CN204601836U - For the cyclone that wet desulfurization system flue gas drop removes - Google Patents
For the cyclone that wet desulfurization system flue gas drop removes Download PDFInfo
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- CN204601836U CN204601836U CN201520212057.8U CN201520212057U CN204601836U CN 204601836 U CN204601836 U CN 204601836U CN 201520212057 U CN201520212057 U CN 201520212057U CN 204601836 U CN204601836 U CN 204601836U
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- cyclone
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Abstract
The utility model relates to a kind of cyclone removed for wet desulfurization system flue gas drop, described cyclone comprises upper body, lower case and multiple swirl vane, be connected with the outlet of desulfurizer mist eliminator bottom lower case, upper body top is connected with chimney.Described swirl vane is spirality, and multiple swirl vane is dish ladder arrangement in lower case; Described upper body is provided with drainage arrangement.The utility model is by arranging cyclone on desulfurizer mist eliminator top, can make desulfurization fume in cyclone, produce strong rotating turbulence motion, drop in air-flow is brought to and upper body contact internal walls and being removed by air-flow, thus effectively improves the situation that chimney rains.This hydrocyclone structure is simple, only needs a little space to arrange, can arrange, therefore applied range at the chimney place in-situ reformation of existing desulphurization system.
Description
Technical field
The utility model relates to Wet Flue Gas Desulfurization Technique field, is specifically related to a kind of cyclone removed for wet desulfurization system flue gas drop.
Background technology
At present, for sulfur dioxide pollution thing contained in fire coal boiler fume and sintering device flue gas, China mainly adopts Wet Flue Gas Desulfurization Technique to administer.Wet Flue Gas Desulfurization Technique mature and reliable, desulfuration efficiency is high, but wet desulphurization exists chimney breast neat stress drop simultaneously carries phenomenon secretly.
Cause chimney breast neat stress drop carry secretly phenomenon because have many-side: the first, flue gas is in the inner uphill process of chimney, and flue gas pressures slowly reduces, and flue gas adiabatic expansion causes flue gas cool-down; The second, the flue gas that temperature is higher and the lower inner wall of stack contact heat-exchanging of temperature, cause outside flue-gas temperature to decline; 3rd, the flue gas in the middle part of flue and chimney and the low-temperature flue gas heat exchange in outside, cause middle part flue-gas temperature to decline.And when flue-gas temperature is reduced to below wet flue gas saturation temperature, the steam in flue gas will be condensed into water droplet, carried out chimney by flue gas.Chimney breast neat stress entrained drip part can drop to ground, forms chimney rain, pollutes surrounding environment, and chimney rain is the disadvantage that wet desulphurization exists.
Therefore be necessary to design a kind of cyclone removed for wet desulfurization system flue gas drop, to overcome the problems referred to above.
Utility model content
The purpose of this utility model is the defect overcoming prior art, provides a kind of cyclone removed for wet desulfurization system flue gas drop, and its structure is simple, occupation of land is few, and drop removal efficiency is high.
The utility model is achieved in that
The utility model provides a kind of cyclone removed for wet desulfurization system flue gas drop, and described wet desulfurization system comprises desulfurizing tower and chimney, and described desulfurizing tower comprises demister.Described cyclone comprises upper body, lower case and multiple swirl vane, is connected bottom described lower case with the outlet of described demister, and described upper body top is connected with described chimney; Described swirl vane is spirality, and described multiple swirl vane is dish ladder arrangement in described lower case; Described upper body is provided with drainage arrangement.
Further, flow perturbation device is provided with along axis in described cyclone.
Further, described flow perturbation device comprises disturbance post, and described disturbance post is bullet-shaped and conehead end is arranged bottom described lower case.
Further, described drainage arrangement comprises osculum, and described osculum is connected with drainpipe; The top of described lower case is flush-mounted within the bottom of described upper body, and the gap between described upper body and lower case forms water leg, and described osculum is opened on described water leg.
