CN201711053U - Big bag-type dust collector with brick-concrete structure - Google Patents
Big bag-type dust collector with brick-concrete structure Download PDFInfo
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- CN201711053U CN201711053U CN2010202540054U CN201020254005U CN201711053U CN 201711053 U CN201711053 U CN 201711053U CN 2010202540054 U CN2010202540054 U CN 2010202540054U CN 201020254005 U CN201020254005 U CN 201020254005U CN 201711053 U CN201711053 U CN 201711053U
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- flue gas
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- dust collector
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Abstract
The utility model discloses a big bag-type dust collector with a brick-concrete structure. The dust collector comprises a dust collector body, and a flue gas inlet, induced air opening and a reverse air opening formed on the dust collector body; the dust collector body is divided into a flue gas mixing chamber, a working chamber and an ash accumulating chamber through an upper tube sheet and a lower tube sheet which are arranged in the dust collector body; the working chamber is arranged between the upper tube sheet and the lower tube sheet; filter bags evenly mounted on the upper tube sheet and the lower tube sheet are arranged in the working chamber; the flue gas mixing chamber and the ash accumulating chamber are respectively positioned at the upper end and the lower end of the working chamber; the dust collector body is provided with a brick-concrete structure; the flue gas inlet is formed on the left side of the top of the flue gas mixing chamber; the induced air opening is formed on the right side of the bottom of the working chamber; and the reverse air opening is formed at the central part of the working chamber and positioned on one side of the induced air opening. The dust collector has the advantages of compact structure, reasonable design, steady and reliable use, effective filtration of flue gas and dust, obvious filtration effect, low manufacture and use cost, no need of frequent maintenance, and large application range.
Description
Technical field
The utility model relates to a kind of cleaner, especially relates to the big sack cleaner of a kind of brick mix structure.
Background technology
Sack cleaner is a kind of equipment that utilizes organic fiber filtering material or inorganic fiber filtration material that the dust-filtering in the dusty gas is come out, can be used for filtering the industrial dust of non-cohesiveness and non-fiber, its effect in cement production process is particularly outstanding.The sack cleaner that is used for cement production process in the prior art, mainly form the deduster body by steel construction, as shown in Figure 1, its top is air-purifying chamber 4-1, and the middle part is operating room 5, and the bottom is an ash accumulating chamber 6,5 inside, operating room are provided with filter bag 7, the side of air-purifying chamber 4-1 is provided with air- vent 2,5 bottoms, operating room and be positioned at air-vent 2 belows one side blowback air port 3 is set, and operating room's 5 bottom opposite sides are provided with gas approach 1.There is following shortcoming in actual use in the sack cleaner of this structure: (1) because the smoke moisture that produces in process of production of cement is bigger, and contains macro-corrosion gas in the flue gas, can cause certain corrosion to deduster; (2) because of the deduster body adopts steel construction, flue gas is bigger at air inducing pipeline and enclosure interior heat loss in dust removal process, makes the sack cleaner internal condensation, and very easily makes filter bag fuzzy, has influenced dust removing effects; (3) need artificial often cleaning filter bag, and the multipotency of filter bag used 10 months, flue and card use at most and just needed in 2 years to change, and cause the significant wastage of human and material resources and financial resources; (4) cross-sectional diameter of filter bag is less, and is generally 110mm～130mm, and is therefore little to the filter area of flue gas.
The utility model content
Technical problem to be solved in the utility model is at above-mentioned deficiency of the prior art, provide a kind of brick mix structure big sack cleaner, its compact conformation, reasonable in design and use reliable and stable, can effectively realize filtration to exhaust gas dust, and filter effect is obvious, it is low to make use cost simultaneously, need not frequent maintenance, applied widely.
