CN103566685B - A kind of spiral fog-type dust collector - Google Patents
A kind of spiral fog-type dust collector Download PDFInfo
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- CN103566685B CN103566685B CN201310538036.0A CN201310538036A CN103566685B CN 103566685 B CN103566685 B CN 103566685B CN 201310538036 A CN201310538036 A CN 201310538036A CN 103566685 B CN103566685 B CN 103566685B
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- main shaft
- rotary main
- water wheels
- baffle plate
- dust collector
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Abstract
The invention provides a kind of spiral fog-type dust collector, it includes: housing, formation processing space in it; Be arranged at the admission line on described housing, extraneous gas is introduced in described process space by it; Outside liquid can be introduced the water inlet in described process space; Extend into the rotary main shaft in described process space; Be located at the induction fan on rotary main shaft, mixed water wheels and point water wheels successively with the bearing of trend along rotary main shaft, described rotary main shaft drives described induction fan, mixed water wheels and point water wheels synchronous axial system.Spiral fog-type dust collector of the present invention have remove harmful components in gas, water consumption is few, power consumption is little, dedusting scope is wide, efficiency of dust collection is high, the dedusting cycle fast, circulating water, without the need to advantages such as cleaning, energy-conserving and environment-protective.
Description
Technical field
The present invention relates to a kind of dust removal machine, especially in regard to a kind of spiral fog-type dust collector.
Background technology
In general, present dry dust removal machine efficiency of dust collection is high, but involve great expense, floor space is large, and dry dust removal machine can only remove most of solid dust, the harmful components in gas can not being removed, easily causing reentrainment of dust when dealing with improperly, also have and to produce when processing the relatively high fuel gas and dust of humidity that dust coheres, the phenomenon of blocking pipe, need take to clear up measure especially.And Wet dust collector structure is simple, initial investment is few, goes back the harmful components in Absorbable rod gas, but efficiency of dust collection is not as dry dust removal machine, and water consumption is large, and power consumption is large, the dust-laden sewage of discharging must arrange sewage treatment facility and carry out two stage treatment, and overall energy consumption is higher.These two kinds of dust removal machines are easily made dirty when running into the oil smoke easily adhered to dust removal machine, and are not easy to dismounting and cleaning.
Summary of the invention
The technical problem to be solved in the present invention is to provide a kind ofly can remove harmful components in gas, water consumption is few, power consumption is little, dedusting scope is wide, efficiency of dust collection is high, the dedusting cycle fast, circulating water, the quick detachable spiral fog-type dust collector without the need to cleaning, energy-conserving and environment-protective.
For solving the problems of the technologies described above, the invention provides a kind of spiral fog-type dust collector, including
Housing, formation processing space in it;
Be arranged at the admission line on described housing, extraneous gas is introduced in described process space by it; With
Outside liquid can be introduced the water inlet in described process space, it is characterized in that: described spiral fog-type dust collector also includes
Extend into the rotary main shaft in described process space; With
Bearing of trend along rotary main shaft is located at the induction fan on rotary main shaft, mixed water wheels and point water wheels successively, and described rotary main shaft drives described induction fan, mixed water wheels and point water wheels synchronous axial system,
When described rotary main shaft rotates, under the driving of described induction fan, extraneous gas is inhaled in described process space by described admission line, the gas be inhaled into continues to be discharged after induction fan, mixed water wheels and point water wheels successively under the driving of described induction fan
Outside liquid flow to described induction fan by described water inlet, and the liquid entered is discharged successively after induction fan, mixed water wheels, point water wheels and the wheel that catchments.
As the preferred version of a kind of spiral fog-type dust collector of the present invention, the end of wherein said rotary main shaft is hollow structure, this hollow structure forms inlet channel, and described rotary main shaft offers at the opposite side of the relatively described mixed water wheels of induction fan the described water inlet be communicated with described inlet channel.
