CN108360094A - A kind of cyclone separator of the anti-paste net and normal pressure blanking blowout prevention ash of automatically cleaning filter cylinder - Google Patents
A kind of cyclone separator of the anti-paste net and normal pressure blanking blowout prevention ash of automatically cleaning filter cylinder Download PDFInfo
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- CN108360094A CN108360094A CN201810205053.5A CN201810205053A CN108360094A CN 108360094 A CN108360094 A CN 108360094A CN 201810205053 A CN201810205053 A CN 201810205053A CN 108360094 A CN108360094 A CN 108360094A
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- shell
- dust cage
- normal pressure
- spiral case
- cyclone separator
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- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01G—PRELIMINARY TREATMENT OF FIBRES, e.g. FOR SPINNING
- D01G9/00—Opening or cleaning fibres, e.g. scutching cotton
- D01G9/08—Opening or cleaning fibres, e.g. scutching cotton by means of air draught arrangements
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01G—PRELIMINARY TREATMENT OF FIBRES, e.g. FOR SPINNING
- D01G9/00—Opening or cleaning fibres, e.g. scutching cotton
- D01G9/14—Details of machines or apparatus
- D01G9/20—Framework; Casings; Coverings; Grids
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
- Y02A50/2351—Atmospheric particulate matter [PM], e.g. carbon smoke microparticles, smog, aerosol particles, dust
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- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Cyclones (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
The present invention relates to a kind of cyclone separator of the anti-paste net and normal pressure blanking blowout prevention ash of automatically cleaning filter cylinder, the top of shell connects spiral case, and lower part connection collects cotton bucket, shell, and spiral case sum aggregate cotton bucket is connected, and air inlet is arranged on spiral case, air outlet is arranged on shell；Guide shell is arranged inside shell and spiral case, and dust cage is arranged in shell, and dust cage top is circular cylinder, lower part connects cone cylinder, and dust cage is equipped with filter mesh, and positioned at the outside of guide shell, the bottom of cone cylinder is cotton output port, and air port is recycled in setting between cone cylinder radial direction and shell.Ventilation resistance of the present invention is small, avoids paste net, material-gas ratio height, normal pressure blanking, reduces secondary pollution, avoid spray ash, automated cleaning, simplify structure, reduce failure.
Description
Technical field
The present invention relates to textile industry fiber automatic collecting device technical field, especially a kind of ventilation resistance is small, avoids
Paste net, material-gas ratio height, normal pressure blanking, reduce secondary pollution, avoid spray ash, automated cleaning, simplify structure, reduction failure certainly
Clean the cyclone separator of the anti-paste net and normal pressure blanking blowout prevention ash of filter cylinder.
Background technology
Cyclone separator presses the difference of its diameter, can be divided into desander, desilter and microclone three classes.1, desanding
Device：The cyclone separator of a diameter of 150~300mm is known as desander, it handles the ability of drilling fluid, is in input pressure
Generally it is not less than 20~120mm when 0.2Mpa3/h.Desander in normal condition can remove about 95% and be more than 74 microns
Drilling cuttings and 50% drilling cuttings more than 44 microns.When selecting desander, maximum pump discharge when permit process amount should be drilling well
1.25 again.2, desilter：The cyclone separator of a diameter of 100~150mm is known as desilter.When input pressure is 0.25Mpa,
Its processing capacity is not less than 10~15m3/h.The desander of normal operating conditions can remove 95% more than 44 microns drilling cuttings and
50% is more than 15 microns of drilling cuttings.The permit process amount of desilter, 1.25~1.5 times of maximum pump discharge when should be drilling well.3, micro-
Type cyclone：The cyclone separator of a diameter of 50mm is known as microclone.Its processing capacity is when input pressure is 0.25Mpa
Not less than 5m3/h.Ranging from 7~25 microns of separating particles.It is mainly used for non-weighted drilling fluid, to remove ultra-fine grain.
