CN209405812U - Multifunctional solid-liquid or dust separation machine - Google Patents
Multifunctional solid-liquid or dust separation machine Download PDFInfo
- Publication number
- CN209405812U CN209405812U CN201822011340.0U CN201822011340U CN209405812U CN 209405812 U CN209405812 U CN 209405812U CN 201822011340 U CN201822011340 U CN 201822011340U CN 209405812 U CN209405812 U CN 209405812U
- Authority
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- China
- Prior art keywords
- cartridge filter
- dust
- swirl cylinder
- sewage
- removing system
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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- 239000000428 dust Substances 0.000 title claims abstract description 49
- 239000007788 liquid Substances 0.000 title claims abstract description 25
- 238000000926 separation method Methods 0.000 title claims abstract description 15
- 239000010865 sewage Substances 0.000 claims abstract description 41
- 239000002893 slag Substances 0.000 claims abstract description 22
- 238000001914 filtration Methods 0.000 claims abstract description 17
- 230000007246 mechanism Effects 0.000 claims abstract description 9
- 230000001360 synchronised effect Effects 0.000 claims abstract description 8
- 238000007599 discharging Methods 0.000 claims description 17
- 230000009471 action Effects 0.000 claims description 2
- 239000002994 raw material Substances 0.000 abstract description 4
- 239000004568 cement Substances 0.000 abstract description 2
- 238000007789 sealing Methods 0.000 description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 13
- 238000003466 welding Methods 0.000 description 12
- 239000003638 chemical reducing agent Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 5
- 239000007787 solid Substances 0.000 description 4
- 239000002184 metal Substances 0.000 description 3
- 230000008901 benefit Effects 0.000 description 2
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 210000005239 tubule Anatomy 0.000 description 2
- 241000208340 Araliaceae Species 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 235000005035 Panax pseudoginseng ssp. pseudoginseng Nutrition 0.000 description 1
- 235000003140 Panax quinquefolius Nutrition 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003818 cinder Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 235000008434 ginseng Nutrition 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000012716 precipitator Substances 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 230000003519 ventilatory effect Effects 0.000 description 1
Classifications
-
- 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
Landscapes
- Filtration Of Liquid (AREA)
Abstract
The utility model relates to a kind of Multifunctional solid-liquid or dust separation machines, including rack, it is provided with eddy flow strainer synchronous filtering on the rack, continuous slag removing system is concentrated, it includes closed swirl cylinder, swirl cylinder coaxial is provided with cartridge filter, there is cavity between swirl cylinder and cartridge filter, raw material to be separated is inputted the cavity by feeding mechanism；The cartridge filter is fixed in hollow shaft and is rotated in swirl cylinder by hollow shaft driving, cartridge filter is filtered the raw sewage or dust to be separated in swirl cylinder, and the cartridge filter upper end is provided with driving eddy flow tube inner chamber raw sewage to be separated or the high-speed rotating paddle piece of dust.The utility model further includes raw sewage or dust washes away continuous slag removing system and the continuous slag removing system of negative-pressure ward, continuous filtering, efficient concentration is carried out to filter residue, in addition automatic ash ejector, does not consume drainage or net air carries out recoil slagging-off and carries out energy-efficient filtering purpose to sewage or dust to reach.It is used suitable for industries such as high pollution sewage treatment plant and cement plants.
Description
Technical field
The utility model relates to a kind of sewage water filtration and cleaners, remove as what solid-liquid separating machine and air-borne dust separated
Dirt machine uses, and belongs to sewage and dust processing technology field.
Background technique
When current sewage water filtration machine operation on the market, with the extension of time, the outer filter residue of filter screen can be gradually strainer
Blocking, declines strainer filtering efficiency rapidly, at this moment will consume a large amount of drainage and backwash to strainer, backwashes heel row
Filter residue water content out is very high, and existing sewage filter exists and can not continuously remove the gred, and recoil water consumption is big, filter residue enrichment
Low and low filter efficiency disadvantage.