As the preferred version of a kind of spiral fog-type dust collector of the present invention, wherein said rotary main shaft is vertically placed, described induction fan, mixed water wheels, point water wheels are arranged on described rotary main shaft successively from top to bottom, described admission line is positioned at above described induction fan, described spiral fog-type dust collector also includes drive motors, this drive motors is connected with described rotary main shaft, and drives described rotary main shaft to rotate.
As the preferred version of a kind of spiral fog-type dust collector of the present invention, wherein said induction fan, mixed water wheels, point water wheels, the wheel that catchments all are arranged in the process space that described housing is formed.
As the preferred version of a kind of spiral fog-type dust collector of the present invention, wherein said mixed water wheels include plural layer and mix wiper blade, every layer of mixed wiper blade is installed on described rotary main shaft along the bearing of trend of described rotary main shaft successively, described every layer of mixed wiper blade includes upper strata blade, reinforcement, lower leave and coordinate the first axle center installation portion installed with described rotary main shaft, described upper strata blade and lower leave all include and outwards to extend spirally and its bearing of trend even number of being oppositely arranged identical with described rotary main shaft direction of rotation mixes water baffle plate in the plane perpendicular to described rotary main shaft place from described first axle center installation portion, described reinforcement from the initiating terminal of each mixed water baffle plate, connects the mixed water baffle plate that passes respectively until the end of mixed water baffle plate of its correspondence.
As the preferred version of a kind of spiral fog-type dust collector of the present invention, wherein said mixed water baffle plate is spiral vertical baffle, described upper strata blade and described lower leave all include two pieces of mixed water baffle plates, and the mixed water baffle plate of described upper strata blade and the mixed water baffle plate of described lower leave offset from each other an angle of 90 degrees.
As the preferred version of a kind of spiral fog-type dust collector of the present invention, wherein said point of water wheels include plural layer splitter vane, described every layer of splitter vane include the second axle center installation portion of coordinating with described rotary main shaft and installing and a plurality of from described second axle center installation portion at the plane outward extending point of water baffle plate perpendicular to described rotary main shaft place.
As the preferred version of a kind of spiral fog-type dust collector of the present invention, wherein said point of water baffle plate is vertical baffle, described every layer of splitter vane includes four pieces of equally distributed point of water baffle plates, offsets from each other miter angle between point water baffle plate of described adjacent every layer of splitter vane.
As the preferred version of a kind of spiral fog-type dust collector of the present invention, the wherein said wheel that catchments is arranged on the inwall of the housing corresponding with described point of water wheels, the described wheel that catchments includes the baffle plate that catchments, base plate, frid and osculum, the tangential direction that the described baffle plate that catchments is described in a plurality of edge point of water wheels direction of rotation and described inner walls are the vertical baffle of acute angle, the described baffle plate that catchments is fixedly connected with described housing, described base plate is the annular slab extended to described process space level from inner walls, the frid stretched out straight up is provided with in the inside edge of described annular slab, the described baffle plate that catchments stretches into by described frid downwards, in the tank that base plate and inner walls are formed, described base plate is also provided with one or more osculum.
As the preferred version of a kind of spiral fog-type dust collector of the present invention, the wherein said wheel that catchments also includes draining leg, described draining leg top is provided with opening and is connected with described corresponding osculum, the side of described draining leg is provided with drain outlet, and described draining leg inside is provided with the drain outlet that drainage pipeline connects open top and side.
Compared with prior art, the present invention has at least following beneficial effect:
One, structure is simple, and cost is low, is easy to large-scale industrial production.
Two, water reusable edible, water is drawn into rotary main shaft from cistern and is discharged, then becomes the impurity such as water smoke absorption flue dust, then pools water droplet again through the wheel that catchments and flows into cistern.
Three, water consumption, little power consumption, recycling of water, decreases the consumption of water, only single work need be driven can to drive whole device simultaneously, save power consumption, reach the requirement of energy-conserving and environment-protective.
Four, without the need to cleaning, pigment are broken into vaporific absorption flue dust impurity by mixed water wheels, and being outwards splashed under centrifugal action after falling into point water wheels catchments takes turns and become water droplet and fall.