Existing automatic fibers collecting device form mainly by：Fiber separation presser, condenser, without shapes such as stripping condensers
Formula, 1) fiber compaction device：Realize that fine qi leel excludes fiber hold down from, helical blade using net cylinder, there are spraying decorations for operation under positive pressure
Phenomenon, negative pressure operation negative pressure is too high, and there are noil difficulty, especially screw shaft rotations to cause thread rolling, knot, and damages fiber；2) have
The condenser of stripping mechanism：Stripping hired roughneck's mode, fiber is added often to block between dust cage and wallboard using traditional rotation dust cage
Gap hinders dust cage to operate and causes traffic jam, and 3) without stripping condenser：It is generally adopted in centralized collection system to save energy consumption
With multiple spot interval dust suction in turn, often there is masses of fibres paste net or the grey problem of discharge port spray causes environmental pollution.Using this patent
Before technology, the matching of equipment air inlet/outlet being adjusted and requires height, air quantity narrow range is handled to fibre damage, net cylinder paste net phenomenon is frequent,
High failure rate is realized the not damaged automatic collection conveying of fiber, is substantially increased the degree of automation after the art of this patent
With reduce collect during secondary pollution environmental problem.Without stripping mechanism, automated cleaning net cylinder eliminates fiber patch net hidden danger,
Equipment operation failure is greatly reduced, discharge air quantity realizes cycle in equipment, realizes normal pressure noil, reduce environmental pollution, hinders
Power low energy consumption is small.
Need a kind of ventilation resistance is small, avoid paste net, material-gas ratio height, normal pressure blanking, reduction secondary pollution, avoid spraying
Ash, the anti-cyclone separator for pasting net and normal pressure blanking blowout prevention ash of automatically cleaning filter cylinder for automated cleaning, simplifying structure, reducing failure.
Invention content
That the object of the present invention is to provide a kind of ventilation resistances is small, avoids paste net, material-gas ratio height, normal pressure blanking, reduction two
Secondary pollution avoids spray ash, automated cleaning, simplifies structure, the anti-paste net of automatically cleaning filter cylinder for reducing failure and normal pressure blanking blowout prevention ash
Cyclone separator.
A kind of cyclone separator of the anti-paste net and normal pressure blanking blowout prevention ash of automatically cleaning filter cylinder, including：
The top of shell, the shell connects spiral case, and lower part connection collects cotton bucket, the shell, and spiral case sum aggregate cotton bucket is connected,
Air inlet is set on the spiral case, air outlet is set on the shell；
Guide shell, the guide shell are arranged inside shell and spiral case, and dust cage, the dust cage top are arranged in the shell
For circular cylinder, lower part connects cone cylinder, and the dust cage is equipped with filter mesh, and positioned at the outside of guide shell, the bottom of the cone cylinder
Portion is cotton output port, and air port is recycled in setting between the cone cylinder radial direction and shell.
At the air outlet, be not provided in recycle air port.
The filter mesh being arranged on the dust cage successively decreases distribution in the height direction, the filter screen being arranged by the top of dust cage
Hole number is more, and the filter mesh quantity being arranged by the lower section of dust cage is few.
The shell, spiral case sum aggregate cotton bucket are respectively annular, and the diameter of the shell is more than the diameter of spiral case, the spiral case
Top seal.
The dust cage is not provided with filter mesh close to air outlet side or the filter mesh is blocked by curved baffle
Closing.
The cone cylinder is funnel-form, and the cotton output port of bottom is connected with the inside of collection cotton bucket.
It includes fixed ring and loose collar to recycle air port in described, and the fixed ring and loose collar are respectively ring segment, institute
State and the first exhaust vent be set in fixed ring, the second exhaust vent is set on the loose collar, the loose collar fixed ring top from
When turning, second exhaust vent adjusts the openings of sizes of the first exhaust vent.
Uniformly it is covered with filter mesh on the dust cage, the outside of the dust cage is equipped with curved baffle, the arc on the lower
Baffle is the arc-like sheet for being bonded dust cage outer wall.
The dust cage is equipped with the curved baffle by air outlet side.
The upper width size of the curved baffle is small, and lower width size is big.