In addition, sack cleaner on the market is essentially all to assemble outside cloth bag to after certain thickness dust at present,
It is just recoiled and is struck with complicated various high pressure gas recoiling devices when efficiency of dust collection substantially lowers, the powder got lodged in outside cloth bag
Dirt removes, and is then further continued for working, and such operation dust-removal cloth-bag easily blocks, and ventilatory capacity is small, low efficiency, device structure are multiple
Miscellaneous, vulnerable part is more and non-refractory.
Summary of the invention
In view of the above technical problems, the purpose of the utility model is to provide a kind of Multifunctional solid-liquid or gas dirt seperator, solutions
Certainly at present sewage filter on the market or dust precipitator can not continuously remove the gred, inefficiency the shortcomings that.
In order to achieve the above objectives, the utility model uses following technical scheme:
A kind of Multifunctional solid-liquid or dust separation machine, including rack, it is dense to be provided with eddy flow strainer synchronous filtering on the rack
Contract continuous slag removing system, dreg removing system, draining or exhaust system, and continuous slag removing system is concentrated in the eddy flow strainer synchronous filtering
Including closed swirl cylinder, swirl cylinder coaxial is provided with cartridge filter, there is cavity between swirl cylinder and cartridge filter, into sewage or
Raw sewage to be separated or dust are inputted the cavity by dust mechanism；The cartridge filter is fixed in hollow shaft and is driven by hollow shaft
It is rotated in swirl cylinder, cartridge filter is filtered the raw material to be separated in swirl cylinder, and the cartridge filter upper end is provided with drive
Dynamic eddy flow tube inner chamber raw sewage to be separated or the high-speed rotating paddle piece of dust.
Further, described into sewage or dust mechanism includes that raw sewage or dust wash away continuous slag removing system, described
It includes protruding into swirl cylinder the jet pipe being aligned close to cartridge filter direction that raw sewage or gas dirt, which wash away continuous slag removing system, is set on jet pipe
Several nozzles towards cartridge filter are equipped with, jet pipe connection lift clutch simultaneously can make nozzle exist under the action of lift clutch
It is moved back and forth up and down in cartridge filter altitude range, raw sewage or dust to be filtered are by entering jet pipe from spray for sewage or dust pump
Mouth enters in swirl cylinder after injecting on cartridge filter.
Further, which further includes the continuous slag removing system of negative-pressure ward, and the negative-pressure ward continuously removes slag system
System includes that cartridge filter excircle is provided with that several piece is distributed with even circumferential and is arranged with cartridge filter in tangential angle close to strainer
Pressure reductor.
Further, the pressure reductor is fixed by the bracket in swirl cylinder inner wall.
Further, the pressure reductor and cartridge filter are arranged in tangential angle refers to pressure reductor along cartridge filter rotation side
To far from cartridge filter.
Further, the dreg removing system is included in swirl cylinder upper end and is provided with upper cover plate, is provided on upper cover plate
Mud hole, upper mud hole are connected with the upper scum pipe of residual cake valve, and swirl cylinder lower part is provided with lower dreg discharging hole, lower row
Lower dreg discharging pipe and automatic emptying machine with auger are provided with outside cinder hole.
Further, the swirl cylinder upper section is cylindrical tube, and lower section is up big and down small conical pipe, and lower dreg discharging hole is set
It sets in swirl cylinder lower end side.
Further, the draining or exhaust system include the hollow shaft in cartridge filter, and hollow shaft is located in cartridge filter
One section be provided with several taps, end socket is arranged in the upper end of hollow shaft, and lower end connects output mechanism.
Further, the outlet setting of the output mechanism is higher than swirl cylinder upper port.
Further, upper end cover and lower cover, strainer, orifice plate cylinder of the cartridge filter by center with axis hole are constituted, orifice plate
Cylinder is cylindrical, and strainer setting is provided with several piece paddle piece on orifice plate drum outer wall, upper end cover.
