CN205495334U - Efficient dry flue gas desulfurization device of desulfurization - Google Patents
Efficient dry flue gas desulfurization device of desulfurization Download PDFInfo
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- CN205495334U CN205495334U CN201620221979.XU CN201620221979U CN205495334U CN 205495334 U CN205495334 U CN 205495334U CN 201620221979 U CN201620221979 U CN 201620221979U CN 205495334 U CN205495334 U CN 205495334U
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Abstract
The utility model relates to an efficient dry flue gas desulfurization device of desulfurization, including flue gas passageway and flue gas desulfurization material sheet frame, the flue gas is through for the long square frame of cavity, has a flue gas inlet in flue gas passageway middle part system, has all made the exhanst gas outlet in the left and right sides of flue gas passageway, and parallel system the in flue gas passageway upper portion interval in the flue gas inlet left and right sides has the bar jack, and the interior interval of jack parallel inlays and is equipped with a plurality of flue gas desulfurization material sheet frames, installs the fan on the exhanst gas outlet, the structure of flue gas desulfurization material sheet frame does a square frame, frame are cavity and left and right sides opening, at left and right sides opening part installation filter screen, pack the desulfurization material in the frame between the filter screen.
Description
Technical field
This utility model belongs to flue gas desulfurization device field, the dry flue gas desulphurization device that a kind of desulfuration efficiency is high.
Background technology
The methods such as the conventional limestone-gypsum method of wet desulphurization such as steam power plant's desulfurization, sodium hydroxide-lime white (or magnesium hydroxide), device is more complicated, operation energy consumption is the highest, produce waste water to need to process, and cause other secondary pollution, cumbersome, directly copy coking furnace flue gas desulfurization process mechanically and be likely difficult to up to standard.Also there is the way (dry desulfurization on ordinary meaning) toward Injection for CFB Boilers calcium carbonate sulphur removal, but this method treatment effect is poor.
Lime white (using the Dual alkali of sodium hydroxide+Calx, and magnesium hydroxide, principle is the most identical) and the SO in flue gas in traditional wet method2Reaction generates calcium sulfite, and (Dual alkali first passes through sodium hydroxide reaction, and the latter and lime white are reacted to calcium sulfite and restore sodium hydroxide.Sodium hydroxide solution Reusability.Clean reaction is that calcium hydroxide reacts generation calcium sulfite with sulfur dioxide);Traditional dry desulfurization is to spray into calcium carbonate with coal dust in fine coal CFBB to enter boiler furnace, and Decomposition of Calcium Carbonate generates calcium oxide, and the latter generates calcium sulfate with a part of oxysulfide;And Roche dry desulfurization simply uses Calx or magnesium hydroxide and oxidation catalyst, wherein catalyst oxidation SO2Become SO3, the latter is with lime reaction becomes calcium sulfate or reacts generation magnesium sulfate/Magnesium hydrogen sulfate etc. with magnesium hydroxide.
Conventional dry desulfurization: CaCO3→CaO+CO2 SOx+CaO→CaSO4
Conventional wet desulfurization: SO2+Ca(OH)2→CaSO3+H2O。
According to retrieval, finding the patent documentation the most relevant to the application, specific disclosure is as follows:
1, patent documentation CN 204093274U discloses a kind of flue gas desulphurization system, this flue gas desulphurization system includes absorption tower, rich solution preheater, poor rich liquid heat exchanger, desorber, reboiler, condenser and steam coupling regenerating unit, absorption tower is connected with preheater rich solution entrance, the outlet of preheater rich solution is connected with heat exchanger rich solution entrance, the outlet of heat exchanger rich solution is connected with desorber rich solution entrance, desorber steam (vapor) outlet is connected with the first steam inlet on steam coupling regenerating unit and the second steam inlet on condenser respectively, steam coupling regenerating unit is additionally provided with fresh primary steam entrance and regeneration primary steam outlet, regeneration primary steam outlet is connected with reboiler, reboiler is connected with desorber.