The top of inventive shell connects spiral case, and lower part connection collection cotton bucket, shell, spiral case sum aggregate cotton bucket is connected, on spiral case
Air inlet is set, air outlet is set on shell；Guide shell is arranged inside shell and spiral case, setting dust cage in shell, on dust cage
Portion is circular cylinder, and lower part connects cone cylinder, and dust cage is equipped with filter mesh, and positioned at the outside of guide shell, the bottom of cone cylinder is
Cotton mouthful recycles air port between cone cylinder radial direction and shell in setting.The entrance of spiral case is connected with external air intake passage air inlet,
Volute outlet is directed downward and is connect with dust cage inside；Air port is set out on the outside of lower part of the housing, then connects sucktion fan, shell and dust cage
Cavity is negative pressuren zone between outer wall, is blown from distant place to air inlet by external cotton transport blower fan, fine dust air is formed after spiral case
Helical swirl falls, into dust cage in complete fine, dirt separation, trifle in the world is under by negative pressure double action outside centrifugal force and dust cage, dirt
Gas is aspirated through air outlet through dust cage and is excluded, and is filtered into dust filtering unit essence, and fiber enters collection cotton bucket through dust cage, and guide shell is eliminated
Vortex in dust cage prevents fiber from knotting, rope silk.By adjusting the effective minimum discharge air quantity of outlet air section control of air outlet；Dust cage
Lower part is equipped with the interior of air circulation in adjusting and recycles air port, the discharge air quantity being discharged into time in collection cotton bucket, and passes through tune
Air port is recycled in section and effectively controls air-out area, ensures that collection cotton bucket lower part is always normal pressure；Annular space is equipped with outside dust cage
The curved baffle of arrangement balances the dust discharge effect of dust cage surrounding, prevents from, because unilateral air draught is excessive, causing cotton layer suction wall traffic congestion existing
As.Ventilation resistance of the present invention is small, avoid paste net, material-gas ratio height, normal pressure blanking, reduce secondary pollution, avoid spraying it is grey, automatic clearly
Clean, simplified structure reduces failure.
Description of the drawings
Fig. 1 is the stereogram of the present invention；
Fig. 2 is the sectional view of the present invention；
Fig. 3 is the sectional view of A-A of the present invention；
Fig. 4 is the sectional view of B-B of the present invention；
Fig. 5 is the sectional view of C-C of the present invention；
Fig. 6 is the stereogram of dust cage of the present invention and curved baffle；
In figure：1, shell, 2, spiral case, 3, collection cotton bucket, 4, air inlet, 5, air outlet, 6, guide shell, 7, dust cage, 8, filtering
Mesh, 9, it is interior recycle air port, 10, cone cylinder, 11, mounting hole, 12, curved baffle, 13, access panel, 14, access hole, 91, fixed
Ring, 92, loose collar, the 93, first exhaust vent, the 94, second exhaust vent.
Specific implementation mode
Below in conjunction with the drawings and specific embodiments, the present invention will be further described.
A kind of cyclone separator of the anti-paste net and normal pressure blanking blowout prevention ash of automatically cleaning filter cylinder, including：Shell 1, shell 1 it is upper
Portion connects spiral case 2, and lower part connection collection cotton bucket 3, shell 1,2 sum aggregate cotton bucket 3 of spiral case is connected, and air inlet 4, shell 1 are arranged on spiral case 2
Upper setting air outlet 5；Guide shell 6, guide shell 6 are arranged inside shell 1 and spiral case 2, setting dust cage 7 in shell 1, on dust cage 7
Portion is circular cylinder, and lower part connects cone cylinder 10, and dust cage 7 is equipped with filter mesh 8, and positioned at the outside of guide shell 6, the bottom of cone cylinder 10
Portion is cotton output port, and air port 9 is recycled in setting between 10 radial direction of cone cylinder and shell 1.
Preferably, at air outlet 5, be not provided in recycle air port 9.
The filter mesh 8 being arranged on dust cage 7 successively decreases distribution in the height direction, the filter screen being arranged by the top of dust cage 7
8 quantity of hole is more, and 8 quantity of filter mesh being arranged by the lower section of dust cage 7 is few.Shell 1,2 sum aggregate cotton bucket 3 of spiral case are respectively annular,
The diameter of shell 1 is more than the diameter of spiral case 2, the top seal of spiral case 2.Dust cage 7 is not provided with filter mesh close to 5 side of air outlet
8 or filter mesh 8 carried out blocking closing by curved baffle.Cone cylinder 10 is funnel-form, the cotton output port of bottom with collect the interior of cotton bucket 3
Portion is connected.It includes fixed ring 91 and loose collar 92 inside to recycle air port 9, and fixed ring 91 and loose collar 92 are respectively ring segment, Gu
Determine that the first exhaust vent 93 is arranged on ring 91, the second exhaust vent 94 be set on loose collar 92, loose collar 92 91 top of fixed ring from
When turning, the second exhaust vent 94 adjusts the openings of sizes of the first exhaust vent 93.Uniformly it is covered with filter mesh 8 on dust cage 7, dust cage 7
Outside is equipped with curved baffle 12 on the lower, and curved baffle 12 is the arc-like sheet for being bonded 7 outer wall of dust cage.The top of curved baffle 12 is wide
Degree size is small, and lower width size is big.