The utility model has the advantages that
Multifunctional solid-liquid or gas dirt seperator provided by the invention, overcome existing sewage filter and air dust remover without
The disadvantage that method continuously removes the gred, back-flushing or gas consumption amount are big, the filter residue enrichment of discharge is low and filter efficiency is poor.The machine has structure
Simply, there is no Mechanical Contact component directly with strainer, no mechanical abrasion, when strainer stainless steel material when compact, slagging-off
When, it is resistant to 480 degree of high temperature and works continuously, strainer long service life, other few easy workout parts, durable, the automatic continuous benefit of energy
Slagging-off is washed away with raw sewage or dust, continuous negative pressure suction slagging-off is continuous to filter, efficient concentration carried out to filter residue, automatic ash ejector,
In addition it not consume drainage or net air carries out recoil slagging-off and carries out energy-efficient filtering purpose to sewage or dust to reach.
Present invention is particularly suitable for the use of the industries such as high pollution sewage treatment plant and cement plant, due to complete machine structure is simple,
Occupied area is small, energy-efficient, so as to save largely found the factory land area and investment operating cost.
Detailed description of the invention
Fig. 1 is broken section organigram of the embodiment of the present invention:
Fig. 2 is A-A cross-sectional view in Fig. 1:
In figure: 1, lift clutch, 2, upper branching holder, 3, driving motor, 4, shaft coupling, 5, lower bearing support, 6, upper bearing (metal)
Seat, 7, upper scum pipe, 8, upper residual cake valve, 9, upper bearing (metal), 10, upper cover plate, 11, upper mud hole, 12, sealing device one, 13, upper branch
Frame, 14, upper lantern ring, 15, upper end cover, 16, paddle piece, 17, strainer, 18, orifice plate cylinder, 19, lower bracket, 20, lower collar, 21, under
End cap, 22, automatic emptying machine, 23, lower cover plate, 24, centre bore three, 25, connector, 26, three-way connection, 27, water inlet pipe, 28,
Centre bore one, 29, rodding eye, 30, sealing device three, 31, cartridge filter, 32, swirl cylinder, 33, sparge pipe, 34, hollow shaft, 35,
Apopore, 36, rack fixing seat, 37, lower dreg discharging pipe, 38, lower dreg discharging hole, 39, centre bore two, 40, sealing device two, 41, under
Bearing, 42, sealing device three, 43, step, 44, reducer pipe, 45, outlet pipe, 46, rack, 47, pressure reductor, 48, screw thread
Hole, 49, nozzle.
Specific embodiment
With reference to the accompanying drawing 1 and the embodiment of 2 pairs of Multifunctional solid-liquids of the invention of attached drawing or gas dirt seperator do and retouch in detail
It states:
For ease of description, this specific embodiment is described using Multifunctional solid-liquid seperator as specific embodiment, i.e.,
Raw material to be separated is by taking the sewage that solid-liquid mixes as an example, and when being related to Multifunctional, air dirt seperator, raw material to be separated is replaced with gas
Dirt, and the components such as filter screen appropriate are selected, belonging to those skilled in the art can be made accordingly by following specific embodiments
The routine techniques of change.
It is dense to be provided with eddy flow strainer synchronous filtering in rack 46 for Multifunctional solid-liquid seperator of the present invention, including rack 46
Contract continuous slag removing system, and raw water washes away the continuous slag removing system of continuous slag removing system, negative-pressure ward, dreg removing system, drainage system.
It includes closed swirl cylinder 32,32 inner cavity of swirl cylinder that continuous slag removing system, which is concentrated, in the eddy flow strainer synchronous filtering
It is provided with cartridge filter 31, the cartridge filter 31 is provided centrally with the hollow shaft 34 being fixed to each other with flat key and the and then rotation of hollow shaft 34
Turn, cartridge filter 31 is filtered the sewage in swirl cylinder 32, and 31 upper end of cartridge filter is provided in driving swirl cylinder 32
The high-speed rotating paddle piece 16 of chamber sewage.
