CN201735324U - Rotational flow and junction coupling desulfurization and dust removal device - Google Patents
Rotational flow and junction coupling desulfurization and dust removal device Download PDFInfo
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- CN201735324U CN201735324U CN2010202898596U CN201020289859U CN201735324U CN 201735324 U CN201735324 U CN 201735324U CN 2010202898596 U CN2010202898596 U CN 2010202898596U CN 201020289859 U CN201020289859 U CN 201020289859U CN 201735324 U CN201735324 U CN 201735324U
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- dust arrester
- sulphur removal
- revolves
- removal dust
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Abstract
The utility model relates to an efficient energy-saving mass transfer and absorption equipment, particularly to a flue gas desulfurization and dust removal device, namely a rotational flow and junction coupling desulfurization and dust removal device, which comprises at least a support component arranged in a absorption tower in a penetrating way, and at least a rotational flow and junction device is arranged on the support component. The device has good contaminant removal effect and cooling down effect, low energy consumption, safe operation, large operating flexibility and simple structure; and with the improvement of the rate of the heat transmission and mass transfer, the device can adapt to different working conditions, generator set load and raw materials quality, thereby improving the operation flexibility and enabling a system to operate safely, efficiently and stably.
Description
Technical field
The utility model relates to a kind of energy-efficient mass transfer, absorption equipment, relates in particular to a kind of desulfurating dust removing device for flue gas.
Background technology
Revolving and converging the coupled desulfurization dedusting technology is upgrade technique on the Pneumatic emulsifying technical foundation.The Pneumatic emulsifying technology is applicable to the flue gas desulfurization of miniature boiler, and there is tangible enlarge-effect in this technology in amplification test, has certain limitation.And at present flue gas desulfurization technique adopts the void tower technology more, and promptly flue gas enters behind the absorption tower without this device, directly and the slurries that spray of top react.Flue gas and slurries will short circuits like this, and some flue gases not reaction have just left the absorption tower, and gas residence time is short, causes desulfuration efficiency low.
Summary of the invention
The purpose of this utility model is to avoid the deficiencies in the prior art to provide a kind of revolving to converge the coupled desulfurization dust arrester, and it is simple in structure, security of operation, stable, and energy consumption is low, and the desulfurization dust-removing efficiency height can effectively be protected the mass transfer absorption equipment of anti-corrosion material in the absorption tower.
For achieving the above object, the technical scheme that the utility model is taked is: a kind of remittance coupling sulphur removal dust arrester that revolves, comprise that at least one runs through the support component that is arranged in the absorption tower, and on described support component, be provided with at least one eddy flow collector-shoe gear.
Further, described support component comprises upper cover plate and lower cover, is provided with cavity between upper and lower cover plate, and described eddy flow collector-shoe gear is arranged in the cavity.
Further, described support component also includes at the two ends of described lower cover and is provided with support ox pin, is provided with support column below lower cover.
Further, the cavity between the described upper and lower cover plate is cylindric.
Further, described eddy flow collector-shoe gear comprises outer cylinder body, is provided with inner barrel in outer cylinder body, and the inner barrel radius is 0.20m～0.75m with the ratio of outer cylinder body radius; Be provided with blade in the cavity between outer cylinder body and inner barrel, above described inner barrel, be provided with blind plate; Also be provided with diversion component in the outer cylinder body above inner barrel.
Further, described blade and inner barrel angle are the 20-55 degree, the rate of blocking between the adjacent blades, and promptly to account for the percentage of individual blade projected area be-10%～45% to adjacent blades lap projected area;
Further, described diversion component comprises guide shell, and guide shell has the guide shell inner core, and the guide shell inner core is coniform, and the cone base angle is 55～80 degree; Above guide shell, be provided with cover plate, between guide shell and described outer cylinder body, be provided with reinforcement.
Further, described guide shell is round table-like.
Further, the described remittance coupling sulphur removal dust arrester that revolves is provided with one deck at least in described absorption tower.
Further, described revolve to converge be provided with the gap between the inwall on coupling sulphur removal dust arrester and described absorption tower.
The beneficial effects of the utility model are:
1, it is effective to remove pollutant.Fire coal boiler fume not only contains a large amount of sulfur dioxide, also contain pollutants such as flue dust, contain the turbulent flow parts of the flue gas elder generation of pollutant through this device, eddy flow also quickens, and passes through the diversion component on its top again, arrives upper space and forms turbulence state, a large amount of sulfur dioxide and flue dust are removed rapidly, desulfuration efficiency and efficiency of dust collection all are improved, and the byproduct of reaction gypsum of generation can be widely used in building materials, cement and improve industries such as farmland.
