CN203494367U - Airflow uniform distribution wet method flue gas desulfurizing absorption tower - Google Patents
Airflow uniform distribution wet method flue gas desulfurizing absorption tower Download PDFInfo
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- CN203494367U CN203494367U CN201320559012.9U CN201320559012U CN203494367U CN 203494367 U CN203494367 U CN 203494367U CN 201320559012 U CN201320559012 U CN 201320559012U CN 203494367 U CN203494367 U CN 203494367U
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- absorption tower
- uniform distribution
- flue gas
- airflow uniform
- diversion rod
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Abstract
The utility model discloses an airflow uniform distribution wet method flue gas desulfurizing absorption tower. The airflow uniform distribution wet method flue gas desulfurizing absorption tower comprises an absorption tower barrel, wherein the bottom of the absorption tower barrel is provided with a seriflux pool; a barrel wall of the absorption tower barrel arranged above the seriflux pool is provided with a smoke inlet channel, the top of the absorption tower barrel is provided with a smoke outlet channel, and an absorbent seriflux spray system and a demister are arranged between the smoke inlet channel and the smoke outlet channel from bottom to top; an airflow uniform distribution device is arranged between the absorbent seriflux spray system and the smoke inlet channel and is provided with multiple guiding rods which are horizontally arranged at intervals, and the cross sections of the guiding rods are of reverse V-shaped structures. The airflow uniform distribution wet method flue gas desulfurizing absorption tower provided by the utility model has the characteristics that the smoke in the absorption tower is uniformly distributed, a condition that the airflow in the absorption tower is effectively rectified is realized, the problem that local air speed is too high is observably solved, the contact area and the contact time of the smoke and seriflux are increased, and the use ratio of the seriflux is improved; the structure is simple, the improvement cost is low, the maintenance is convenient, and the popularization is easy.
Description
Technical field
The utility model relates to the spray absorber in wet process of FGD equipment, refers to particularly a kind of airflow uniform distribution formula wet flue gas desulfurization absorption tower.
Background technology
Acid rain problem is one of global environmental problem of face of mankind nowadays, the coal-fired oxysulfide SO producing
2with nitrogen oxide NO
xpollution is the main protozoa of China's acid rain.Because the energy resource structure of China be take coal as main, in China's power industry, thermoelectricity accounts for 70% left and right of gross generation always, and coal-fired power plant is the first pollution sources of China's atmosphere pollution.Power-plant flue gas being polluted to control be the requirement that realizes economic, society, harmonious development, is also the requirement of bringing into play coal in China superiority of reserves, realizing coal-burning power plant self sustainable development.It is several that tradition coal fired power plant flue gas desulfurization technique is generally divided into wet method, semidry method and dry desulfurization etc., and wherein Wet Flue Gas Desulfurization Technique is applied the most extensively.In Wet Flue Gas Desulfurization Technique, be that the sulfur dioxide in flue gas is directly contacted with vaporific slurries, vaporific slurries and sulfur dioxide are reacted and be absorbed, thereby reach the object of desulfurization.
At present, at the Wet Flue Gas Desulfurization Technique of industrial application, be used widely because of advantages such as desulfuration efficiency are high, system is simple and reliable as limestone-gypsum method and the ammonia process of desulfurization etc.Wet desulphurization equipment is mainly spray absorber, in actual applications, because the flue gas flow rate at smoke inlet place is larger, only rely on the motion of air-flow self and the airflow uniform distribution effect of spray liquid rectified action limited, after causing a large amount of flue gases to enter tower body, move away from inlet side in edge, cause smoke gas flow skewness in absorption tower, and the speed variance on same cross section is larger, cause flue gas to be difficult to fully contact with spray liquid, have a strong impact on mass transfer and the heat transfer of gas-liquid two-phase; Especially in ammonia process list tower desulphurization system, " the escaping of ammonia " phenomenon is very serious, and wherein the too high escape amount that all can increase ammonia of air-flow skewness and local air velocity, has not only wasted absorbent but also polluted surrounding environment.
Summary of the invention
The purpose of this utility model is exactly the defect that will overcome air-flow skewness in the existing tower of existing desulfurization spray absorber, and a kind of airflow uniform distribution formula wet flue gas desulfurization absorption tower is provided.