Five, steam is separated, and in point water wheels, water smoke major part all flies to and catchments in wheel, and all direct bottom loss from point water wheels of most of air goes out, and can not discharge from draining leg, thus air can not be made to emerge at the bottom of pond become bubble to take water smoke out of cistern.
Accompanying drawing explanation
In order to be illustrated more clearly in the technical scheme of the embodiment of the present invention, below the accompanying drawing used required in describing embodiment is briefly described, apparently, accompanying drawing in the following describes is only some embodiments of the present invention, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.Wherein,
Fig. 1 is the perspective view of spiral fog-type dust collector of the present invention.
Fig. 2 is the structural representation of the sectional view of spiral fog-type dust collector of the present invention.
Fig. 3 is the perspective view of the mixed water wheels in spiral fog-type dust collector of the present invention.
Fig. 4 is the structural representation of the top view of mixed water wheels in Fig. 3.
Fig. 5 is the perspective view of point water wheels in spiral fog-type dust collector of the present invention.
Fig. 6 is the structural representation of the top view of point water wheels in Fig. 5.
Fig. 7 is the perspective view of taking turns and not having housing of catchmenting in spiral fog-type dust collector of the present invention.
Detailed description of the invention
For enabling above-mentioned purpose of the present invention, feature and advantage become apparent more, and below in conjunction with detailed description of the invention, the present invention is further detailed explanation.
First, alleged herein " embodiment " or " embodiment " refers to special characteristic, structure or the characteristic that can be contained at least one implementation of the present invention.Different local in this manual " in one embodiment " occurred not all refers to same embodiment, neither be independent or optionally mutually exclusive with other embodiments embodiment.
Secondly; the present invention utilizes structural representation etc. to be described in detail; when describing the embodiment of the present invention in detail; for ease of explanation; represent that the schematic diagram of spiral fog-type dust collector structure can be disobeyed general ratio and be made partial enlargement; and described schematic diagram is example, it should not limit the scope of protection of the invention at this.In addition, the three dimensions of length, width and the degree of depth should be comprised in actual fabrication.
In Fig. 1 to Fig. 5, rotary main shaft 1; Water inlet 12; Inlet channel 13; Mixed water wheels 2; Mixed wiper blade 21; Upper strata blade 211; Lower leave 212; Reinforcement 213; Mixed water baffle plate 214; First axle center installation portion 215; Divide water wheels 3; Splitter vane 31; Second axle center installation portion 32; Divide water baffle plate 311; Catchment wheel 4; Catchment baffle plate 41; Base plate 42; Frid 43; Osculum 44; Draining leg 45; Drain outlet 451; Drive motors 5; Smoke-intake pipe road 6; Induction fan 7; Housing 8.
Consult Fig. 1 and Fig. 2, in this embodiment, spiral fog-type dust collector of the present invention includes rotary main shaft 1, mixed water wheels 2, point water wheels 3, the wheel 4 that catchments, drive motors 5, smoke-intake pipe road 6, induction fan 7 and housing 8.Wherein induction fan 7, mixed water wheels 2 and point water wheels 3 are located on rotary main shaft 1 successively along the bearing of trend of rotary main shaft 1.It is inner that rotary main shaft 1 is vertically placed on housing 8, and its top is extended housing 8 and is connected with drive motors 5.When drive motors 5 works, its driven rotary main shaft 1 rotates, and rotary main shaft 1 then drives induction fan 7, mixed water wheels 2 and point water wheels 3 to carry out synchronous axial system.Induction fan 7, mixed water wheels 2, point water wheels 3, the wheel 4 that catchments all are positioned at the process space that housing 8 is formed.Smoke-intake pipe road 6 is communicated with the process space formed to housing 8, rotary main shaft 1 below smoke-intake pipe road 6 is provided with induction fan 7, this induction fan 7 contains the gas of impurity for the exit inspiration flue dust from smoke-intake pipe road 6 etc., also being provided with one deck gauze screen in the exit in smoke-intake pipe road 6, entering dust removal machine for preventing excessive solid particulate matter.