2, patent documentation 203379781U fume desulfurizing tower, including tower body and the tower body inner chamber that surrounded by tower body.Described fume desulfurizing tower is divided into washing section along flow of flue gas direction, absorber portion and exhausting section, wherein, described washing section include setting gradually along flow of flue gas direction with lower component: the air inlet pipe being arranged on tower body, first gas distributor, and cleaning mixture the first spray equipment being arranged in tower body inner chamber, described first gas distributor includes the multiple deflectors being arranged in described air inlet pipe, the exhaust gases passes formed between the plurality of deflector independently of one another and extend to different directions, described exhaust gases passes has and the gas outlet of tower body inner space, flue gas enters tower body inner chamber from different directions by described exhaust gases passes.Fume desulfurizing tower of the present utility model is used, it is possible to increase the desulfurization degree of flue gas in sulfur removal technology.
3, patent documentation 203737103U discloses a kind of flue gas desulfurization device, it is possible to reduce materials from bonding also can improve desulfuration efficiency.This flue gas desulfurization device is mainly and central water supply becomes dispersion water supply, it is provided with for the first jet to smoke inlet flue conveying water at the smoke inlet flue of desulfurization reaction tower, first jet and the first water inlet pipe are connected, first water inlet pipe is provided with electromagnetic valve, it is provided with on blower fan air supply duct towards the second nozzle within blower fan air supply duct, second nozzle and the second water inlet pipe are connected, and the second water inlet pipe is provided with electromagnetic valve.Adding water at one and become many places and add water, the moisture making material is more uniform, in the case of ensureing the total Water needed for desulphurization reaction, and the uniform moisture of material.Make material be difficult to bonding, and can ensure that desulfurized effect is preferable.
The equipment that said apparatus is for meeting wet desulphurization and prepares, the novel solid fume desulfurizing tower that the application designs according to new solid sulfur removal material, differ greatly with traditional flue gas desulphurization system, there is novelty and creativeness.
Utility model content
In place of the purpose of this utility model is to overcome the deficiencies in the prior art, it is provided that a kind of simple in construction, low cost of manufacture, dry flue gas desulphurization device that the desulfuration efficiency easily that reloads is high.
This utility model solves its technical problem and be the technical scheme is that
The dry flue gas desulphurization device that a kind of desulfuration efficiency is high, including exhaust gases passes and flue gas desulfurization material sheet frame, described flue gas is by for hollow rectangular framework, gas approach it is shaped with in the middle part of exhaust gases passes, exhanst gas outlet all it is shaped with in the left and right sides of exhaust gases passes, exhaust gases passes top in the gas approach left and right sides is spaced and parallel is shaped with bar shaped jack, spaced and parallel in jack it is embedded with multiple flue gas desulfurization material sheet frame, exhanst gas outlet is installed blower fan, the structure of described flue gas desulfurization material sheet frame is, including a square frame, housing is hollow and left and right sides opening, at left and right sides opening part, drainage screen is installed, sulfur removal material is filled in housing between drainage screen.
And, described sulfur removal material can be calcium hydroxide particle or calcium carbonate granule.
And, the interior survey installation sealing strip of the position that contacts with exhaust gases passes at sheet frame.
And, flue gas desulfurization material sheet frame is installed handle.
Advantage of the present utility model and good effect be:
1, the dry flue gas desulphurization device that the desulfuration efficiency of this utility model offer is high has the desulfurization sheet frame of detachable installation, sheet frame is directly inserted in flue framework, flue gas passes through, and changes sulfur removal material the most simple and easy to do, and its exhaust gases passes is designed as left and right and two-way circulates, increase fume treatment area, improving desulfuration efficiency, also have desulfuration efficiency high, investment and running cost all ratios are relatively low, do not produce secondary pollution, be easily processed advantage up to standard.
2, flue gas is passed through removing means according to Flue duct design by the dry flue gas desulphurization device that the desulfuration efficiency of this utility model offer is high, it is not necessary to flue gas is carried out forward and backward process, after flue gas carries out adsorbing desulfurization, directly discharges, and it is the simplest, convenient to operate;Material replacing simultaneously is convenient, disposal ability is big, it is not necessary to the most more conversion materials, time saving and energy saving.
The installation of the high dry flue gas desulphurization device of desulfuration efficiency that 3, this utility model provides, dismantle and reload and be quite convenient to, provide the user with bigger convenience, simultaneously technique and simple, waste water is not the most produced without water, movement-less part, therefore not easy break-down, desulfurized effect is stable and easily dimmable.
