CN205495155U - Spiral -flow type dust removal for boiler ware - Google Patents
Spiral -flow type dust removal for boiler ware Download PDFInfo
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- CN205495155U CN205495155U CN201620196852.7U CN201620196852U CN205495155U CN 205495155 U CN205495155 U CN 205495155U CN 201620196852 U CN201620196852 U CN 201620196852U CN 205495155 U CN205495155 U CN 205495155U
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- collecting pipe
- housing
- casing
- duster
- cyclone
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Abstract
The utility model discloses a spiral -flow type dust removal for boiler ware, including the casing, the upper end of casing is connected with the upper cover, and the lower extreme is connected with the low head, and ji chenkou is connected to the lower extreme of low head, being equipped with the air inlet on the upper portion of casing, being equipped with the collecting pipe in the inside axial of casing, the collecting pipe makes progress the reducing and extends to the casing appearance and become the gas vent, be provided with the shunt tubes that corresponds with the air inlet in the casing, the shunt tubes is fixed on the collecting pipe through the support cover that sets up on the collecting pipe, still is provided with the kuppe in the lower part of collecting pipe, the casing lower part is equipped with the baffle, and the baffle is connected with the dust leg downwards. Design like this the utility model discloses can effectually get rid of a large amount of dust particle in the boiler exhaust gas, reduce the pollution to atmosphere and all ring edge borders, also alleviateed simultaneously the enterprise production pressure, reduced economic loss. The utility model discloses simple structure, operation are reliable, and the dust collection efficiency can reach more than 90%, has wide application prospect.
Description
Technical field
This utility model belongs to a kind of cleaner unit, is specifically related to a kind of duster for cyclone-type boiler.
Background technology
At present, in boiler industry, most of boiler dust removal equipment separation efficiency are low, and boiler expellant gas contains in a large number
Dirt particle, Air Pollutant Emission is the most up to standard, causes the severe contamination of air and surrounding enviroment.Boiler dust removal equipment is general
Expensive, strict law enforcement and the great dynamics of environmental administration is imposed a fine in addition, has had a strong impact on the normal production of enterprise, has made to enterprise
Huge economic pressures and property loss are become.For solving an above-mentioned difficult problem, in the urgent need to a kind of efficient, reliable, economic boiler
Cleaner.
The current common method of gas solid separation has: filter separation, gravity inertial separates, centrifugal sedimentation separates.Wherein, filtration point
From method separation efficiency the highest, poor reliability；Gravity inertial separates needs bigger floor space, and separation efficiency is the most not
High.In actual applications, using universal separating for centrifugal sedimentation, capital equipment is Cyclonic separating apparatus, and separation efficiency is only
About 60%, treating capacity is the least, still can not meet the needs of actual production.
Utility model content
This utility model is contemplated to solve the problem that existing boiler dust remover efficiency of dust collection is the highest, the one proposed
Duster for cyclone-type boiler.
This utility model realizes according to techniques below scheme.
A kind of duster for cyclone-type boiler, including housing, the upper end of housing connects upper cover, and lower end connects lower envelope
Head, the lower end of low head connects dust collecting opening；It is provided with air inlet on the top of housing, is axially arranged with collecting pipe in enclosure interior, receive
Collector forms air vent outside upwards reducing extends to housing；The isocon corresponding with air inlet it is provided with in described housing, point
Flow tube is fixed on collecting pipe by the support set being arranged on collecting pipe, is additionally provided with kuppe in the bottom of collecting pipe；?
Described lower housing portion is provided with baffle plate, and baffle plate connects downwards dust leg.
Connect on the outer surface of the 2/3 of described isocon and have a support set, air inlet and the isocon being not connected with support set
The outer surface of 1/3 is relative.
Described collecting pipe upper end is diameter tube, and lower end is expansion tube.
Described upper cover is that ramp shaped is the most circular, and low head is taper；The bottom of collecting pipe is bell-mouth structure of air, and baffle plate is
V-shaped structure.
The height of described housing is 5.8:1～6.2:1 with the ratio of internal diameter.
The internal diameter of described air inlet is 0.28:1～0.58:1 with the ratio of the internal diameter of housing.
The internal diameter of described dust collecting opening is 0.22:1～0.42:1 with the ratio of the internal diameter of housing.
This utility model obtains following beneficial effect.