For solving the problems of the technologies described above, the technical solution adopted in the utility model is: the big sack cleaner of a kind of brick mix structure, comprise deduster body and the gas approach that is opened on the described deduster body, air-vent and blowback air port, described deduster body is divided into flue gas mixing-chamber by the upper face plate and the lower face plate of the portion of setting within it with described deduster body, operating room and ash accumulating chamber, part is the operating room between described upper face plate and the lower face plate, inside, described operating room is provided with the filter bag that evenly is installed on upper face plate and the lower face plate, described flue gas mixing-chamber and ash accumulating chamber lay respectively at the top and bottom of operating room, it is characterized in that: described deduster body is a brick mix structure deduster body, described gas approach is arranged on the flue gas mixing-chamber top left side, described air-vent is arranged on right side, bottom, operating room, and described blowback air port is arranged on the middle part, operating room and is positioned at a side of air-vent.
The big sack cleaner of above-mentioned brick mix structure, it is characterized in that: described air-vent is provided with coupled air inducing pipeline, described blowback air port is provided with coupled reverse-blow pipe road, described air inducing pipeline is provided with air-introduced machine, and described reverse-blow pipe road is provided with back blowing machine.
The big sack cleaner of above-mentioned brick mix structure is characterized in that: also comprise the pure qi (oxygen) delivery pipe that the lower end is connected with described air inducing pipeline, described pure qi (oxygen) delivery pipe middle and lower part is provided with a gas outlet, and described gas outlet is connected with end, described reverse-blow pipe road.
The big sack cleaner of above-mentioned brick mix structure is characterized in that: described filter bag is cylindric, and its cross-sectional diameter is 260mm～300mm.
The utility model compared with prior art has the following advantages:
1, compact conformation, reasonable in design, this deduster adopt brick mix structure to make, and gas approach is arranged on the flue gas mixing-chamber top left side, and air-vent is arranged on right side, bottom, operating room, and the blowback air port is arranged on the middle part, operating room and is positioned at a side of air-vent.
2, use is reliable and stable, because this deduster adopts brick mix structure to make, therefore not only efficiently solve in the prior art steel construction deduster easy problem of dewfall at work, reduced corrosion function to filter bag, and can make the inner environment that forms a relative steady temperature and humidity of deduster, guaranteed the deduster operate as normal, it is low to make use cost simultaneously, applied widely.
3, can effectively realize filtration to exhaust gas dust, and filter effect is obvious, because this deduster is rationally laid gas approach, air-vent, blowback air port and pure qi (oxygen) delivery pipe, make flue gas flow direction flow to consistent (all being from top to bottom) with dust, not only effectively prevent reentrainment of dust, and reduced the operation power of deduster.Owing to communicate between air inducing pipeline and the reverse-blow pipe road, therefore, not only make pure qi (oxygen) circulation after filtering participate in the blowback vane joint simultaneously, make attached to the dust on the filter bag easily to fall in the ash accumulating chamber with uniform temperature.
4, because this deduster adopts brick mix structure to make, and the filter bag cross-sectional diameter is bigger, therefore need not frequent maintain and replace, and maintenance cost is lower.
5, applied widely, can effectively use to cement, electric power and metallurgy industry processing procedure flue dust.
Below by drawings and Examples, the utility model is described in further detail.
Description of drawings
Fig. 1 is the structural representation of existing sack cleaner.
Fig. 2 is an overall structure schematic diagram of the present utility model.
Description of reference numerals:
The 1-gas approach; The 2-air-vent; 3-blowback air port;
The 4-1-air-purifying chamber; The 4-2-flue gas mixing-chamber; The 5-operating room;
6-ash accumulating chamber; The 7-filter bag; The 8-air-introduced machine;
The 9-back blowing machine; 10-pure qi (oxygen) delivery pipe; The 11-1-upper face plate;
The 11-2-lower face plate.
The specific embodiment
The big sack cleaner of a kind of brick mix structure as shown in Figure 2, comprise deduster body and the gas approach 1 that is opened on the described deduster body, air-vent 2 and blowback air port 3, described deduster body is divided into flue gas mixing-chamber 4-2 by the upper face plate 11-1 and the lower face plate 11-2 of the portion of setting within it with described deduster body, operating room 5 and ash accumulating chamber 6, part is operating room 5 between described upper face plate 11-1 and the lower face plate 11-2,5 inside, described operating room are provided with the filter bag 7 that evenly is installed on upper face plate 11-1 and the lower face plate 11-2, described flue gas mixing-chamber 4-2 and ash accumulating chamber 6 lay respectively at the top and bottom of operating room 5, described deduster body is a brick mix structure deduster body, described gas approach 1 is arranged on flue gas mixing-chamber 4-2 top left side, described air-vent 2 is arranged on right side, 5 bottom, operating room, and described blowback air port 3 is arranged on 5 middle parts, operating room and is positioned at a side of air-vent 2.