Further, described osculum is 4, and described 4 osculum uniform ring are located in described upper body.
Further, described drainpipe and described upper body angle at 45 ° are arranged obliquely.
Further, described osculum is flange hole, and described drainpipe is provided with the adpting flange suitable with described osculum.
Further, the lift angle of described multiple swirl vane dish ladder arrangement is 45 °.
Further, described cyclone is connected with described demister and described chimney respectively by the mode of Flange joint.
Further, described upper body and described lower case are cylindrical.
The utility model has following beneficial effect: by arranging cyclone on desulfurizer mist eliminator top, cyclone spiral blade is in dish ladder arrangement, can make desulfurization fume in cyclone, produce strong rotating turbulence motion, drop in air-flow is brought to and upper body contact internal walls and being removed by air-flow, thus effectively improves the situation that chimney rains.Use this cyclone, the pressure drop of flue gas is less, is beneficial to the fume emission of desulphurization system.This hydrocyclone structure is simple, only needs a little space to arrange, can arrange, therefore applied range at the chimney place in-situ reformation of existing desulphurization system.
Further beneficial effect of the present utility model is: by arranging flow perturbation device, especially the disturbance post of bullet-shaped is adopted, make flue gas when entering cyclone gentle transition to the inwall side of lower case, thus increase the contact of flue gas and swirl vane, effectively improve the removal effect of drop.
Further beneficial effect of the present utility model is: by arranging water leg, is convenient to collect the drop removed, and avoids drop enter in lower case and again carried by flue gas.
Accompanying drawing explanation
In order to be illustrated more clearly in the utility model embodiment or technical scheme of the prior art, be briefly described to the accompanying drawing used required in embodiment or description of the prior art below, apparently, accompanying drawing in the following describes is only embodiments more of the present utility model, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
Fig. 1 looks perspective view for the master of the cyclone that the utility model embodiment provides;
The plan structure schematic diagram of the upper body that Fig. 2 provides for the utility model embodiment, lower case and disturbance post.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the utility model embodiment, be clearly and completely described the technical scheme in the utility model embodiment, obviously, described embodiment is only the utility model part embodiment, instead of whole embodiments.Based on the embodiment in the utility model, other embodiments all that those of ordinary skill in the art obtain under the prerequisite not making creative work, all belong to the scope of the utility model protection.
As Fig. 1-Fig. 2, the utility model embodiment provides a kind of cyclone removed for wet desulfurization system flue gas drop, and described wet desulfurization system comprises desulfurizing tower and chimney, and described desulfurizing tower comprises demister.Described cyclone comprises upper body 1, lower case 3 and multiple swirl vane 4, is connected bottom described lower case 3 with the outlet of described demister, and described upper body 1 top is connected with described chimney.Swirl vane 4 is located in lower case 3, and swirl vane 4 is spirality, and described multiple swirl vane 4 is dish ladder arrangement in described lower case 3; Preferably, described multiple swirl vane 4 coils the lift angle of ladder arrangement is 45 °.Wherein, described upper body 1 and described lower case 3 can be cylindrical or other shapes, as rectangular structure; Preferably adopt cylindrical, be convenient to the rotating turbulence motion of flue gas.The connected mode of cyclone and demister and chimney all adopts the mode of Flange joint, Stability Analysis of Structures and be convenient to installing/dismounting.
As Fig. 1-Fig. 2, described upper body 1 is provided with drainage arrangement, and described drainage arrangement comprises osculum and water leg, and osculum is opened in described upper body 1, and described osculum is connected with drainpipe 2.This osculum is flange hole, and this drainpipe 2 is provided with the adpting flange suitable with described osculum, and namely the connected mode of osculum and drainpipe 2 is Flange joint.Preferably, described drainpipe 2 is arranged obliquely with described upper body 1 angle at 45 °, is convenient to the discharge of the drop collected.The structure of water leg is: the top of described lower case 3 is flush-mounted within the bottom of described upper body 1, and namely the gap between described upper body 1 and lower case 3 forms water leg, and described osculum is opened on described water leg.In the present embodiment, described osculum is 4, and described 4 osculum uniform ring are located in described upper body 1.
