CN102430292A - Cyclone dust removing tower - Google Patents
Cyclone dust removing tower Download PDFInfo
- Publication number
- CN102430292A CN102430292A CN2010102960553A CN201010296055A CN102430292A CN 102430292 A CN102430292 A CN 102430292A CN 2010102960553 A CN2010102960553 A CN 2010102960553A CN 201010296055 A CN201010296055 A CN 201010296055A CN 102430292 A CN102430292 A CN 102430292A
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- China
- Prior art keywords
- ash
- dust
- discharging device
- pipe
- fixed
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Abstract
The invention discloses a cyclone dust removing tower with a circular simple structure. The tower is provided with a gas outlet pipe orifice, an upper cyclone disc, a lower cyclone disc, a supporting member, a gas inlet pipe orifice, an ash collecting bucket, an ash unloading device and an ash outlet, wherein the gas inlet pipe orifice is formed between the upper cyclone disc and the lower cyclone disc; and the gas outlet pipe orifice is formed on the top of a body. Dust is separated from dust-containing gas through cyclone inertia, falls into the dust collecting bucket from the cyclone disc and then is discharged to the ash outlet through the ash unloading device; and purified gas is discharged from the gas outlet pipe orifice on the top of the body. The tower is a dust removing facility, which has a simple and convenient structure and is effective in dust removal, convenient and safe in operation and low in operation cost, for dust control of production workshops of industries of leather, textile, resin, stone, casting and the like.
Description
Technical field
The present invention relates to a kind of industrial gas purifying device, relate in particular to a kind of spiral-flow type gas wash tower that adopts inertial separation.
Background technology
In the industries such as leather, weaving, resin, stone material, casting; The dust that workshop produced causes serious pollution to environment; Particularly some small business are not enough to the environmental improvement attention degree, and the safeguard procedures of being taked are ineffective, are the emphasis places that dust atmosphere is administered.
Summary of the invention
The objective of the invention is to containing the spiral-flow type gas wash tower that the dust industrial gasses provide a kind of features simple structure, better dust removal effect.
The present invention is a circular cylinder body structure, is provided with the mouth of pipe of giving vent to anger, body, forward spin flow dish, supporter, the air inlet mouth of pipe, following eddy flow tray, flue-dust retainer, ash-discharging device and cinder-discharging port.The air inlet mouth of pipe is located between forward spin flow dish and the following eddy flow tray, and the mouth of pipe of giving vent to anger is located at forward spin flow dish top, and flue-dust retainer is located at down the bottom of eddy flow tray, and flue-dust retainer is connected with ash-discharging device through flange, and the body bottom is provided with ash hole.The two-tube double-valve structure of ash-discharging device for dividing two-stage to form connects with ring flange between the two-stage ash-discharging device; Ash-unloading door and right angle screw rod are fixed into one, with respect to the sleeve rotation that is fixed on the cement output tank; Establish on the right angle screw rod and can move axially the balancing weight of transfer, the body bottom is provided with ash hole.
Send out the dusty gas that contains that dirt pits collects from each dust of workshop, be connected to air inlet of the present invention, contain dusty gas in air inlet gets into body; Under the blast effect, quality is produced gravity inertial greater than the dust of air, be able to buffering in the buffering wooden partition, fall into ash-discharging device along the inwall of division board, body, flue-dust retainer from ash port, dust is expelled to ash hole by ash-unloading door.And the Purge gas after the dedusting is discharged from the gas outlet.The present invention is that a kind of structure was simple and direct during dust atmosphere was administered, dedusting is effective, easy and safe to operate, spiral-flow type gas wash tower that operating cost is low.
Description of drawings
Fig. 1 is the structural representation of the embodiment of the invention.
Fig. 2 is that the A of Fig. 1 is to view.
Fig. 3 is an embodiment of the invention eddy flow tray structural representation.
Fig. 4 is an embodiment of the invention blade construction sketch map.
Fig. 5 is an embodiment of the invention blind plate structural representation.
Fig. 6 is an embodiment of the invention hook structure sketch map.
Fig. 7 is an embodiment of the invention ash-discharging device structural representation.
Fig. 8 is the vertical view of Fig. 7.
The specific embodiment
Referring to Fig. 1～8, the present invention is provided with the mouth of pipe 1 of giving vent to anger, body 2, forward spin flow plate 3, supporter 4, the air inlet mouth of pipe 5, following eddy flow plate 6, flue-dust retainer 7, flange 8, ash-discharging device 9 and ash hole 10.Contain dusty gas from what each dust origination point of workshop was collected, be connected to air inlet pipe mouth 5 mutually from pipeline, contain dusty gas and get in the bodies 2 through the air inlet mouth of pipe 5 through blower fan; The air inlet mouth of pipe 5 is located between forward spin flow plate 3 and the following eddy flow plate 6, and taper flue-dust retainer 7 is located at down under the eddy flow plate 6, and flue-dust retainer 7 connects in ash-discharging device 9 through flange 8; The bottom of body 2 is provided with ash hole 10.
Referring to Fig. 3～6, identical forward spin flow dish 3 and following eddy flow tray 6, installation direction is opposite.Eddy flow tray 3, (6) are provided with blind plate 31, blade 32, cranse 33 and link up with 34.Hook 34 is fixed on the blind plate 31, and blade 32 microcephalies insert hook 34, and blade 32 big end surface are fastening by two semi-circular cranses 33.