Mounting hole 11 is set on dust cage 7, and fasteners through mounting holes 11 fix curved baffle 12；As another form,
Curved baffle 12 can be from the outside installed to by anchor ear etc. on the designated position of dust cage 7.Access panel is set on shell 1 and spiral case 2
13.1 outside of shell recycles setting access hole 14 at air port 9 close to interior, and access hole 14 is switch gate.
The entrance of spiral case 2 is connected with external air intake passage air inlet 4,2 export direction of spiral case downward and with inside dust cage 7
Connection；1 lower outside of shell sets out air port 5, then connects sucktion fan, and cavity is negative pressuren zone between 7 outer wall of shell 1 and dust cage, is passed through
External cotton transport blower fan is blown from distant place to air inlet 4, and air-flow containing fine dust tangentially enters in dust cage 7 by spiral case 2, larger
Fiber dust lower end discharge port returned back to by air-flow enter collection cotton bucket 3 and be discharged, trifle in the world is by the 7 dual work of outer negative pressure of centrifugal force and dust cage
Under, dust and gas is aspirated through air outlet 5 through dust cage 7 and is excluded, and is filtered into dust filtering unit essence, and fiber enters collection cotton bucket through dust cage 7
3, guide shell 6 eliminates vortex in dust cage 7, prevents fiber from knotting, rope silk.By adjusting the minimum discharge wind of 5 bore of air outlet control
Amount；7 lower part of dust cage is equipped with the interior of air circulation in adjusting and recycles air port 9, the discharge wind being discharged into time in collection cotton bucket 3
Amount ensures that 3 lower part of collection cotton bucket is always normal pressure；7 outside of dust cage is equipped with the curved baffle 12 of annular space arrangement, balances dust cage 7
The dust discharge effect of surrounding.
Further, in order to prevent because unilateral air draught is excessive, lead to cotton layer suction wall traffic jam, close to air outlet 5
Curved baffle 12 is arranged in side, and larger close to 12 area of the curved baffle that air outlet 5 goes out.
It is cylindrical tube in the shell 1 of condenser, is trepanning sealing plate up and down, lower part sets out air port, and dust cage 7 is lifted on shell
On 1 upper plate of body, 7 outside of dust cage forms the closed cavity of gap uniformity with 1 inside of shell, and it is in gradually to open that 1 top of shell, which is provided with,
The spiral case 2 of line mode, the entrance of spiral case 2 are connected with external air intake passage air inlet 4, export direction downward and in dust cage 7
Chamber connects, and 7 top of dust cage is in cylindrical drum, and lower part is in frustum cone cylinder, and uniformly distributed mesh is provided on the cylinder of top；2 inside center of spiral case is pacified
It is stretched into dust cage 7 equipped with guide shell 6,7 outer middle and lower part of dust cage is equipped with the curved baffle 12 of annular space arrangement, adjusts dust cage 7 four
All air draught uniformities；For shell 1 on collection cotton bucket 3,7 times mouths of dust cage pick out air port 5, are circular layout on 1 time sealing plate of shell more
A return air inlet, sealing plate lower part are equipped with air-flow plate, and rotation adjustable plate control return air inlet opens size, is in realization collection cotton bucket 3
Normal pressure.After live pipe network system determines, automated cleaning starts operation automatically.
Air-flow with fiber enters through air inlet 4 in spiral case 2 and shell 1, by forming rotation in spiral case 2 and dust cage 7
Gas is revolved, and air is discharged through 7 mesh of dust cage, and fiber will not condense in 7 inner surface of dust cage under the drive of eddy flow cyclone, and by
Gradually backspin is entered in collection cotton bucket 3 through cotton output port, is settled；To realize the lossless collection of fiber.The setting in spiral case 2
There is guide shell 6, extends to 1 middle part of shell；Dust cage 7 is provided in shell 1；The lower end of dust cage 7 is connected with cone cylinder 10
Cotton output port, cotton output port are conical opening, are extended in collection cotton bucket 3.