For achieving the above object, the airflow uniform distribution formula wet flue gas desulfurization absorption tower that the utility model is designed, comprise absorber tower cylinder, described absorber tower cylinder bottom is provided with slurry pool, on the absorber tower cylinder barrel of described slurry pool top, be provided with gas approach passage, described absorber tower cylinder top is provided with exhanst gas outlet passage, between described gas approach passage and exhanst gas outlet passage, be provided with absorbent slurry spray equipment and demister from bottom to top, its special character is: between described absorbent slurry spray equipment and gas approach passage, be provided with airflow uniform distribution device, described airflow uniform distribution device comprises the diversion rod that arrange a plurality of horizontal intervals, the cross section of described diversion rod is reverse V-shaped structure.
Preferably, the angle between described diversion rod and gas approach channel centerline is 90 ± 10 °, and by sparse, becomes gradually intensive from the side near gas approach passage to its arrangement of a side away from gas approach passage.Like this, can optimize rectification effect, flue gas is uniformly distributed.
Preferably, the gap area summation between described diversion rod is 30～60% with the ratio of the cross-sectional area of absorber tower cylinder corresponding position, and the best is 40～50%.Like this, can, in the situation that not affecting slurries and contacting with flue gas, air-flow in absorption tower be evenly arranged.
Preferably, the reverse V-shaped drift angle of described diversion rod is 30～70 °, and the height of described diversion rod from reverse V-shaped drift angle to bottom is 100～300mm; The best is: the reverse V-shaped drift angle of diversion rod is 40～60 °, and the height of diversion rod from reverse V-shaped drift angle to bottom is 150～250mm.Like this, can realize air-flow in absorption tower is carried out to effective rectification, increase contact area and the time of contact of flue gas and slurries, improve the utilization rate of slurries.
Preferably, the reverse V-shaped drift angle of described diversion rod to the vertical range H of gas approach channel centerline and the entrance height of gas approach passage or diameter L meets following mathematical relationship: H=0.5L+(1.5～2.5), unit is m.Like this, can optimize each several part dimension scale, realize best rectification effect.
Preferably, the two ends of described diversion rod are fixed on support frame, and the barrel of described support frame and absorber tower cylinder is fixedly linked.Like this, can maintain easily and overhaul, also can adjust according to actual conditions the arrangement of diversion rod.
Preferably, the two ends of described diversion rod barrel direct and absorber tower cylinder is weldingly connected.Like this, can constructability, also can improve the fixing stability of diversion rod.
Preferably, described absorbent slurry spray equipment is provided with three layers.Like this, can increase contact area and the time of contact of flue gas and slurries, improve desulfuration efficiency.
The utlity model has following advantage: in absorption tower, set up the airflow uniform distribution device that the diversion rod by many reverse V-shaped structures combines, the flue gas that makes to enter in absorption tower can be uniformly distributed, realization is carried out effective rectification to air-flow in absorption tower, significantly alleviated the excessive problem of local flue gas flow rate, increase contact area and the time of contact of flue gas and slurries, improved the utilization rate of slurries; And there is the features such as simple in structure, improvement cost is cheap, easy to maintenance, be easy to promote.
Accompanying drawing explanation
Fig. 1 is a kind of structural representation of airflow uniform distribution formula wet flue gas desulfurization absorption tower.
Fig. 2 is the A-A cross-sectional view in Fig. 1.
In figure: exhanst gas outlet passage 1, demister 2, gas approach passage 3, slurry pool 4, airflow uniform distribution device 5(be diversion rod 5.1 wherein), absorbent slurry spray equipment 6, absorber tower cylinder 7.
The specific embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail.
Embodiment 1:
Airflow uniform distribution formula wet flue gas desulfurization absorption tower as shown in Fig. 1～2, comprise absorber tower cylinder 7, absorber tower cylinder 7 bottoms are provided with slurry pool 4, on absorber tower cylinder 7 barrels of slurry pool 4 tops, be provided with gas approach passage 3, absorber tower cylinder 7 tops are provided with exhanst gas outlet passage 1, between gas approach passage 3 and exhanst gas outlet passage 1, be disposed with three layers of absorbent slurry spray equipment 6 and demister 2 from bottom to top, between absorbent slurry spray equipment 6 and gas approach passage 1, be provided with airflow uniform distribution device 5, airflow uniform distribution device 5 comprises the diversion rod 5.1 that arrange a plurality of horizontal intervals, the two ends barrel direct and absorber tower cylinder 7 of diversion rod 5.1 is weldingly connected, also the two ends of diversion rod 5.1 can be fixed on support frame, support frame is fixedly linked with the barrel of absorber tower cylinder 7 again.