With reference to Fig. 2 and Fig. 3, in this embodiment, water inlet 12 is arranged on the rotary main shaft 1 below induction fan 7 above mixed water wheels 2, the inlet channel 13 of hollow is provided with from the end of this water inlet 12 to rotary main shaft 1, inlet channel 13 end is connected to water pump, in order to be sucked by the water of outside in dust removal machine and to spill from water inlet 12.In another embodiment, water inlet 12 is arranged on the rotary main shaft 1 above induction fan 7, can clean from this watering to induction fan.
Mixed water wheels 2 are arranged on the below of water inlet 12 on rotary main shaft 1, and in this embodiment, mixed water wheels 2 include 4 layers of mixed wiper blade 21, and every layer of mixed wiper blade 21 is installed on described rotary main shaft 1 successively along the bearing of trend of described rotary main shaft 1.With reference to Fig. 3 and Fig. 4, every layer of mixed wiper blade 21 includes upper strata blade 211, lower leave 212, reinforcement 213 and coordinate the first axle center installation portion 215 installed with rotary main shaft 1, blade 211 and lower leave 212 all include and outwards extend spirally and its bearing of trend be oppositely arranged 2 mixed water baffle plates 214 identical with rotary main shaft 1 direction of rotation in the plane perpendicular to rotary main shaft 1 place from described first axle center installation portion 215 at the middle and upper levels for they, mixed water baffle plate 214 is vertical baffle, 2 mixed water baffle plates 214 of upper strata blade 211 and 2 mixed water baffle plates 214 of lower leave 212 offset from each other an angle of 90 degrees, on, skew 90 degree between lower two-layer adjacent blades, make the effect all between whole adjacent every layer of mixed water wheels with cutting: water droplet is dispersed as water smoke and mixes with impurity in gas, there will not be the mixed water baffle plate only having one deck very long, cause the situation that mixed water baffle plate drive air moves together with water smoke.Reinforcement 213 is fixedly connected with upper strata blade 211 and lower leave 212 along the initiating terminal of each mixed water baffle plate 214 to the direction of terminal respectively, prevents mixing water baffle plate 214 during High Rotation Speed and deforms because resistance is excessive.When mixed water baffle plate 214 is with rotary main shaft 1 synchronous axial system, the water dripped from top water inlet 12 is dispersed as water smoke by the mixed water baffle plate of High Rotation Speed, and the flue dust impurity of this water smoke to inspiration from smoke-intake pipe road 6 carries out absorption and sorption.The water smoke absorbing impurity outwards disperses under centrifugal action, but spiral mixed water baffle plate, and the impurity water smoke that its outermost layer constantly dispersing blocks, and continues impurity water smoke inwardly to rotate to be sent to spiral center place.Because spirality mixes the stop of water baffle plate, make impurity water smoke to touch housing, avoid tough material in impurity water smoke and stick on housing.And the mixed water baffle plate of High Rotation Speed and the collision of water droplet be also equivalent to constantly to mixed water baffle plate carry out the degree of depth cleaning, scrub, thus can not make impurity absorption on mixed water baffle plate, ensure that the clean of mixed water baffle plate, clean without the need to artificial unloading.
In another embodiment, below the mixed water baffle plate of the every one deck of mixed wiper blade in mixed water wheels, all correspondence arranges one deck reinforcement, need not as above in an embodiment two-layer mixed water baffle plate share one deck reinforcement, this does not need too complex when being the mould in order to manufacture mixed water wheels, the example of two-layer mixed water baffle plate one deck reinforcement is relatively applicable to the mixed water wheels that metal does, and middle employing is welded.And one deck mixes the corresponding one deck reinforcement of water baffle plate and is applicable to mould of plastics, than being easier to processing.
