CN203540269U - Composite dust remover - Google Patents
Composite dust remover Download PDFInfo
- Publication number
- CN203540269U CN203540269U CN201320698926.3U CN201320698926U CN203540269U CN 203540269 U CN203540269 U CN 203540269U CN 201320698926 U CN201320698926 U CN 201320698926U CN 203540269 U CN203540269 U CN 203540269U
- Authority
- CN
- China
- Prior art keywords
- sack cleaner
- inertia force
- dust collector
- dust remover
- complex dust
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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- 239000000428 dust Substances 0.000 title claims abstract description 65
- 239000002131 composite material Substances 0.000 title abstract 3
- 239000012716 precipitator Substances 0.000 claims description 30
- 239000004744 fabric Substances 0.000 claims description 9
- 238000003860 storage Methods 0.000 claims description 8
- 238000001914 filtration Methods 0.000 claims description 4
- 238000005507 spraying Methods 0.000 claims description 3
- 239000011362 coarse particle Substances 0.000 abstract 2
- 230000002035 prolonged effect Effects 0.000 abstract 2
- 238000005299 abrasion Methods 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 4
- 239000008187 granular material Substances 0.000 description 4
- 238000010926 purge Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010410 dusting Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 230000003116 impacting effect Effects 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Images
Landscapes
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
The utility model provides a composite dust remover, comprising an inertia force dust remover (1) and a bag dust remover (4), wherein the lower end of the inertia force dust remover (1) is communicated with the lower end of the bag-type dust remover (4); a dust-containing gas inlet is formed at the upper end of the inertia force dust remover (1); an exhaust chamber (8) is arranged at the upper end of the bag-type dust remover (4). According to the composite dust remover based on the technical scheme, the inertia force dust remover is added in front of the bag-type dust remover, and large-diameter coarse particles can be firstly captured, so that abrasion on the filter bag caused by the coarse particles can be reduced. The concentration of the dust-containing gas entering the bag-type dust remover is reduced under the action of the front inertia force dust remover. Therefore, the deashing interval time can be prolonged, the service life of the filter bag is prolonged, the dust concentration of the exhaust gas can be reduced, and the overall performance of the dust remover is improved.
Description
Technical field
The utility model relates to a kind of dust arrester, relates in particular to a kind of inertia force pocket type complex dust collector.
Background technology
Traditional inertia force precipitator generally purifies density and larger metal or the mineral dust of particle diameter, and its purifying rate is not high, can trap coarse granules more than 10～20 μ m, therefore general the primary dust removing for multistage dedusting.Sack cleaner efficiency of dust collection is high, stable, and strong adaptability is widely used in the dust purification that multiple industry production produces.The dust removal process of described sack cleaner is mainly completed by filter bag, when adopting outside filtering type deduster, dust-contained airflow flows to inner side by filter bag outside, and dust is captured and is deposited on filter bag outer surface, in its filter bag, will be provided with support frame, so filter bag wearing and tearing are larger.
Therefore those skilled in the art wish to solve the deficiency of above-mentioned inertia force precipitator and sack cleaner always.
Summary of the invention
The purpose of this utility model is to provide a kind of complex dust collector that can overcome prior art defect.
To achieve these goals, the utility model has adopted following technical scheme: a kind of complex dust collector, and it includes inertia force precipitator and sack cleaner, and the lower end of described inertia force precipitator is communicated with the lower end of sack cleaner; The upper end of described inertia force precipitator is provided with dusty gas entrance, and the upper end of described sack cleaner is provided with exhaust chamber.
Further, the inlet plenum of the air channel of the lower end of described inertia force precipitator and the lower end of sack cleaner is communicated with.
Further, described sack cleaner inside is provided with the cloth bag for filtering gas, and the bottom of described sack cleaner is provided with for storing the storage ash bucket of the dust that cloth bag falls into.
Further, the baffle plate that strengthens gas rotating intensity is housed in described inertia force precipitator, the angle α of this baffle plate and horizontal direction is 30-45 °, to strengthen coarse grained removal efficiency.
Further, in described inertia force pocket type complex dust collector, the storage ash bucket sidewall of described sack cleaner and the angle β of horizontal direction are greater than 60 °, make deashing easier.
Further, described inertia force precipitator and described sack cleaner storage ash bottom are provided with unloading valve, for when clearing up the dust of deduster, carry out deashing open to shut to regulate.
Further, between the inlet plenum of described sack cleaner and exhaust chamber and sack cleaner body, be provided with valve body, for controlling the break-make situation of air-flow.
Further, the inlet plenum of described sack cleaner and exhaust chamber may be embodied as integral type setting, are provided with baffle plate so that inlet plenum and exhaust chamber are separated in the middle of it.