The cross section of diversion rod 5.1 is reverse V-shaped structure, and the angle between itself and gas approach passage 3 center lines is 90 ± 10 °, and by sparse, becomes gradually intensive from the side near gas approach passage 3 to its arrangement of a side away from gas approach passage 3.The reverse V-shaped drift angle of diversion rod 5.1 to the vertical range H of gas approach passage 3 center lines and the entrance height of gas approach passage 3 or diameter L meets following mathematical relationship: H=0.5L+1.5～2.5, unit is m.
During optimal design, the gap area summation between diversion rod 5.1 is 30～60% with the ratio of the cross-sectional area of absorber tower cylinder 7 corresponding positions, and the best is 40～50%, is 35～45% in the present embodiment.The reverse V-shaped drift angle of diversion rod 5.1 is 30～70 °, and the height of diversion rod 5.1 from reverse V-shaped drift angle to bottom is 100～300mm.Preferred plan is that the reverse V-shaped drift angle of diversion rod 5.1 is 40～60 °, and the height of diversion rod 5.1 from reverse V-shaped drift angle to bottom is 150～250mm; In the present embodiment, the height of diversion rod 5.1 is 100～200mm, and reverse V-shaped drift angle is 40～60 °.
Embodiment 2:
Another kind of airflow uniform distribution formula wet flue gas desulfurization absorption tower of the present utility model, its general structure is substantially the same manner as Example 1, just the height of diversion rod 5.1 from reverse V-shaped drift angle to bottom is 200～300mm, the reverse V-shaped drift angle of diversion rod 5.1 is 60～70 °, and the gap area summation between diversion rod 5.1 is 45%～55% with the ratio of the cross-sectional area of absorber tower cylinder 7 corresponding positions.
The utility model is set up the airflow uniform distribution device 5 that the diversion rod 5.1 by the reverse V-shaped structure of a row forms in absorption tower, flue gas enters in tower from gas approach passage 3, by the flow-disturbing effect of reverse V-shaped diversion rod 5.1, flue gas stream in absorption tower is uniformly distributed again, realization is carried out effective rectification to air-flow in absorption tower, significantly improve the excessive problem of local gas speed, increased contact area and the time of contact of flue gas and slurries, improved the utilization rate of slurries.With respect to prior art, diversion rod 5.1 arrangements on airflow uniform distribution device 5 are flexible, can be large in exhaust gas volumn and region that velocity of flue gas is high arrange relatively intensively, the region that exhaust gas volumn is little and velocity of flue gas is low is arranged relatively sparse, improves sprayed slurry liquid utilization rate and desulfuration efficiency.Moreover because the voidage of airflow uniform distribution device 5 is large, therefore install pressure drop ratio that airflow uniform distribution device 5 causes additional, that the pressure drop that other forms of airflow uniform distribution device causes is installed is little; The reverse V-shaped structure of diversion rod 5.1, make slurries and flue gas reverse contact react after, when the product of generation drop to airflow uniform distribution device 5, can arrive smoothly slurry pool, prevent residual product crystallization on airflow uniform distribution device 5 phenomenon that results in blockage; Meanwhile, reduce the impact strength of spray liquid to airflow uniform distribution device 5, can extend the service life of airflow uniform distribution device 5.
Finally, it should be pointed out that above embodiment is only the more representational example of the utility model.Obviously, the utility model is not limited to above-described embodiment, can also have many distortion.Every foundation technical spirit of the present utility model, to any simple modification made for any of the above embodiments, equivalent variations and modification, all should be thought and belong to protection domain of the present utility model.