As shown in Figure 2, described air-vent 2 is provided with coupled air inducing pipeline, and described blowback air port 3 is provided with coupled reverse-blow pipe road, and described air inducing pipeline is provided with air-introduced machine 8, and described reverse-blow pipe road is provided with back blowing machine 9.
As shown in Figure 2, the utility model also comprises the pure qi (oxygen) delivery pipe 10 that the lower end is connected with described air inducing pipeline, and described pure qi (oxygen) delivery pipe 10 middle and lower parts are provided with a gas outlet, and described gas outlet is connected with end, described reverse-blow pipe road.This pure qi (oxygen) delivery pipe is used to discharge the part pure qi (oxygen) after filter operating room 5.
In the utility model, described filter bag 7 is cylindric, and its cross-sectional diameter is 260mm～300mm.Cross-sectional diameter is the filter bag of 110mm～130mm in the prior art relatively, and its filter area is bigger, and filter effect is obvious.
Operation principle of the present utility model is: flue gas is entered by gas approach 1 during use, behind flue gas mixing-chamber 4-2, enter operating room 5, filter by the 7 pairs of flue gases of filter bag that are provided with in the operating room 5, impurity after the filtration falls into ash accumulating chamber 6, pure qi (oxygen) is through air inducing pipeline flow-direction pure qi (oxygen) delivery pipe 10, then most of pure qi (oxygen) is discharged from pure qi (oxygen) delivery pipe 10, be connected with end, reverse-blow pipe road owing to pure qi (oxygen) delivery pipe 10 simultaneously, therefore, when blowback wind is worked, the sub-fraction pure qi (oxygen) is sent into operating room 5 again behind back blowing machine 9, filter bag 7 is carried out reverse gas cleaning.In entire work process, aspirate by 8 pairs of flue gases of air-introduced machine, accelerated the rate of filtration of flue gas, and owing to communicate between pure qi (oxygen) delivery pipe 10 and the reverse-blow pipe road, make after filtering pure qi (oxygen) participate in during the blowback vane saves with uniform temperature.Therefore, overcome effectively not only that flue gas has guaranteed the deduster operate as normal, and avoided the flue gas reentrainment of dust that in air inducing pipeline and easy dewfall of enclosure interior and the easily fuzzy problem of filter bag promptly the dust trend is consistent with wind direction, all from top to bottom in the prior art.In addition,, effectively brought into play the resonance usefulness of air inducing and blowback wind, made easily to fall in the ash accumulating chamber 6, reduced the operation power of deduster simultaneously attached to the dust on the filter bag 7 because blowback air port 3 is positioned at 5 middle parts, operating room.
In the utility model, because the deduster body adopts brick mix structure to make, therefore, not only efficiently solve the easy problem of dewfall at work of steel construction deduster in the prior art, reduced corrosion function to filter bag, and it is slow to have heat conduction, thermal losses is little, the heat of attracting deposit is regulated the characteristics of flue-gas temperature, promptly when flue-gas temperature is lower, the heat of storage inside is discharged, reach the effect of regulating temperature, make the inner environment that forms a relative steady temperature and humidity of deduster, satisfied the demand of burning till, guaranteed the deduster operate as normal, greatly reduce cost of manufacture simultaneously, it is about 30% that its relative steel construction deduster cost reduces, and has tangible price advantage.
The above; it only is preferred embodiment of the present utility model; be not that the utility model is imposed any restrictions; everyly any simple modification that above embodiment did, change and equivalent structure are changed, all still belong in the protection domain of technical solutions of the utility model according to the utility model technical spirit.