With reference to Fig. 2, Fig. 5 and Fig. 6, water wheels 3 are divided to be arranged on the below of mixed water wheels 2 on rotary main shaft 1, in this embodiment, water wheels 3 are divided to include 6 layers of splitter vane 31, every layer of splitter vane 31 includes the second axle center installation portion 32 and 4 that to coordinate with rotary main shaft 1 and install from described second axle center installation portion 32 at the outward extending point water baffle plate 311 vertically of plane perpendicular to rotary main shaft 1 place, 4 points of water baffle plates 311 are evenly arranged on the same cross section of rotary main shaft 1, interval an angle of 90 degrees between adjacent point of water baffle plate 311.Miter angle is offset mutually between point water baffle plate 311 of adjacent every layer of splitter vane 31.Vertical point water baffle plate 311 is responsible for the impurity water smoke fallen from mixed water wheels 2 to produce huge centrifugal force, and be thrown to and catchmented in wheel.Offsetting from each other angle between adjacent every layer is also effect in order to produce cutting between each layer there.
In another embodiment, water wheels 3 are divided to comprise the identical splitter vane that haves three layers, every layer of splitter vane includes upper strata splitter vane and lower floor's splitter vane, upper and lower layer splitter vane all includes point water baffle plate of 4 spaced an angle of 90 degrees, and offsets from each other miter angle between splitter vane adjacent between levels.In this embodiment, upper and lower two are laminated together formation one deck splitter vane, and a point water baffle plate for this layer of splitter vane is all connected with rotary main shaft by the second axle center installation portion, and the diameter between mixed water wheels 2 and point water wheels 3 is identical.
In one embodiment, the upper and lower layer blade in water wheels 3 is divided all to include point water baffle plate of 8 spaced miter angles.
In one embodiment, with reference to Fig. 1, Fig. 2 and Fig. 7, the wheel 4 that catchments is arranged on housing 8 inwall corresponding with point water wheels 3, and it includes the baffle plate 41 that catchments, base plate 42, frid 43, osculum 44 and draining leg 45.The baffle plate 41 that wherein catchments is that much the individual tangential directions along described point of water wheels 3 direction of rotation and inner walls are the vertical baffle of acute angle, and baffle plate 41 top of catchmenting is fixedly connected with housing 8.Base plate 42 is the annular slab extended to described process space level from the inwall of housing 8, the frid 43 stretched out straight up is provided with in the inside edge of described annular slab, described frid 43, base plate 42 and housing 8 inwall are formed can the tank of storage of liquids, and the baffle plate 41 that catchments stretches into downwards in this tank.Described base plate 42 is also provided with 3 osculums 44.Draining leg 45 is arranged on the below of described base plate 42, and be provided with corresponding draining leg 45 below each osculum 44, described draining leg 45 top is provided with opening and is connected with described osculum 44.Bottom, draining leg 45 side is provided with drain outlet 451, and described drain outlet 451 is communicated with the opening of top setting and the drain outlet 451 of bottom, side.The impurity water smoke falling into point water wheels is driven by point water wheels point water baffle plate and outwards throws away to the wheel that catchments at a high speed, and water smoke is all descended by the baffle plate gear that catchments and continues to impinge upon inner walls place formation water droplet and falls into tank below.Water in tank enters draining leg by osculum, and discharges from the drain outlet draining leg.Draining leg can put into cistern, drain outlet is arranged on below liquid level, can dissolve in water by the water smoke in a small amount of bubble contained of discharging from the wheel that catchments herein, recycle-water resource greatly.
Spiral fog-type dust collector of the present invention have remove harmful components in gas, water consumption is few, power consumption is little, dedusting scope is wide, efficiency of dust collection is high, the dedusting cycle fast, circulating water, without the need to advantages such as cleaning, energy-conserving and environment-protective.
It should be noted that, above embodiment is only in order to illustrate technical scheme of the present invention and unrestricted, although with reference to preferred embodiment to invention has been detailed description, those of ordinary skill in the art is to be understood that, can modify to technical scheme of the present invention or equivalent replacement, and not departing from the spirit and scope of technical solution of the present invention, it all should be encompassed in the middle of right of the present invention.