Air inlet 4 is arranged vertically on spiral case 2, and certain vortex shape is collectively formed with spiral case 2 in air inlet 4, to make to contain
Fine air-flow can be rotated along being arranged in intermediate guide shell 6, after air inlet enters equipment to form swirling eddy.
Contain fine dust in swirling eddy, be affected by gravity, flow gradually downward, i.e., is diverted into dust cage 7 from 2 inward turning of spiral case.7 table of dust cage
Face is provided with filter mesh 8, for discharging air out of dust cage 7, and then is left by air outlet 5.
When filter mesh 8 of the air through 7 surface of dust cage leaves from the inside of dust cage 7, enter between dust cage 7 and shell 1
When space, rotation air velocity constantly reduces in dust cage 7, and air-flow continuously decreases dust cage inner wall souring, and fiber can be inhaled
Attached force effect attaches to 7 surface of dust cage；If swirling eddy is supplied to the rotation of fiber hypodynamic, i.e., it can lead to fiber
It is trapped in 7 surface of dust cage, or even is hung and is stayed, blocks filter mesh, and then can not ensure that fiber is smoothly settled down in collection cotton bucket.And
With the rotational flow gradually downward of air-flow, air is constantly flowed away by the filter mesh 8 on 7 surface of dust cage, and wind will certainly be caused
Speed reduces, and then influences the sedimentation of fiber；Especially along the vertical direction of dust cage 7, closer to 7 bottom of dust cage, swirling eddy wind
Speed is lower.To keep the wind speed of 7 internal gas flow of dust cage sufficiently high, to can be smoothly transferred to kinetodesma in collection cotton bucket 3.Dirt
The main body of cage 7 is the net cylinder with filter mesh 8；It is equipped with cone cylinder 10 below dust cage 7, is mutually connected with the cone mouth of cotton output port, bores
It is not provided with filter mesh on cylinder 10；The mounting hole 11 of fixed curved baffle 12 is provided on dust cage 7, the mounting hole 11 is for solid
Dingan County fills curved baffle 12；Curved baffle 12 is mounted on the outer surface of dust cage 7, by selecting suitable curved baffle 12, to adjust
7 lower half portion of whole dust cage for outlet air 8 quantity of filter mesh and area accounting, to ensure the wind of swirling eddy on the downside of dust cage
Speed.Making dust cage, position filter mesh part air permeance resistance is uniform and stable up and down, to ensure downside swirling eddy at a lower wind speed
Work fiber does not paste net；Preferably, air-flow flows through mesh wind speed general control in 5m/s.Curved baffle 12 have with outside dust cage 7
The radian that surface fits prevents dust cage 7 from being kept off with arc to be blocked as far as possible to the filter mesh 8 on 7 surface of dust cage
Unnecessary leakage is generated between plate 12, and fiber is caused to be adhered to 7 inside of dust cage.
Preferably, the upper width size of curved baffle 12 is small, and lower width size is big, in the present embodiment, curved baffle
12 be taper, and in 7 upper position of dust cage, stub end is arranged in 7 upper position of dust cage for small head end setting；Curved baffle 12 it is specific
Shape arranges quantity, can be according to the wind speed for the different air-flows for entering equipment, the rotary speed of fiber, the characteristic of different fibers
It is designed accordingly, with setting.
It preferably, can also be by directly adjusting dust cage if you do not need to if adjusting the size of curved baffle 12, quantity
The arrangement of filter mesh 8 on 7 realizes that the setting quantity of the top filter mesh 8 of dust cage 7 is more, the mistake of the lower section of dust cage 7
The setting quantity of opening of sieve 8 is smaller, is realized on the vertical direction of dust cage 7 with this, effective mesh quantity stepped change, realizes
Effect same as setting curved baffle 12.
Again it is preferred to, close to the side of air outlet 5, it is not provided with filter mesh 8, to prevent the mistake of 5 side of air outlet
Net wind speed is excessive, influences fiber whereabouts and is collected.
7 lower part of dust cage is provided with closed cone cylinder 10, when air-flow containing fine dust is after guide shell 6 is slowed down, into cone
It in cylinder 10, under the drive of air-flow, is converged, and settle whereabouts, by cotton output port, into collection cotton bucket 3.