Accompanying drawing explanation
Fig. 1 is the structural representation of this utility model dry flue gas desulphurization tower.
Detailed description of the invention
The utility model is described in further detail below in conjunction with the accompanying drawings and by specific embodiment, and following example are illustrative, are not determinate, it is impossible to limit protection domain of the present utility model with this.
The dry flue gas desulphurization device that a kind of desulfuration efficiency is high, including exhaust gases passes 8 and flue gas desulfurization material sheet frame 4, described flue gas is by for hollow rectangular framework, gas approach 10 it is shaped with in the middle part of exhaust gases passes, exhanst gas outlet 2 all it is shaped with in the left and right sides of exhaust gases passes, 9, exhaust gases passes top in the gas approach left and right sides is spaced and parallel is shaped with bar shaped jack, spaced and parallel in jack it is embedded with multiple flue gas desulfurization material sheet frame, in order to make flue gas try one's best perpendicular through flue gas desulfurization material sheet frame, exhanst gas outlet is installed blower fan 1, to form negative pressure in exhaust gases passes, contribute to flue gas to discharge.
The structure of described flue gas desulfurization material sheet frame is; including a square frame, housing is hollow and left and right sides opening, installs drainage screen 7 at left and right sides opening part; filling sulfur removal material 5 in housing between drainage screen, described sulfur removal material can be calcium hydroxide particle or calcium carbonate granule.In order to make flue gas desulfurization material sheet frame surrounding seal with exhaust gases passes, the interior survey installation sealing strip 6 of the position that contacts with exhaust gases passes at sheet frame, on the one hand can increase sealing, on the one hand also contribute to the position of fixing square frame.
For the ease of flue gas desulfurization material sheet frame is taken out in jack and installed, flue gas desulfurization material sheet frame is installed handle 3.
Claims (4)
1. the dry flue gas desulphurization device that a desulfuration efficiency is high, it is characterized in that: include exhaust gases passes and flue gas desulfurization material sheet frame, described flue gas is by for hollow rectangular framework, gas approach it is shaped with in the middle part of exhaust gases passes, exhanst gas outlet all it is shaped with in the left and right sides of exhaust gases passes, exhaust gases passes top in the gas approach left and right sides is spaced and parallel is shaped with bar shaped jack, spaced and parallel in jack it is embedded with multiple flue gas desulfurization material sheet frame, exhanst gas outlet is installed blower fan, the structure of described flue gas desulfurization material sheet frame is, including a square frame, housing is hollow and left and right sides opening, at left and right sides opening part, drainage screen is installed, sulfur removal material is filled in housing between drainage screen.
The dry flue gas desulphurization device that desulfuration efficiency the most according to claim 1 is high, it is characterised in that: described sulfur removal material is calcium hydroxide particle or calcium carbonate granule.
The dry flue gas desulphurization device that desulfuration efficiency the most according to claim 1 is high, it is characterised in that: the interior survey installation sealing strip of the position that contacts with exhaust gases passes at sheet frame.
The dry flue gas desulphurization device that desulfuration efficiency the most according to claim 1 is high, it is characterised in that: handle is installed on flue gas desulfurization material sheet frame.
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CN201620221979.XU CN205495334U (en) | 2016-03-22 | 2016-03-22 | Efficient dry flue gas desulfurization device of desulfurization |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107890771A (en) * | 2017-11-17 | 2018-04-10 | 钟玮家 | A kind of flue gas low-temperature dry desulfurization denitration process system and method |
CN109420428A (en) * | 2017-08-21 | 2019-03-05 | 江苏佳鑫环保工程有限公司 | A kind of dry desulfurization processing unit |
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2016
- 2016-03-22 CN CN201620221979.XU patent/CN205495334U/en active Active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109420428A (en) * | 2017-08-21 | 2019-03-05 | 江苏佳鑫环保工程有限公司 | A kind of dry desulfurization processing unit |
CN107890771A (en) * | 2017-11-17 | 2018-04-10 | 钟玮家 | A kind of flue gas low-temperature dry desulfurization denitration process system and method |
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