Claims (10)
1. an airflow uniform distribution formula wet flue gas desulfurization absorption tower, comprise absorber tower cylinder (7), described absorber tower cylinder (7) bottom is provided with slurry pool (4), on absorber tower cylinder (7) barrel of described slurry pool (4) top, be provided with gas approach passage (3), described absorber tower cylinder (7) top is provided with exhanst gas outlet passage (1), between described gas approach passage (3) and exhanst gas outlet passage (1), be provided with absorbent slurry spray equipment (6) and demister (2) from bottom to top, it is characterized in that: between described absorbent slurry spray equipment (6) and gas approach passage (1), be provided with airflow uniform distribution device (5), described airflow uniform distribution device (5) comprises the diversion rod (5.1) that arrange a plurality of horizontal intervals, the cross section of described diversion rod (5.1) is reverse V-shaped structure.
2. airflow uniform distribution formula wet flue gas desulfurization absorption tower according to claim 1, it is characterized in that: the angle between described diversion rod (5.1) and gas approach passage (3) center line is 90 ± 10 °, and by sparse, become gradually intensive from the side near gas approach passage (3) to its arrangement of a side away from gas approach passage (3).
3. airflow uniform distribution formula wet flue gas desulfurization absorption tower according to claim 1, is characterized in that: the ratio of the cross-sectional area of the gap area summation between described diversion rod (5.1) and absorber tower cylinder (7) corresponding position is 30～60%.
4. airflow uniform distribution formula wet flue gas desulfurization absorption tower according to claim 1, is characterized in that: the ratio of the cross-sectional area of the gap area summation between described diversion rod (5.1) and absorber tower cylinder (7) corresponding position is 40～50%.
5. airflow uniform distribution formula wet flue gas desulfurization absorption tower according to claim 1, is characterized in that: the reverse V-shaped drift angle of described diversion rod (5.1) is 30～70 °, and the height of described diversion rod (5.1) from reverse V-shaped drift angle to bottom is 100～300mm.
6. airflow uniform distribution formula wet flue gas desulfurization absorption tower according to claim 1, is characterized in that: the reverse V-shaped drift angle of described diversion rod (5.1) is 40～60 °, and the height of described diversion rod (5.1) from reverse V-shaped drift angle to bottom is 150～250mm.
7. airflow uniform distribution formula wet flue gas desulfurization absorption tower according to claim 1, it is characterized in that: the reverse V-shaped drift angle of described diversion rod (5.1) meets following mathematical relationship to the vertical range H of gas approach passage (3) center line and entrance height or the diameter L of gas approach passage (3): H=0.5L+(1.5～2.5), unit is m.
8. airflow uniform distribution formula wet flue gas desulfurization absorption tower according to claim 1, is characterized in that: the two ends of described diversion rod (5.1) are fixed on support frame, and the barrel of described support frame and absorber tower cylinder (7) is fixedly linked.
9. airflow uniform distribution formula wet flue gas desulfurization absorption tower according to claim 1, is characterized in that: the two ends barrel direct and absorber tower cylinder (7) of described diversion rod (5.1) is weldingly connected.
10. airflow uniform distribution formula wet flue gas desulfurization absorption tower according to claim 1, is characterized in that: described absorbent slurry spray equipment (6) is provided with three layers.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320559012.9U CN203494367U (en) | 2013-09-09 | 2013-09-09 | Airflow uniform distribution wet method flue gas desulfurizing absorption tower |
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|---|---|---|---|
| CN201320559012.9U CN203494367U (en) | 2013-09-09 | 2013-09-09 | Airflow uniform distribution wet method flue gas desulfurizing absorption tower |
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| CN203494367U true CN203494367U (en) | 2014-03-26 |
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| CN201320559012.9U Expired - Fee Related CN203494367U (en) | 2013-09-09 | 2013-09-09 | Airflow uniform distribution wet method flue gas desulfurizing absorption tower |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103463961A (en) * | 2013-09-09 | 2013-12-25 | 武汉钢铁(集团)公司 | Airflow uniform distribution type wet-method smoke desulfurization and absorption tower |
-
2013
- 2013-09-09 CN CN201320559012.9U patent/CN203494367U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103463961A (en) * | 2013-09-09 | 2013-12-25 | 武汉钢铁(集团)公司 | Airflow uniform distribution type wet-method smoke desulfurization and absorption tower |
| CN103463961B (en) * | 2013-09-09 | 2015-05-06 | 武汉钢铁(集团)公司 | Airflow uniform distribution type wet-method smoke desulfurization and absorption tower |
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140326 Termination date: 20140909 |
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| EXPY | Termination of patent right or utility model |