In collection cotton bucket 3 and cotton output port outlet, can certainly will also there be certain air-flow, enter in collection cotton bucket 3；The part gas
The fiber collected in cotton bucket 3 will certainly be blown afloat if wind speed is excessive, cause spraying decoration phenomenon by stream, polluted environment and be unfavorable for fiber
Collection；To reduce the wind speed of the fraction, at the top of collection cotton bucket 3, on the annulus being connected with shell 1, it is equipped with interior cycle
Air outlet 9.
Preferably, it inside recycles and is additionally provided with interior air circulation regulating device at air port 9, by recycling air port in adjusting
The practical area for outlet air makes in collection cotton bucket 3, the collection on cotton output port horizontal plane to adjust the interior cycle wind speed in collection cotton bucket 3
3 inner wall wind pressure static pressure of cotton bucket is controlled in ± 20Pa；It is further preferred that the static pressure is controlled in ± 5Pa, so that fiber settles
Accumulation, facilitates collection.
Preferably, air port 9 is recycled at air outlet 5, being not provided with, to prevent the interior office for recycling the generation of air port 9
Portion's negative pressure is excessively concentrated, and then influences the interior fiber sedimentation recycled in 9 inside collection cotton bucket 3 of air port near air outlet 5, is caused
Fiber near air outlet 5 in recycle air port 9 and be sucked out, pass through 5 device for transferring of air outlet.
Advantage：
(1) dust cage 7 arranges that ventilation resistance is small, avoids paste net according to air-flow rotation direction, 8 trepanning of filter mesh using ladder
Hidden danger；
(2) the cotton output port optimization design of cone cylinder 10, realizes discharge air quantity minimum, and material-gas ratio reaches 0.5；
(3) circulating regulation mechanism in discharge air quantity equipment is used, normal pressure blanking reduces secondary pollution, thoroughly avoids
Spray ash may；
(4) it being controlled automatically using guide shell 6, adjustment disengaging air quantity realizes 7 automatic cleaning function of dust cage,
(5) no-rotary part cancels the transmission mechanism of traditional condenser complexity, the operation of machine zero failure is realized, in fibre-condensing
Dust cage 7 is static in the process, changes traditional rotation dust cage 7 plus the stripping mode of stripping hired roughneck, overcomes the shortcomings of existing product.
The basic principles, main features and advantages of the invention have been shown and described above.The technical staff of the industry should
Understand, the present invention is not limited to the above embodiments, and the above embodiments and description only describe the originals of the present invention
Reason, various changes and improvements may be made to the invention without departing from the spirit and scope of the present invention, these changes and improvements
It all fall within the protetion scope of the claimed invention.The claimed scope of the invention is by appended claims and its equivalent circle
It is fixed.
Claims (10)
1. a kind of cyclone separator of the anti-paste net and normal pressure blanking blowout prevention ash of automatically cleaning filter cylinder, which is characterized in that including：
Shell (1), the top connection spiral case (2) of the shell (1), lower part connection collection cotton bucket (3), the shell (1), spiral case
(2) sum aggregate cotton bucket (3) is connected, setting air inlet (4) on the spiral case (2), setting air outlet (5) on the shell (1)；
Guide shell (6), guide shell (6) setting is internal in shell (1) and spiral case (2), and dust cage is arranged in the shell (1)
(7), dust cage (7) top is circular cylinder, and lower part connects cone cylinder (10), and the dust cage (7) is equipped with filter mesh (8), and
The bottom of outside positioned at guide shell (6), the cone cylinder (10) is cotton output port, and the cone cylinder (10) is radial between shell (1)
Air port (9) is recycled in setting.
2. a kind of cyclone separator of the anti-paste net and normal pressure blanking blowout prevention ash of automatically cleaning filter cylinder according to claim 1,
Be characterized in that, at the air outlet (5), be not provided in recycle air port (9).
3. a kind of cyclone separator of the anti-paste net and normal pressure blanking blowout prevention ash of automatically cleaning filter cylinder according to claim 1,
It is characterized in that, the filter mesh (8) being arranged on the dust cage (7) successively decreases distribution in the height direction, is set above dust cage (7)
Filter mesh (8) quantity set is more, and filter mesh (8) quantity being arranged by the lower section of dust cage (7) is few.