2, good cooling effect.Because turbulent flow parts of this device and diversion component combination make flue gas produce the high-efficiency turbulent flow state; top is sprayed the liquid that gets off breaks up and becomes very fine particle; flue-gas temperature reduces rapidly; it is more thorough on the one hand reaction to be carried out; anti-corrosion material is protected in the absorption tower; can save the cooling installation before the absorption tower on the other hand, reduce plant investment.
3, energy consumption is low.The absorption tower section arranges that one deck revolves the remittance coupling device, flue gas produces the turbulent flow space that the gas-liquid rotation is seethed through this device, it is long-pending to improve the gas-liquid contact surface, therefore the required slurries amount of absorption reaction reduces, liquid-gas ratio is little, and the slurries internal circulating load is little, and system's power consumption is low, can regulate circulating pump according to parameters such as payload, contents of sulfur dioxide during operation and open the platform number, reduce desulphurization system operating cost.
4, security of operation, operating flexibility is big.This device has improved heat and mass speed, and it is wideer to make device adapt to the scope of different operating modes, different unit load and different material quality, has improved operation elasticity, makes system's operation more safe and efficient stable.
5, simple in structure.No rotating machinery in the whole device revolves the remittance coupling device and once finishes at the installation initial stage, and long service life need not maintenance repair.
6, system's operational reliability height.Owing to increase in the absorption tower and revolve the remittance coupling device, be used to carry the circulating pump of the liquid platform number that puts into operation to mediate according to operating mode, pollutant load, avoided the round-the-clock running of circulating pump, when prolonging equipment life, for overhaul of the equipments provides powerful guarantee, make desulphurization system operation operational percentage height, system's operation safety and reliability.
Description of drawings
Fig. 1 is a section structure schematic diagram of the present utility model;
Fig. 2 is an I position enlarged drawing among the utility model figure one;
Fig. 3 is the utility model eddy flow collector-shoe gear structural representation;
Fig. 4 is the CC plan structure schematic diagram of the utility model Fig. 3;
Fig. 5 is that the B of the utility model Fig. 3 is to view;
Fig. 6 is the structural representation of the utility model diversion component;
Fig. 7 is the absorption tower front view.
The specific embodiment
Below in conjunction with accompanying drawing principle of the present utility model and feature are described, institute gives an actual example and only is used to explain the utility model, is not to be used to limit scope of the present utility model.
Embodiment 1: as Fig. 1, and Fig. 2, Fig. 3, Fig. 4, Fig. 5, Fig. 6, shown in Figure 7, a kind of remittance coupling sulphur removal dust arrester that revolves comprises that three run through the support component 1 that is arranged in the absorption tower 4, are provided with a plurality of eddy flow collector-shoe gears 2 on described support component 1.Described support component 1 comprises upper cover plate 11 and lower cover 12, is provided with cavity between upper cover plate 11, lower cover 12, and described eddy flow collector-shoe gear 2 is arranged in the cavity.Described support component 1 also includes at the two ends of described lower cover 12 and is provided with support ox pin 13, is provided with support column 14 below lower cover 12.Cavity between described upper cover plate 11, the lower cover 12 is cylindric.Described eddy flow collector-shoe gear 2 comprises outer cylinder body 21, is provided with inner barrel 22 in outer cylinder body 21, and the inner barrel radius r is 0.20m with the ratio of outer cylinder body radius R; Be provided with blade 23 in the cavity between outer cylinder body 21 and inner barrel 22, blade and inner barrel angle α are 20 degree, the rate of blocking between the adjacent blades, and promptly to account for the percentage of individual blade projected area be-10% to adjacent blades lap 231 projected areas; Above described inner barrel 22, be provided with blind plate 24; Also be provided with diversion component 3 in the outer cylinder body 21 above inner barrel 22.Described diversion component 3 comprises guide shell 31, and guide shell has the guide shell inner core, and the guide shell inner core is coniform, and the cone base angle is 55～80 degree; Above guide shell 31, be provided with cover plate 32, between guide shell 31 and described outer cylinder body 21, be provided with reinforcement 33.Described guide shell 31 is round table-like.The described remittance coupling sulphur removal dust arrester that revolves is provided with one deck in described absorption tower.Described revolve to converge be provided with the gap between the inwall on coupling sulphur removal dust arrester 2 and described absorption tower 4, described revolve to converge be provided with pad 15 between coupling sulphur removal dust arrester 2 and the support ox pin 13.
