid separation chamber, the equal gas chamber distinguish from bottom to top liquid outlet described in connection,
Gas chamber, the inlet and described are distinguished described in connection from bottom to top by the air inlet and the clean room, the clean room
Clean room and the gas outlet described in connection are distinguished from bottom to top by gas-liquid separation chamber, the gas-liquid separation chamber.
3. a kind of efficient aerodynamic according to claim 2 emulsifies flue gas desulfurization device, it is characterised in that: in the clean room
Equipped with cyclone.
4. a kind of efficient aerodynamic according to claim 3 emulsifies flue gas desulfurization device, it is characterised in that: the cyclone packet
Include the first cyclone and the second cyclone, first cyclone and the second cyclone parallelly distribute on, first eddy flow
Device and second cyclone are placed in the inlet lower part.
5. a kind of efficient aerodynamic according to claim 3 or 4 emulsifies flue gas desulfurization device, it is characterised in that: the eddy flow
Device includes shell, the enclosure interior be equipped with blade, the blade be spiral shape, the blade be it is multiple, the blade be in disk
Scalariform is evenly distributed in the shell.
6. emulsifying flue gas desulfurization device according to a kind of any efficient aerodynamic of claim 2 to 4, it is characterised in that: described
Gas-liquid separator is equipped in gas-liquid separation room.
7. a kind of efficient aerodynamic according to claim 6 emulsifies flue gas desulfurization device, it is characterised in that: the gas-liquid separation
Device includes separator body, and the separator body is hollow cylinder, and the separator body is equipped with open-work, the open-work
To be multiple, the open-work is evenly distributed in the separator body.
8. emulsifying flue gas desulfurization device according to a kind of any efficient aerodynamic of claim 2 to 4, it is characterised in that: described
Liquid outlet passes through the second centrum and clean room's connection, institute by the first centrum and the equal gas chamber connection, the equal gas chamber
Clean room is stated by third centrum and gas-liquid separation chamber's connection, the gas-liquid separation chamber passes through the 4th centrum and the outlet
Mouth connection.
9. a kind of efficient aerodynamic according to claim 8 emulsifies flue gas desulfurization device, it is characterised in that: the equal gas chamber,
The clean room and the gas-liquid separation chamber are cylindrical body, and the equal gas chamber diameter is greater than clean room's diameter, described equal
Gas chamber diameter is less than gas-liquid separation chamber's diameter.
10. a kind of according to claim 1 to 4 or 7 or 9 any efficient aerodynamics emulsify flue gas desulfurization device, feature exists
In: air-introduced machine is equipped at the air inlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920327448.2U CN209714738U (en) | 2019-03-14 | 2019-03-14 | A kind of efficient aerodynamic emulsification flue gas desulfurization device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920327448.2U CN209714738U (en) | 2019-03-14 | 2019-03-14 | A kind of efficient aerodynamic emulsification flue gas desulfurization device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209714738U true CN209714738U (en) | 2019-12-03 |
Family
ID=68686618
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920327448.2U Expired - Fee Related CN209714738U (en) | 2019-03-14 | 2019-03-14 | A kind of efficient aerodynamic emulsification flue gas desulfurization device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209714738U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114797437A (en) * | 2022-04-28 | 2022-07-29 | 东方电气集团东方锅炉股份有限公司 | Slurry reflux circulation system of flue gas desulfurization tower |
-
2019
- 2019-03-14 CN CN201920327448.2U patent/CN209714738U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114797437A (en) * | 2022-04-28 | 2022-07-29 | 东方电气集团东方锅炉股份有限公司 | Slurry reflux circulation system of flue gas desulfurization tower |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106457140B (en) | Rotation, which converges, couples ultra-clean desulphurizing and dust-removing integral system and its desulfurization and dust-removal method | |
| CN1114467C (en) | Dry cyclic suspension bed fume desulfurizing process and system | |
| CN203123767U (en) | Composite type dust collector | |
| CN105169926B (en) | A kind of flue gas desulphurization system and the method that flue gas desulfurization is carried out using it | |
| CN205308097U (en) | High -efficient desulfurization dust removal integrated device | |
| CN102847422A (en) | Apparatus for desulfurizing smoke through ammonia process | |
| CN209714738U (en) | A kind of efficient aerodynamic emulsification flue gas desulfurization device | |
| CN111318154A (en) | Integration low temperature denitrification facility | |
| CN105477998B (en) | A kind of low-energy-consumption high-efficiency calcium base wet-process desulfurizer and technique | |
| CN105233659B (en) | A kind of fume desulfurizing tower and fume desulphurization method | |
| CN201384922Y (en) | Spiral type vertical sieve plate jet bubbling desulfurization dust absorbing tower | |
| CN111097249B (en) | Rotational flow-based high-efficiency turbulent flow atomization mixing desulfurization dust removal process | |
| CN100460047C (en) | Circulation fluidized bed dry method flue gas desulfur device | |
| CN2550043Y (en) | Cyclone flow spray aeration desulfurization dust remover | |
| CN205517232U (en) | Energy -conserving desulfurization dust removal minimum discharge integrated device | |
| CN204768247U (en) | Defogging wet -type desulfurizing tower system | |
| CN202161916U (en) | Flue gas desulfurization spraying equipment | |
| CN204502782U (en) | A kind of efficient boiler desulfurization treatment system | |
| CN219318829U (en) | Circulating fluidized bed | |
| CN101518716B (en) | Helical-type vertical sieve tray injection bubbling desulfurization and dedusting absorption tower | |
| CN206604374U (en) | A kind of desulfurizing tower | |
| CN208287797U (en) | A kind of efficient oxidation wet desulfurization system | |
| CN204447724U (en) | A kind of Pneumatic emulsifying device of dedusting and desulfurizing tower | |
| CN208287798U (en) | A kind of efficient oxidation wet desulphurization device | |
| CN202173875U (en) | Ammonia flue gas desulfurization device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20191203 |