In addition, during actual use, this upper body 1 can be selected to adopt chimney on the spot, and namely this cyclone comprises housing and is located at the multiple swirl vanes 4 in housing, and this housing is flush-mounted within described chimney bottom; Drainage arrangement is arranged on the bottom of chimney.Take this structure, the structure of cyclone can be simplified further, this cyclone is taken up an area less, be convenient to install and use.And, because chimney corrosion resistance is better, the corrosion resistant material making upper body 1 therefore can be saved.
As Fig. 1-Fig. 2, as a kind of preferred structure of the present embodiment, in described cyclone, be provided with flow perturbation device along axis.Preferably, described flow perturbation device comprises disturbance post 5, and described disturbance post 5 is bullet-shaped and conehead end is arranged bottom described lower case 3.The height of this disturbance post 5 is preferably with the height of lower case 3 suitable, conehead bottom portion can with lower case 3 bottom flush with or slightly higher than bottom lower case 3.In addition, this disturbance post 5 can be hollow body, to alleviate the weight of equipment; This disturbance post 5 is fixed in lower case 3 by support, to improve its operation stability.When flue gas enters cyclone, under the effect of disturbance post 5, gentle transition is to the inwall side of lower case 3, thus increases the contact of flue gas and swirl vane 4, effectively improves the removal effect of drop.
The operation principle of this cyclone is principle of inertia, and after desulfurization fume enters cyclone inside with certain speed bottom lower case 3, air-flow produces strong rotating turbulence motion under the effect of winding staircase shape swirl vane 4; Due to varying in size of the power such as the centrifugal force be subject between drop and gas, centripetal buoyancy, fluid drag, in flue gas, most of drop is rotated to upper body 1 inwall wall by swirler blades; Drop and upper body 1 inwall collide and adhere to, and after the drop of trapping collects in water leg, discharge via drainpipe 2, thus reach the object of administering chimney and raining.
Be 2,000,000 Nm for an exhaust gas volumn
3the power plant of/h, adopt limestone-gypsum method to remove sulfur dioxide in flue gas, during the cyclone not adopting the present embodiment to provide, chimney breast drop amount is 68mg/m
3, there is chimney in power-plant flue gas discharge downstream and to rain problem.After desulfurizing tower top increases the cyclone that the present embodiment provides, chimney breast drop amount is less than 30 mg/m
3, power plant's downstream chimney problem of raining effectively is alleviated.
The utility model embodiment has following beneficial effect: by arranging cyclone on desulfurizer mist eliminator top, cyclone spiral blade is in dish ladder arrangement, can make desulfurization fume in cyclone, produce strong rotating turbulence motion, drop in air-flow is brought to and upper body 1 contact internal walls and being removed by air-flow, thus effectively improves the situation that chimney rains.Use this cyclone, the pressure drop of flue gas is less, is generally less than 200-600pa, is beneficial to the fume emission of desulphurization system.This hydrocyclone structure is simple, only needs a little space to arrange, can arrange, therefore applied range at the chimney place in-situ reformation of existing desulphurization system.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all within spirit of the present utility model and principle, any amendment done, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (10)
1. the cyclone removed for wet desulfurization system flue gas drop, described wet desulfurization system comprises desulfurizing tower and chimney, described desulfurizing tower comprises demister, it is characterized in that: described cyclone comprises upper body, lower case and multiple swirl vane, be connected with the outlet of described demister bottom described lower case, described upper body top is connected with described chimney; Described swirl vane is spirality, and described multiple swirl vane is dish ladder arrangement in described lower case; Described upper body is provided with drainage arrangement.