This utility model effectively solves the problem that existing boiler dust remover efficiency of dust collection is the highest.So basis of design
Utility model can effectively remove substantial amounts of dirt particle in boiler emission gas, reduces air and the dirt of surrounding enviroment
Dye, also mitigates the production pressure of enterprise simultaneously, decreases economic loss.This utility model simple in construction, reliable, dedusting
Efficiency, up to more than 90%, has broad application prospects.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model；
Fig. 2 is top view of the present utility model.
Wherein: 1 housing 2 air inlet
3 isocon 4 baffle plates
5 dust leg 6 dust collecting opening
7 collecting pipe 8 kuppes
9 support set 10 air vents.
Detailed description of the invention
Below in conjunction with the accompanying drawings and this utility model is described in detail by embodiment.
As shown in Figure 1, 2, a kind of duster for cyclone-type boiler, including housing 1, the upper end of housing 1 connects upper cover, under
End connection has low head, and the lower end of low head connects dust collecting opening 6；Circular air inlet 2 it is provided with, in housing 1 on the top of housing 1
Portion is axially arranged with collecting pipe 7, and collecting pipe 7 upwards reducing extends to housing 1 outer formation air vent 10；Arrange in described housing 1
Having the isocon 3 corresponding with air inlet 2, isocon 3 is fixed on collecting pipe 7 by the support set 9 being arranged on collecting pipe 7,
It is additionally provided with kuppe 8 in the bottom of collecting pipe 7；Baffle plate 4, baffle plate 4 outer rim and housing 1 inwall it is provided with in described housing 1 bottom
Between leave certain space, baffle plate 4 center has circular hole, and baffle plate 4 connects downwards dust leg 5.
Connect on the outer surface of the 2/3 of described isocon 3 and have support set 9, air inlet 2 and the shunting being not connected with support set 9
The outer surface of the 1/3 of pipe 3 is relative.Tangent with the cylindrical outer wall of the 1/3 of isocon 3 by the gas of air inlet 2, isocon 3 is
Ceramic material.
Described collecting pipe 7 upper end is diameter tube, and lower end is expansion tube.The lower end of support set 9 is the variable-diameter joint of collecting pipe 7
Point.
Described upper cover is that ramp shaped is the most circular, and low head is taper；The bottom of collecting pipe 7 is bell-mouth structure of air, baffle plate 4
For v-shaped structure.
The height of described housing 1 is 5.8:1～6.2:1 with the ratio of internal diameter.
The internal diameter of described air inlet 2 is 0.28:1～0.58:1 with the ratio of the internal diameter of housing 1.
The internal diameter of described dust collecting opening 6 is 0.22:1～0.42:1 with the ratio of the internal diameter of housing 1.
Work process of the present utility model is: after boiler emission gas enters air inlet 2, and conventional tangential admission is changed into
Half tangential entrance housing 1, portion gas collides with 1/3 column part of isocon 3, the gas of collision rift and another part gas
Body mutually collides formation turbulent flow, and owing to gas temperature is higher, the chance making molecule in air-flow mutually clash into increases, and is formed relatively
Bulky grain, downwards, under the influence of centrifugal force, bigger granule is got rid of to housing 1 inwall, drops to housing 1 end in tangential rotation
The probability in portion increases, thus improves separation efficiency, owing to the effect of gravity drops to bottom housing 1, has separated so for the first time
Become.The gas being rotated down, after kuppe 8, defines quick local mixing flow field, makes small contained in gas
Grain collides to condense and merges, and forms sedimentation, completes second time gas solid separation.Rotate downward air-flow to turn to through baffle plate 4, due to
The effect of centrifugal force, completes third time gas solid separation in collecting pipe 7.Gas after three gas solid separation passes through collecting pipe
The air vent 10 on the top of 7 is discharged, and the granule collected collects bottom housing 1, is discharged outside housing 1 by dust collecting opening 6.
Claims (7)
1. a duster for cyclone-type boiler, including housing (1), it is characterised in that: the upper end of housing (1) connects upper cover,
Lower end connects low head, and the lower end of low head connects dust collecting opening (6)；It is provided with air inlet (2), at shell on the top of housing (1)
Body (1) is internal is axially arranged with collecting pipe (7), and collecting pipe (7) upwards reducing extends to housing (1) and forms outward air vent (10)；?
Being provided with the isocon (3) corresponding with air inlet (2) in described housing (1), isocon (3) is by being arranged on collecting pipe (7)
Support set (9) be fixed on collecting pipe (7), be additionally provided with kuppe (8) in the bottom of collecting pipe (7)；In described housing (1)
Bottom is provided with baffle plate (4), and baffle plate (4) connects downwards dust leg (5).