Adopted the complex dust collector of technique scheme, owing to having added inertia force precipitator before sack cleaner, the coarse granule that diameter is large can first be captured, and therefore contributes to reduce the wearing and tearing of coarse granule to filter bag, in addition, due to the effect of inertia force precipitator above, make to enter dusty gas concentration in sack cleaner and reduce, therefore can extend deashing interval time, extend the service life of filter bag, and can reduce the dust content of Exhaust Gas, improve the overall performance of deduster.
Accompanying drawing explanation
Fig. 1 is the structural representation sketch of complex dust collector described in the utility model;
Fig. 2 is the A-A cutaway view of complex dust collector shown in Fig. 1.
The specific embodiment
In order better to understand the object of the utility model complex dust collector, below in conjunction with its background, accompanying drawing and actual condition, its structure and function are described in detail.
The main feature of the utility model complex dust collector is, inertia force precipitator and sack cleaner are combined, the upper end of the inertia force precipitator of leading portion is provided with dusty gas entrance, the lower end of described inertia force precipitator is communicated with the lower end of the sack cleaner of back segment, gas vent after the upper end of described sack cleaner is provided with and purifies.Wherein, the inertia force dedusting area of leading portion can trap coarse granule more than 10-20 μ m, and the bag-type dust district of back segment can trap the dustshot of 0.1-10 μ m, so the utility model can carry out thick dedusting and smart dedusting simultaneously.
Below in conjunction with accompanying drawing, the structure of the utility model specific embodiment is described in detail:
Fig. 1 is the utility model inertia force pocket type complex dust collector structural representation sketch.As shown in Figure 1, described inertia force pocket type complex dust collector includes inertia force precipitator 1 and sack cleaner 4, the air channel of the lower end of described inertia force precipitator 1 is communicated with the inlet plenum 3 of the lower end of sack cleaner 4, and the Purge gas after inertia force precipitator is processed enters sack cleaner through the inlet plenum 3 of described air channel and sack cleaner; The upper end of described inertia force precipitator 1 is provided with dusty gas entrance, and the upper end of described sack cleaner 4 is provided with the exhaust chamber 8 for the discharge of dedusting after-purification gas; Described sack cleaner 4 inside are provided with the cloth bag 5 for filtering gas, and the bottom of described sack cleaner 4 is provided with for storing the ash bucket 10 of the dust that cloth bag 5 falls into.
In described inertia force pocket type complex dust collector, in described inertia force precipitator, baffle plate is housed, the angle α of this baffle plate and horizontal direction is 30-45 °, to strengthen the spin intensity of gas, strengthens coarse grained removal efficiency.
In described inertia force pocket type complex dust collector, the storage ash bucket sidewall of described sack cleaner and the angle β of horizontal direction are greater than 60 °, make deashing easier.
In described inertia force pocket type complex dust collector, described inertia force precipitator and described sack cleaner storage ash bottom are provided with unloading valve 11, for when clearing up the dust of deduster, carry out deashing open to shut to regulate.
In described inertia force pocket type complex dust collector, between the inlet plenum 3 of described sack cleaner and exhaust chamber 8 and sack cleaner body, be provided with valve body, for controlling the break-make situation of air-flow.
Described inertia force pocket type meets in deduster, and the top of described sack cleaner is provided with compressed air spraying pipe 9.
When the air quantity of processing is larger, described inertia force pocket type complex dust collector further may be embodied as and includes two or more fiber bag precipitators, described two or more sack cleaner is set up in parallel, its inlet plenum is all communicated in the air channel that inertia force precipitator is processed rear gas, from described inertia force precipitator Purge gas out, because air quantity is larger, enter respectively two or more sack cleaners.
When the air quantity of processing is larger, inlet plenum 3 and the exhaust chamber 8 in described bag-type dusting district may be embodied as integral type setting, are provided with baffle plate so that inlet plenum and exhaust chamber are separated in the middle of it.
Below in conjunction with accompanying drawing and said structure, the course of work of the utility model specific embodiment is described in detail:
As Fig. 1, shown in Fig. 2, first dusty gas is entered the inertia force dedusting area of complex dust collector by the dusty gas entrance of inertial dust separator 1, air-flow is along channel flow, after impacting on baffle plate 2, airflow direction generation drastic shift, inertia force effect due to grit itself, grit and flow separation, thick grit more than this section of main trapping 10-20 μ m, through inertial dust separator purified gas, by the air channel of lower end and the inlet plenum 3 in bag-type dust district, entered in the sack cleaner 4 of back segment, this section can catch the dustshot of 0.1-10 μ m, Purge gas after cloth bag 5 filters is got rid of through exhaust chamber 8 by sack cleaner 4 upper ends.When sack cleaner is carried out to deashing, adopt off-line ash-clearing, close and need the valve 6 of the inlet plenum of deashing 3 and exhaust chamber 8 and valve 7, open the electromagnetic impulse valve of respective chamber/chambers, compressed air carries out deashing by 9 pairs of cloth bags of compressed air spraying pipe 5, dust falls into ash bucket 10, regularly through unloading valve 11, discharges.