Claims (4)
1. big sack cleaner of brick mix structure, comprise deduster body and the gas approach (1) that is opened on the described deduster body, air-vent (2) and blowback air port (3), described deduster body is divided into flue gas mixing-chamber (4-2) by the upper face plate (11-1) and the lower face plate (11-2) of the portion of setting within it with described deduster body, operating room (5) and ash accumulating chamber (6), part is operating room (5) between described upper face plate (11-1) and the lower face plate (11-2), inside, described operating room (5) is provided with the filter bag (7) that evenly is installed on upper face plate (11-1) and the lower face plate (11-2), described flue gas mixing-chamber (4-2) and ash accumulating chamber (6) lay respectively at the top and bottom of operating room (5), it is characterized in that: described deduster body is a brick mix structure deduster body, described gas approach (1) is arranged on flue gas mixing-chamber (4-2) top left side, described air-vent (2) is arranged on right side, bottom, operating room (5), and described blowback air port (3) is arranged on middle part, operating room (5) and is positioned at a side of air-vent (2).
2. according to the big sack cleaner of the described brick mix structure of claim 1, it is characterized in that: described air-vent (2) is provided with coupled air inducing pipeline, described blowback air port (3) is provided with coupled reverse-blow pipe road, described air inducing pipeline is provided with air-introduced machine (8), and described reverse-blow pipe road is provided with back blowing machine (9).
3. according to the big sack cleaner of the described brick mix structure of claim 2, it is characterized in that: also comprise the pure qi (oxygen) delivery pipe (10) that the lower end is connected with described air inducing pipeline, described pure qi (oxygen) delivery pipe (10) middle and lower part is provided with a gas outlet, and described gas outlet is connected with end, described reverse-blow pipe road.
4. according to the big sack cleaner of the described brick mix structure of claim 1, it is characterized in that: described filter bag (7) is for cylindric, and its cross-sectional diameter is 260mm～300mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202540054U CN201711053U (en) | 2010-07-08 | 2010-07-08 | Big bag-type dust collector with brick-concrete structure |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202540054U CN201711053U (en) | 2010-07-08 | 2010-07-08 | Big bag-type dust collector with brick-concrete structure |
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| Publication Number | Publication Date |
|---|---|
| CN201711053U true CN201711053U (en) | 2011-01-19 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010202540054U Expired - Fee Related CN201711053U (en) | 2010-07-08 | 2010-07-08 | Big bag-type dust collector with brick-concrete structure |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106076017A (en) * | 2016-08-18 | 2016-11-09 | 太仓市冠东机械科技有限公司 | A kind of electrical dust-removing exhauster |
| CN106215556A (en) * | 2016-08-29 | 2016-12-14 | 合肥合意环保科技工程有限公司 | A kind of shaft kiln glass cleaner |
| CN106245197A (en) * | 2016-08-31 | 2016-12-21 | 何县香 | A kind of composite fibre filtering material and preparation method thereof |
| CN112426811A (en) * | 2020-11-03 | 2021-03-02 | 虞小梅 | Pitch waste gas bag filter equipment based on reverse air current deashing |
| CN114470984A (en) * | 2022-01-24 | 2022-05-13 | 杭州卓尔净化工程有限公司 | Circulation self-cleaning formula high-pressure pulse dust remover |
-
2010
- 2010-07-08 CN CN2010202540054U patent/CN201711053U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106076017A (en) * | 2016-08-18 | 2016-11-09 | 太仓市冠东机械科技有限公司 | A kind of electrical dust-removing exhauster |
| CN106215556A (en) * | 2016-08-29 | 2016-12-14 | 合肥合意环保科技工程有限公司 | A kind of shaft kiln glass cleaner |
| CN106245197A (en) * | 2016-08-31 | 2016-12-21 | 何县香 | A kind of composite fibre filtering material and preparation method thereof |
| CN112426811A (en) * | 2020-11-03 | 2021-03-02 | 虞小梅 | Pitch waste gas bag filter equipment based on reverse air current deashing |
| CN114470984A (en) * | 2022-01-24 | 2022-05-13 | 杭州卓尔净化工程有限公司 | Circulation self-cleaning formula high-pressure pulse dust remover |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110119 Termination date: 20140708 |
|
| EXPY | Termination of patent right or utility model |