A kind of duster for cyclone-type boiler the most according to claim 1, it is characterised in that: the 2/3 of described isocon (3)
Connect on outer surface and have a support set (9), air inlet (2) with the 1/3 of the isocon (3) being not connected with support set (9) outer surface phase
Right.
A kind of duster for cyclone-type boiler the most according to claim 1, it is characterised in that: described collecting pipe (7) upper end is
Diameter tube, lower end is expansion tube.
A kind of duster for cyclone-type boiler the most according to claim 1, it is characterised in that: described upper cover is that ramp shaped is excessive
Circle, low head is taper；The bottom of collecting pipe (7) is bell-mouth structure of air, and baffle plate (4) is v-shaped structure.
A kind of duster for cyclone-type boiler the most according to claim 1, it is characterised in that: the height of described housing (1) with
The ratio of internal diameter is 5.8:1～6.2:1.
A kind of duster for cyclone-type boiler the most according to claim 1, it is characterised in that: the internal diameter of described air inlet (2)
It is 0.28:1～0.58:1 with the ratio of the internal diameter of housing (1).
A kind of duster for cyclone-type boiler the most according to claim 1, it is characterised in that: the internal diameter of described dust collecting opening (6)
It is 0.22:1～0.42:1 with the ratio of the internal diameter of housing (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620196852.7U CN205495155U (en) | 2016-03-15 | 2016-03-15 | Spiral -flow type dust removal for boiler ware |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620196852.7U CN205495155U (en) | 2016-03-15 | 2016-03-15 | Spiral -flow type dust removal for boiler ware |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205495155U true CN205495155U (en) | 2016-08-24 |
Family
ID=56728363
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620196852.7U Active CN205495155U (en) | 2016-03-15 | 2016-03-15 | Spiral -flow type dust removal for boiler ware |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205495155U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI649116B (en) * | 2018-03-28 | 2019-02-01 | X'pole Precision Tools Inc. | Dust collection device for filtering dust with multiple cyclones |
| TWI704959B (en) * | 2019-08-23 | 2020-09-21 | 鼎朋企業股份有限公司 | Multi-cyclone dust filter |
| CN114737900A (en) * | 2021-12-27 | 2022-07-12 | 核工业北京化工冶金研究院 | Static rotational flow well washing device and method for cleaning ground immersed borehole |
| CN115282696A (en) * | 2022-08-24 | 2022-11-04 | 浙江艾卡蒙特环保科技有限公司 | Waste gas treatment device |
-
2016
- 2016-03-15 CN CN201620196852.7U patent/CN205495155U/en active Active
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI649116B (en) * | 2018-03-28 | 2019-02-01 | X'pole Precision Tools Inc. | Dust collection device for filtering dust with multiple cyclones |
| CN110314454A (en) * | 2018-03-28 | 2019-10-11 | 鼎朋企业股份有限公司 | With the dust collecting of multiple cyclonic dust filtering |
| CN110314454B (en) * | 2018-03-28 | 2022-03-01 | 鼎朋企业股份有限公司 | Dust collecting device for filtering dust by multiple cyclones |
| TWI704959B (en) * | 2019-08-23 | 2020-09-21 | 鼎朋企業股份有限公司 | Multi-cyclone dust filter |
| CN114737900A (en) * | 2021-12-27 | 2022-07-12 | 核工业北京化工冶金研究院 | Static rotational flow well washing device and method for cleaning ground immersed borehole |
| CN115282696A (en) * | 2022-08-24 | 2022-11-04 | 浙江艾卡蒙特环保科技有限公司 | Waste gas treatment device |
| CN115282696B (en) * | 2022-08-24 | 2024-02-27 | 湖南鼎格云天环保科技股份有限公司 | Waste gas treatment device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 300384 Tianjin hi tech District of Xiqing City Huayuan Industrial Zone Development six road No. 6 Haitai green industry base building J room 104 Patentee after: China core (Tianjin) New Technology Development Co., Ltd. Address before: 300384 Tianjin hi tech District of Xiqing City Huayuan Industrial Zone Development six road No. 6 Haitai green industry base building J room 104 Patentee before: Huahe New Technology Development Company, Research Institute of Physical and Chemical Engineering of Nuclear Industry |
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| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20200304 Address after: 300180, No. 168 Jintang Road, Hedong District, Tianjin Patentee after: Inst. of Physics and Chemistry Engineering Address before: 300384 Tianjin hi tech District of Xiqing City Huayuan Industrial Zone Development six road No. 6 Haitai green industry base building J room 104 Patentee before: China core (Tianjin) New Technology Development Co., Ltd. |