Adopted the inertia force pocket type complex dust collector of said structure, can carry out thick dedusting and smart dedusting simultaneously, by inertia force precipitator, removing the thick grit that removes on the one hand can play a protective role to cloth bag below, effectively extenuates the wearing and tearing of bulky grain to filter bag, extends the service life of filter bag; Meanwhile, due to the effect of inertia force precipitator, greatly reduce the dust content that enters sack cleaner, thereby realize the concentration of emission that meets environmental requirement, improved the effect of deduster overall performance.
The above is only a kind of specific embodiment of complex vibration device described in the utility model; it should be pointed out that for those skilled in the relevant art, under the premise without departing from the principles of the invention; trickle modification and the improvement made, also should be considered as belonging to protection domain of the present utility model.
Claims (10)
1. a complex dust collector, is characterized in that, includes inertia force precipitator (1) and sack cleaner (4), and the lower end of described inertia force precipitator (1) is communicated with the lower end of sack cleaner (4); The upper end of described inertia force precipitator (1) is provided with dusty gas entrance, and the upper end of described sack cleaner (4) is provided with exhaust chamber (8).
2. complex dust collector as claimed in claim 1, is characterized in that, the air channel of the lower end of described inertia force precipitator (1) is communicated with the inlet plenum (3) of the lower end of sack cleaner (4).
3. complex dust collector as claimed in claim 1, it is characterized in that, described sack cleaner (4) inside is provided with the cloth bag (5) for filtering gas, and the bottom of described sack cleaner (4) is provided with for storing the storage ash bucket (10) of the dust that cloth bag (5) falls into.
4. complex dust collector as claimed in claim 1, is characterized in that, the baffle plate that strengthens gas rotating intensity is housed in described inertia force precipitator, and the angle α of this baffle plate and horizontal direction is 30-45 °.
5. complex dust collector as claimed in claim 1, is characterized in that, the sidewall of the storage ash bucket 10 of described sack cleaner and the angle β of horizontal direction are greater than 60 °.
6. complex dust collector as claimed in claim 1, is characterized in that, the bottom of described inertia force precipitator is provided with unloading valve.
7. complex dust collector as claimed in claim 1, is characterized in that, the bottom of the storage ash bucket 10 of described sack cleaner is provided with unloading valve.
8. complex dust collector as claimed in claim 3, is characterized in that, the top of described sack cleaner is provided with compressed air spraying pipe (9).
9. complex dust collector as claimed in claim 2, is characterized in that, between the inlet plenum of described sack cleaner (3) and exhaust chamber (8) and sack cleaner body, is provided with valve body, for controlling the break-make situation of air-flow.
10. complex dust collector as claimed in claim 2, is characterized in that, the inlet plenum of described sack cleaner (3) and exhaust chamber (8) are integral type setting, is provided with baffle plate so that inlet plenum and exhaust chamber are separated in the middle of it.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320698926.3U CN203540269U (en) | 2013-11-07 | 2013-11-07 | Composite dust remover |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320698926.3U CN203540269U (en) | 2013-11-07 | 2013-11-07 | Composite dust remover |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203540269U true CN203540269U (en) | 2014-04-16 |
Family
ID=50458439
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320698926.3U Expired - Lifetime CN203540269U (en) | 2013-11-07 | 2013-11-07 | Composite dust remover |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203540269U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105854480A (en) * | 2016-04-27 | 2016-08-17 | 云南华云天朗环保有限责任公司 | Composite dedusting method for high-concentration, high-temperature, high-humidity and large-particle kiln exhaust |
| CN106110824A (en) * | 2016-08-31 | 2016-11-16 | 福建铁拓机械有限公司 | A kind of sack cleaner improving service life and dust collection method thereof |
| CN107115723A (en) * | 2017-05-23 | 2017-09-01 | 中国北方车辆研究所 | A kind of dust collect plant |
| CN109908667A (en) * | 2019-04-30 | 2019-06-21 | 廊坊中建机械有限公司 | Surge tank and dust pelletizing system |
-
2013
- 2013-11-07 CN CN201320698926.3U patent/CN203540269U/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105854480A (en) * | 2016-04-27 | 2016-08-17 | 云南华云天朗环保有限责任公司 | Composite dedusting method for high-concentration, high-temperature, high-humidity and large-particle kiln exhaust |
| CN106110824A (en) * | 2016-08-31 | 2016-11-16 | 福建铁拓机械有限公司 | A kind of sack cleaner improving service life and dust collection method thereof |
| CN107115723A (en) * | 2017-05-23 | 2017-09-01 | 中国北方车辆研究所 | A kind of dust collect plant |
| CN107115723B (en) * | 2017-05-23 | 2020-01-07 | 中国北方车辆研究所 | Dust collecting device |
| CN109908667A (en) * | 2019-04-30 | 2019-06-21 | 廊坊中建机械有限公司 | Surge tank and dust pelletizing system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140416 |
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| CX01 | Expiry of patent term |