Referring to Fig. 7～8, ash-discharging device 9 joins through adpting flange 94 and adpting flange 8.The two-tube double-valve structure of ash-discharging device 9 for dividing two-stage to form is provided with cement output tank 92,91, ash bucket 93, adpting flange 94,97,98, ash port 95, ash-unloading door 96,912, balancing weight 99, right angle screw rod 910, adjustment nut 911, sleeve 913,915, axle sleeve 914 and fastening nut 916.Ash-unloading door 96,912 is fixed in right angle screw rod 910, with respect to sleeve 914 rotations that are fixed on the cement output tank 92,91, to open or to close ash-unloading door 96,912; Establishing pouring weight 99 on the right angle screw rod 910, through the position of adjustment nut 911 adjustment balancing weights 99, the dust weight destruction of balance in cement output tank 92,91, ash-unloading door 96,912 is opened; Connect with ring flange 97,98 between the two-stage ash-discharging device.Body 2 bottoms are provided with ash hole 10, and from then on the dust of gathering waits for outward transport.
Get into the intrinsic dusty gas that contains from the air inlet mouth of pipe 5; Under the blast effect; Quality is produced gravity inertial greater than the dust of air, along forward spin flow dish 3, down blade, body 2, the flue-dust retainer 7 of eddy flow tray 6 inwall through ash port 95 fall into ash-discharging device 9 cement output tank 92, get in the ash 93 through ash-unloading door 96; Drop down onto ash hole 10 from cement output tank 91, ash-unloading door 912 again.Purge gas after the dedusting is discharged from the mouth of pipe 6 of giving vent to anger.
Through test, the embodiment of the invention can reach following major parameter.
1. smoke dust discharge concentration≤200～150mg/m
3
2. lingemann blackness: 1 grade.
Claims (3)
1. a spiral-flow type gas wash tower is characterized in that being provided with the give vent to anger mouth of pipe, body, forward spin flow dish, supporter, the air inlet mouth of pipe, following eddy flow tray, flue-dust retainer, ash-discharging device and cinder-discharging port; The air inlet mouth of pipe is located between forward spin flow dish and the following eddy flow tray, and the mouth of pipe of giving vent to anger is located at forward spin flow dish top, and flue-dust retainer is located at down the bottom of eddy flow tray, and flue-dust retainer is connected with ash-discharging device through flange, and the body bottom is provided with ash hole; The two-tube double-valve structure of ash-discharging device for dividing two-stage to form connects with ring flange between the two-stage ash-discharging device; Ash-unloading door and right angle screw rod are fixed into one, with respect to the sleeve rotation that is fixed on the cement output tank; Establish on the right angle screw rod and can move axially the balancing weight of transfer, the body bottom is provided with ash hole.
2. a kind of spiral-flow type gas wash tower as claimed in claim 1 is characterized in that identical forward spin flow dish and following eddy flow tray, and installation direction is opposite; Eddy flow tray is provided with blind plate, blade, cranse and extension and purchases; Hook is fixed on the blind plate, and the blade microcephaly inserts hook, and the blade big end surface is fastening by two semi-circular cranses.
3. a kind of spiral-flow type gas wash tower as claimed in claim 1 is characterized in that ash-discharging device is the two-tube double-valve structure that the branch two-stage is formed, and connects with ring flange between the two-stage ash-discharging device; Ash-unloading door and right angle screw rod are fixed into one, with respect to the sleeve rotation that is fixed on the cement output tank; Establish on the right angle screw rod and can move axially the balancing weight of transfer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010102960553A CN102430292A (en) | 2010-09-29 | 2010-09-29 | Cyclone dust removing tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010102960553A CN102430292A (en) | 2010-09-29 | 2010-09-29 | Cyclone dust removing tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102430292A true CN102430292A (en) | 2012-05-02 |
Family
ID=45978863
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010102960553A Pending CN102430292A (en) | 2010-09-29 | 2010-09-29 | Cyclone dust removing tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102430292A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106512566A (en) * | 2017-01-12 | 2017-03-22 | 海宁蒙努皮革制品有限公司 | Cleaning device for sofa leather production workshop |
| CN107309065A (en) * | 2017-07-25 | 2017-11-03 | 贵州省华腾农业科技有限公司 | A kind of pulverizer dust collecting and its application method |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5387068A (en) * | 1977-01-10 | 1978-08-01 | Nippon Steel Corp | Apparatus for and method of removing dust contained in exhaust gas |
| CN2671672Y (en) * | 2004-01-08 | 2005-01-19 | 周文权 | Tubular bag type dust remover |
| CN2902422Y (en) * | 2006-03-10 | 2007-05-23 | 东莞市洛河神环保有限公司 | Cyclone type waste gas treatment device |
| CN201880437U (en) * | 2010-09-29 | 2011-06-29 | 张步芳 | Cyclone type dust removing tower |
-
2010
- 2010-09-29 CN CN2010102960553A patent/CN102430292A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5387068A (en) * | 1977-01-10 | 1978-08-01 | Nippon Steel Corp | Apparatus for and method of removing dust contained in exhaust gas |
| CN2671672Y (en) * | 2004-01-08 | 2005-01-19 | 周文权 | Tubular bag type dust remover |
| CN2902422Y (en) * | 2006-03-10 | 2007-05-23 | 东莞市洛河神环保有限公司 | Cyclone type waste gas treatment device |
| CN201880437U (en) * | 2010-09-29 | 2011-06-29 | 张步芳 | Cyclone type dust removing tower |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106512566A (en) * | 2017-01-12 | 2017-03-22 | 海宁蒙努皮革制品有限公司 | Cleaning device for sofa leather production workshop |
| CN107309065A (en) * | 2017-07-25 | 2017-11-03 | 贵州省华腾农业科技有限公司 | A kind of pulverizer dust collecting and its application method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20120502 |