4. a kind of cyclone separator of the anti-paste net and normal pressure blanking blowout prevention ash of automatically cleaning filter cylinder according to claim 1,
It is characterized in that, the shell (1), spiral case (2) sum aggregate cotton bucket (3) is respectively annular, and the diameter of the shell (1) is more than spiral case
(2) diameter, the top seal of the spiral case (2).
5. a kind of cyclone separator of the anti-paste net and normal pressure blanking blowout prevention ash of automatically cleaning filter cylinder according to claim 1,
It is characterized in that, the dust cage (7) is not provided with filter mesh (8) or the filter mesh (8) by arc close to air outlet (5) side
Shape baffle carries out blocking closing.
6. a kind of cyclone separator of the anti-paste net and normal pressure blanking blowout prevention ash of automatically cleaning filter cylinder according to claim 1,
It is characterized in that, the cone cylinder (10) is funnel-form, and the cotton output port of bottom is connected with the inside of collection cotton bucket (3).
7. a kind of cyclone separator of the anti-paste net and normal pressure blanking blowout prevention ash of automatically cleaning filter cylinder according to claim 1,
Be characterized in that, it is described in recycle air port (9) include fixed ring (91) and loose collar (92), the fixed ring (91) and loose collar
(92) it is respectively ring segment, the first exhaust vent (93) is set on the fixed ring (91), is arranged second on the loose collar (92)
Exhaust vent (94), in fixed ring (91) top rotation, second exhaust vent (94) adjusts first and goes out the loose collar (92)
The openings of sizes of air holes (93).
8. a kind of cyclone separator of the anti-paste net and normal pressure blanking blowout prevention ash of automatically cleaning filter cylinder according to claim 1,
It is characterized in that, filter mesh (8) is uniformly covered on the dust cage (7), and the outside of the dust cage (7) is equipped with curved baffle on the lower
(12), the curved baffle (12) is the arc-like sheet for being bonded dust cage (7) outer wall.
9. a kind of cyclone separator of the anti-paste net and normal pressure blanking blowout prevention ash of automatically cleaning filter cylinder according to claim 8,
It is characterized in that, the dust cage (7) is equipped with the curved baffle (12) by air outlet (5) side.
10. a kind of cyclonic separation of the anti-paste net and normal pressure blanking blowout prevention ash of automatically cleaning filter cylinder according to claim 8 or claim 9
Device, which is characterized in that the upper width size of the curved baffle (12) is small, and lower width size is big.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810205053.5A CN108360094B (en) | 2018-03-13 | 2018-03-13 | Cyclone separator capable of automatically cleaning filter cylinder to prevent pasting net and normal-pressure blanking to prevent dust spraying |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810205053.5A CN108360094B (en) | 2018-03-13 | 2018-03-13 | Cyclone separator capable of automatically cleaning filter cylinder to prevent pasting net and normal-pressure blanking to prevent dust spraying |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN108360094A true CN108360094A (en) | 2018-08-03 |
| CN108360094B CN108360094B (en) | 2023-07-21 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810205053.5A Active CN108360094B (en) | 2018-03-13 | 2018-03-13 | Cyclone separator capable of automatically cleaning filter cylinder to prevent pasting net and normal-pressure blanking to prevent dust spraying |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109440237A (en) * | 2018-12-24 | 2019-03-08 | 恒天重工股份有限公司 | A kind of double mouth-piece type Aerodynamic fiber separators of double volute |
| CN112746980A (en) * | 2020-12-31 | 2021-05-04 | 深圳市银星智能科技股份有限公司 | Fan subassembly and cleaning machines people |
| CN112853552A (en) * | 2021-02-02 | 2021-05-28 | 青岛诚利佳机械有限公司 | Hair coagulating device |
| CN113893635A (en) * | 2021-11-16 | 2022-01-07 | 江苏精亚环境科技有限公司 | Secondary dust, pile and dust separating method and equipment for dust filter unit |
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| CN112746980A (en) * | 2020-12-31 | 2021-05-04 | 深圳市银星智能科技股份有限公司 | Fan subassembly and cleaning machines people |
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| CN112853552A (en) * | 2021-02-02 | 2021-05-28 | 青岛诚利佳机械有限公司 | Hair coagulating device |
| CN113893635A (en) * | 2021-11-16 | 2022-01-07 | 江苏精亚环境科技有限公司 | Secondary dust, pile and dust separating method and equipment for dust filter unit |
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|---|---|
| CN108360094B (en) | 2023-07-21 |
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