Claims (9)
1. a spiral fog-type dust collector, includes:
Housing, formation processing space in it;
Be arranged at the admission line on described housing, extraneous gas is introduced in described process space by it; With
Outside liquid can be introduced the water inlet in described process space, it is characterized in that: described spiral fog-type dust collector also includes
Extend into the rotary main shaft in described process space; With
Bearing of trend along rotary main shaft is located at the induction fan on rotary main shaft, mixed water wheels and point water wheels successively, and described rotary main shaft drives described induction fan, mixed water wheels and point water wheels synchronous axial system,
When described rotary main shaft rotates, under the driving of described induction fan, extraneous gas is inhaled in described process space by described admission line, the gas be inhaled into continues to be discharged after induction fan, mixed water wheels and point water wheels successively under the driving of described induction fan
Outside liquid flow to described induction fan by described water inlet, and the liquid entered is discharged successively after induction fan, mixed water wheels, point water wheels and the wheel that catchments,
Described mixed water wheels include plural layer and mix wiper blade,
Every layer of mixed wiper blade is installed on described rotary main shaft along the bearing of trend of described rotary main shaft successively,
Described every layer of mixed wiper blade includes upper strata blade, reinforcement, lower leave and coordinates the first axle center installation portion installed with described rotary main shaft,
Described upper strata blade and lower leave all include and outwards to extend spirally and its bearing of trend even number of being oppositely arranged identical with described rotary main shaft direction of rotation mixes water baffle plate in the plane perpendicular to described rotary main shaft place from described first axle center installation portion,
Described reinforcement from the initiating terminal of each mixed water baffle plate, connects the mixed water baffle plate that passes respectively until the end of mixed water baffle plate of its correspondence.
2. spiral fog-type dust collector according to claim 1, it is characterized in that: the end of described rotary main shaft is hollow structure, this hollow structure forms inlet channel, and described rotary main shaft offers at the opposite side of the relatively described mixed water wheels of induction fan the described water inlet be communicated with described inlet channel.
3. spiral fog-type dust collector according to claim 1, it is characterized in that: described rotary main shaft is vertically placed, described induction fan, mixed water wheels, point water wheels are arranged on described rotary main shaft successively from top to bottom, and described admission line is positioned at above described induction fan
Described spiral fog-type dust collector also includes drive motors, and this drive motors is connected with described rotary main shaft, and drives described rotary main shaft to rotate.
4. spiral fog-type dust collector according to claim 1, is characterized in that: described induction fan, mixed water wheels, point water wheels, the wheel that catchments all are arranged in the process space that described housing is formed.
5. spiral fog-type dust collector according to claim 1, is characterized in that: described mixed water baffle plate is spiral vertical baffle,
Described upper strata blade and described lower leave all include two pieces of mixed water baffle plates,
The mixed water baffle plate of described upper strata blade and the mixed water baffle plate of described lower leave offset from each other an angle of 90 degrees.
6. spiral fog-type dust collector according to claim 1, is characterized in that: described point of water wheels include plural layer splitter vane,
Described every layer of splitter vane include the second axle center installation portion of coordinating with described rotary main shaft and installing and a plurality of from described second axle center installation portion at the plane outward extending point of water baffle plate perpendicular to described rotary main shaft place.
7. spiral fog-type dust collector according to claim 6, is characterized in that: described point of water baffle plate is vertical baffle,
Described every layer of splitter vane includes four pieces of equally distributed point of water baffle plates,
Miter angle is offset from each other between point water baffle plate of described adjacent every layer of splitter vane.