2. the cyclone removed for wet desulfurization system flue gas drop according to claim 1, is characterized in that: be provided with flow perturbation device along axis in described cyclone.
3. the cyclone removed for wet desulfurization system flue gas drop according to claim 2, is characterized in that: described flow perturbation device comprises disturbance post, described disturbance post is bullet-shaped and conehead end is arranged bottom described lower case.
4. the cyclone removed for wet desulfurization system flue gas drop according to claim 1, it is characterized in that: described drainage arrangement comprises osculum, described osculum is connected with drainpipe; The top of described lower case is flush-mounted within the bottom of described upper body, and the gap between described upper body and lower case forms water leg, and described osculum is opened on described water leg.
5. the cyclone removed for wet desulfurization system flue gas drop according to claim 4, is characterized in that: described osculum is 4, described 4 osculum uniform ring are located in described upper body.
6. the cyclone removed for wet desulfurization system flue gas drop according to claim 4, is characterized in that: described drainpipe and described upper body angle at 45 ° are arranged obliquely.
7. the cyclone removed for wet desulfurization system flue gas drop according to claim 4, is characterized in that: described osculum is flange hole, and described drainpipe is provided with the adpting flange suitable with described osculum.
8. the cyclone removed for wet desulfurization system flue gas drop according to claim 1, is characterized in that: the lift angle of described multiple swirl vane dish ladder arrangement is 45 °.
9. the cyclone removed for wet desulfurization system flue gas drop according to claim 1, is characterized in that: described cyclone is connected with described demister and described chimney respectively by the mode of Flange joint.
10. the cyclone removed for wet desulfurization system flue gas drop according to claim 1 or 4, is characterized in that: described upper body and described lower case are cylindrical.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520212057.8U CN204601836U (en) | 2015-04-10 | 2015-04-10 | For the cyclone that wet desulfurization system flue gas drop removes |
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| CN201520212057.8U CN204601836U (en) | 2015-04-10 | 2015-04-10 | For the cyclone that wet desulfurization system flue gas drop removes |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105056691A (en) * | 2015-09-28 | 2015-11-18 | 福建鑫泽环保设备工程有限公司 | Device and method for dedusting and demisting after wet desulphurization |
| CN109030122A (en) * | 2018-08-15 | 2018-12-18 | 山东国舜建设集团有限公司 | Wet flue gas condensation water sampler and method are saturated after a kind of wet desulphurization |
| CN110314452A (en) * | 2019-07-01 | 2019-10-11 | 江苏双良低碳产业技术研究院有限公司 | A kind of flue gas takes off white device |
-
2015
- 2015-04-10 CN CN201520212057.8U patent/CN204601836U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105056691A (en) * | 2015-09-28 | 2015-11-18 | 福建鑫泽环保设备工程有限公司 | Device and method for dedusting and demisting after wet desulphurization |
| CN109030122A (en) * | 2018-08-15 | 2018-12-18 | 山东国舜建设集团有限公司 | Wet flue gas condensation water sampler and method are saturated after a kind of wet desulphurization |
| CN109030122B (en) * | 2018-08-15 | 2023-12-01 | 山东国舜建设集团有限公司 | Sampling device and method for saturated wet flue gas condensate after wet desulfurization |
| CN110314452A (en) * | 2019-07-01 | 2019-10-11 | 江苏双良低碳产业技术研究院有限公司 | A kind of flue gas takes off white device |
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| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: 430205 No. 59 Liufang Avenue, Donghu High-tech Development Zone, Wuhan City, Hubei Province Patentee after: Zhongye Southern Urban Environmental Protection Engineering Technology Co., Ltd. Address before: 430071 Dongsha Building, 122 North Road, Wuchang District, Wuhan City, Hubei Province, 15th Floor Patentee before: Wuhan Urban Environment Protection Engineering Techn Co., Ltd. |
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| CP03 | Change of name, title or address |