The operation course of work of described device:
As shown in Figure 7,72 end face smoke inlets 71 enter from the absorption tower from the high-temperature flue gas of boiler, through overwinding remittance coupling sulphur removal dust arrester 73, improve flue gas flow rate and under the guide effect of turbulent flow blade, form the air-flow that rotation is risen, the desulfurization slurry that sprays through diversion component and top slurries spray equipment 74 is reverse fully to be contacted, form powerful turbulent flow space, reaction efficiently removes pollutants such as sulfur dioxide, dust rapidly, realizes the efficient purification of flue gas.Flue gas after being purified is removed moisture in the flue gas through the secondary demister 75 on top, absorption tower, discharges 76 absorption towers from exhanst gas outlet, drains into atmosphere through clean flue gas flue, chimney.
Embodiment 2: identical with embodiment 1, different is that described eddy flow collector-shoe gear 2 comprises outer cylinder body 21, is provided with inner barrel 22 in outer cylinder body 21, and the inner barrel radius r is 0.75m with the ratio of outer cylinder body radius R; Be provided with blade 23 in the cavity between outer cylinder body 21 and inner barrel 22, blade and inner barrel angle α are 55 degree, the rate of blocking between the adjacent blades, and promptly to account for the percentage of individual blade projected area be 45% to adjacent blades lap 231 projected areas.
The above only is preferred embodiment of the present utility model, and is in order to restriction the utility model, not all within spirit of the present utility model and principle, any modification of being done, is equal to replacement, improvement etc., all should be included within the protection domain of the present utility model.
Claims (10)
1. one kind revolves remittance coupling sulphur removal dust arrester, it is characterized in that, comprises that at least one runs through the support component that is arranged in the absorption tower, is provided with one deck eddy flow collector-shoe gear at least on described support component.
2. the remittance coupling sulphur removal dust arrester that revolves as claimed in claim 1 is characterized in that described support component comprises upper cover plate and lower cover, is provided with cavity between upper and lower cover plate, and described eddy flow collector-shoe gear is arranged in the cavity.
3. the remittance coupling sulphur removal dust arrester that revolves as claimed in claim 2 is characterized in that described support component also includes at the two ends of described lower cover and is provided with support ox pin, is provided with support column below lower cover.
4. the remittance coupling sulphur removal dust arrester that revolves as claimed in claim 2 is characterized in that the cavity between the described upper and lower cover plate is cylindric.
5. the remittance coupling sulphur removal dust arrester that revolves as claimed in claim 1 is characterized in that described eddy flow collector-shoe gear comprises outer cylinder body, is provided with inner barrel in outer cylinder body, and inner barrel radius and outer cylinder body radius ratio are 0.20m～0.75m; Be provided with blade in the cavity between outer cylinder body and inner barrel, above described inner barrel, be provided with blind plate; Also be provided with diversion component in the outer cylinder body above inner barrel.
6. the remittance coupling sulphur removal dust arrester that revolves as claimed in claim 5 is characterized in that described blade and inner barrel angle are 20 degree～55 degree, and the rate of blocking between the adjacent blades is-10%～45%.
7. the remittance coupling sulphur removal dust arrester that revolves as claimed in claim 5 is characterized in that described diversion component comprises guide shell, and guide shell has the guide shell inner core, and the guide shell inner core is coniform, and the cone base angle is 55～80 degree; Above guide shell, be provided with cover plate, between guide shell and described outer cylinder body, be provided with reinforcement.
8. the remittance coupling sulphur removal dust arrester that revolves as claimed in claim 7 is characterized in that described guide shell is round table-like.
9. as the arbitrary described remittance coupling sulphur removal dust arrester that revolves of claim 1 to 8, it is characterized in that the described remittance coupling sulphur removal dust arrester that revolves is provided with one deck at least in described absorption tower.