8. spiral fog-type dust collector according to claim 1, is characterized in that: described in the wheel that catchments be arranged on the inwall of the housing corresponding with described point of water wheels,
The described wheel that catchments includes the baffle plate that catchments, base plate, frid and osculum,
The tangential direction that the described baffle plate that catchments is described in a plurality of edge point of water wheels direction of rotation and described inner walls are the vertical baffle of acute angle,
The described baffle plate that catchments is fixedly connected with described housing,
Described base plate is the annular slab extended to described process space level from inner walls,
The frid stretched out straight up is provided with in the inside edge of described annular slab,
The described baffle plate that catchments stretches in the tank that is made up of described frid, base plate and inner walls downwards,
Described base plate is also provided with one or more osculum.
9. spiral fog-type dust collector according to claim 8, is characterized in that: described in catchment wheel also include draining leg,
Described draining leg top is provided with opening and is connected with described corresponding osculum,
The side of described draining leg is provided with drain outlet,
Described draining leg inside is provided with the drain outlet that drainage pipeline connects open top and side.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310538036.0A CN103566685B (en) | 2013-11-01 | 2013-11-01 | A kind of spiral fog-type dust collector |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310538036.0A CN103566685B (en) | 2013-11-01 | 2013-11-01 | A kind of spiral fog-type dust collector |
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| Publication Number | Publication Date |
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| CN103566685A CN103566685A (en) | 2014-02-12 |
| CN103566685B true CN103566685B (en) | 2015-08-19 |
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| CN201310538036.0A Expired - Fee Related CN103566685B (en) | 2013-11-01 | 2013-11-01 | A kind of spiral fog-type dust collector |
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Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106563328A (en) * | 2016-10-20 | 2017-04-19 | 霍进铭 | Rotary spray type dust remover |
| CN110687265A (en) * | 2019-09-23 | 2020-01-14 | 河南教育学院 | Detection device for ecological environment improvement |
| CN112044211B (en) * | 2020-08-07 | 2023-09-12 | 太原理工大学 | Multifunctional integrated dust removal device and method |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB397862A (en) * | 1932-01-22 | 1933-08-22 | Robert Rogers Harmon | Improvements in processes and apparatus for washing gas |
| CH638998A5 (en) * | 1978-10-03 | 1983-10-31 | Alexandr Vladimir Shafranovsky | Rotary mass transfer and heat exchange appliance |
| CN2145636Y (en) * | 1993-03-19 | 1993-11-10 | 滕伯阳 | Rotary spraying duster |
| CN1093943A (en) * | 1993-11-11 | 1994-10-26 | 秦彪 | A kind of air washing purifier |
| CN2227518Y (en) * | 1995-05-05 | 1996-05-22 | 王继杰 | Water-filtering air cleaner |
| CN203609997U (en) * | 2013-11-01 | 2014-05-28 | 薛绍富 | Rotating mist type dusting machine |
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2013
- 2013-11-01 CN CN201310538036.0A patent/CN103566685B/en not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB397862A (en) * | 1932-01-22 | 1933-08-22 | Robert Rogers Harmon | Improvements in processes and apparatus for washing gas |
| CH638998A5 (en) * | 1978-10-03 | 1983-10-31 | Alexandr Vladimir Shafranovsky | Rotary mass transfer and heat exchange appliance |
| CN2145636Y (en) * | 1993-03-19 | 1993-11-10 | 滕伯阳 | Rotary spraying duster |
| CN1093943A (en) * | 1993-11-11 | 1994-10-26 | 秦彪 | A kind of air washing purifier |
| CN2227518Y (en) * | 1995-05-05 | 1996-05-22 | 王继杰 | Water-filtering air cleaner |
| CN203609997U (en) * | 2013-11-01 | 2014-05-28 | 薛绍富 | Rotating mist type dusting machine |
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Inventor after: Xue Shaofu Inventor before: Xue Shaofu |
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Address after: The new road 224700 in Jiangsu Province, Yancheng City Jianhu County No. 233 Patentee after: Xue Shaofu Address before: The new road 224700 in Jiangsu Province, Yancheng City Jianhu County No. 233 Patentee before: Xue Shaofu |
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Granted publication date: 20150819 Termination date: 20161101 |