10. converge coupling sulphur removal dust arrester as arbitrary described the revolving of claim 1 to 8, it is characterized in that, described revolve to converge be provided with the gap between the inwall on coupling sulphur removal dust arrester and described absorption tower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202898596U CN201735324U (en) | 2010-08-12 | 2010-08-12 | Rotational flow and junction coupling desulfurization and dust removal device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202898596U CN201735324U (en) | 2010-08-12 | 2010-08-12 | Rotational flow and junction coupling desulfurization and dust removal device |
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| CN201735324U true CN201735324U (en) | 2011-02-09 |
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| CN2010202898596U Expired - Lifetime CN201735324U (en) | 2010-08-12 | 2010-08-12 | Rotational flow and junction coupling desulfurization and dust removal device |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN103657411A (en) * | 2013-12-13 | 2014-03-26 | 哈尔滨锅炉厂有限责任公司 | Vortex mixing device for SCR (silicon controlled rectification) flue gas denitration system |
| WO2016050030A1 (en) * | 2014-09-29 | 2016-04-07 | 北京国电清新环保技术股份有限公司 | Rotational flow and sink flow-coupling integrated system for ultra-clean desulphuration and dedusting and desulphuration and dedusting method therefor |
| CN106582249A (en) * | 2017-01-19 | 2017-04-26 | 浙江富春江环保热电股份有限公司 | Deep desulfurization and dust removal system of circulating fluidized bed boiler |
| CN107352609A (en) * | 2017-09-12 | 2017-11-17 | 哈尔滨锅炉厂环保工程技术有限公司 | A kind of evaporator for waste water evaporation |
| TWI642471B (en) * | 2017-03-30 | 2018-12-01 | 北京清新環境技術股份有限公司 | Rotational flow and sink flow coupling integrated system for ultra-clean desulphurization and dedusting |
-
2010
- 2010-08-12 CN CN2010202898596U patent/CN201735324U/en not_active Expired - Lifetime
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103657411B (en) * | 2013-12-13 | 2016-10-05 | 哈尔滨锅炉厂有限责任公司 | Rotational flow mixing device for SCR flue gas denitrification system |
| CN103657411A (en) * | 2013-12-13 | 2014-03-26 | 哈尔滨锅炉厂有限责任公司 | Vortex mixing device for SCR (silicon controlled rectification) flue gas denitration system |
| JP2017518881A (en) * | 2014-09-29 | 2017-07-13 | 北京国▲電▼清新▲環▼保技▲術▼股▲ふん▼有限公司Ｂｅｉｊｉｎｇ Ｓｐｃ Ｅｎｖｉｒｏｎｍｅｎｔ Ｐｒｏｔｅｃｔｉｏｎ Ｔｅｃｈ Ｃｏ．， Ｌｔｄ | Spin exchange coupled ultra-clean desulfurization and dust integration system and desulfurization and dust removal method |
| KR20160143801A (en) * | 2014-09-29 | 2016-12-14 | 베이징 에스피씨 인바이론먼트 프로텍션 테크 컴퍼니 리미티드 | Rotational flow and sink flow-coupling integrated system for ultra-clean desulphuration and dedusting and desulphuration and dedusting method therefor |
| CN106457140A (en) * | 2014-09-29 | 2017-02-22 | 北京清新环境技术股份有限公司 | Rotational flow and sink flow-coupling integrated system for ultra-clean desulphuration and dedusting and desulphuration and dedusting method therefor |
| WO2016050030A1 (en) * | 2014-09-29 | 2016-04-07 | 北京国电清新环保技术股份有限公司 | Rotational flow and sink flow-coupling integrated system for ultra-clean desulphuration and dedusting and desulphuration and dedusting method therefor |
| US9915423B2 (en) | 2014-09-29 | 2018-03-13 | Beijing Spc Environment Protection Tech Co., Ltd. | Rotational flow and sink flow-coupling integrated system for ultra-clean desulphuration and dedusting and desulphuration and dedusting method therefor |
| AU2015327602B2 (en) * | 2014-09-29 | 2018-03-15 | Beijing Spc Environment Protection Tech Co.,Ltd | Rotational flow and sink flow-coupling integrated system for ultra-clean desulphuration and dedusting and desulphuration and dedusting method therefor |
| EP3202483A4 (en) * | 2014-09-29 | 2018-09-19 | Beijing SPC Environment Protection Tech Co., Ltd. | Rotational flow and sink flow-coupling integrated system for ultra-clean desulphuration and dedusting and desulphuration and dedusting method therefor |
| KR101932091B1 (en) * | 2014-09-29 | 2019-03-20 | 베이징 에스피씨 인바이론먼트 프로텍션 테크 컴퍼니 리미티드 | Rotational flow and sink flow-coupling integrated system for ultra-clean desulphuration and dedusting and desulphuration and dedusting method therefor |
| CN106582249A (en) * | 2017-01-19 | 2017-04-26 | 浙江富春江环保热电股份有限公司 | Deep desulfurization and dust removal system of circulating fluidized bed boiler |
| TWI642471B (en) * | 2017-03-30 | 2018-12-01 | 北京清新環境技術股份有限公司 | Rotational flow and sink flow coupling integrated system for ultra-clean desulphurization and dedusting |
| CN107352609A (en) * | 2017-09-12 | 2017-11-17 | 哈尔滨锅炉厂环保工程技术有限公司 | A kind of evaporator for waste water evaporation |
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Granted publication date: 20110209 |
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| CX01 | Expiry of patent term |