The raw water washes away continuous slag removing system and includes sparge pipe 33, protrudes into the interior alignment of swirl cylinder 32 close to 31 side of cartridge filter
To sparge pipe 33 on be provided with several nozzles 49 communicated therewith, 33 upper end of sparge pipe is provided with three-way connection 26 and mutually solid
Surely it is connected, 26 upper end of three-way connection is fixed on 25 lower end of connector, while being fixed on setting automatic on upper branching holder 2
Lifter 1 is fixedly connected by connector 25, and three-way connection is provided with water inlet pipe 27 by 26 side.
The continuous slag removing system of negative-pressure ward includes that 31 excircle of cartridge filter close to strainer 17 is provided with the same circumference of several piece
Pressure reductor 47 equally distributed and being arranged with cartridge filter 31 in tangential angle, 47 upper end of pressure reductor are provided with internal diameter and are greater than filtering
The upper lantern ring 14 of 31 outer diameters of cylinder, upper lantern ring periphery are provided with several uniformly distributed upper brackets 13,13 inner end of upper bracket and upper lantern ring 14
It is fixedly connected with welding manner, outer end is fixed by bolts on 32 inner wall of swirl cylinder, and 47 upper end of pressure reductor is fixed with welding manner
On upper lantern ring 14,47 lower end of pressure reductor is provided with the lower collar 20 that internal diameter is greater than 31 outer diameter of cartridge filter, and 20 periphery of lower collar is set
Several uniformly distributed lower brackets 19 are equipped with, 19 inner end of lower bracket is mutually permanently connected with lower collar 20 with welding manner, outer end spiral shell
Bolt is fixed on 32 inner wall of swirl cylinder, and 47 lower end of pressure reductor is fixed in lower collar 20 with welding manner, pressure reductor 47 and filtering
Cylinder refers to pressure reductor 47 along 31 direction of rotation of cartridge filter far from cartridge filter 31 in tangential angle setting.
The dreg removing system is included in 32 upper end of swirl cylinder and is provided with upper cover plate 10, is provided with mud hole on upper cover plate 10
11, upper mud hole 11 is provided with scum pipe 7 above, be provided on upper scum pipe 7 residual cake valve 8 (residual cake valve is the prior art,
Solid residue can be discharged in the case where keeping pressure without liquid is discharged), 32 lower part of swirl cylinder is provided with lower dreg discharging
Hole 38, lower dreg discharging hole 38 are provided with the lower dreg discharging pipe 37 and automatic emptying machine 22 that auger is had in the outer imperial palace tubule of bore outside.
The drainage system includes hollow shaft 34, and several apopores 35 are provided in the hollow shaft 34 in cartridge filter 31, empty
34 lower end of mandrel is provided with the step 43 with sealing device, be provided with below step 43 be fixed to each other with it and with
The reducer pipe 44 that hollow shaft 34 communicates, the outlet pipe 45 that water outlet is provided on reducer pipe 44 higher than 32 upper port of swirl cylinder are used in combination
Pipe tooth is connected.
Specifically, swirl cylinder 32 be upper section be cylindrical tube, lower section is up big and down small conical pipe and is welded to each other fixation,
Cylindrical tube upper end, which is provided with, is welded to each other fixed outward flange, and 32 lower part of swirl cylinder is provided with lower dreg discharging hole 38, lower dreg discharging hole
It is provided in 38 in the outer imperial palace tubule of bore and has the lower dreg discharging pipe 37 of auger, and fix company with welding manner with swirl cylinder 32
It connects, the automatic emptying machine 22 for driving manage interior auger rotation together is provided on lower dreg discharging pipe 37,32 lower port of swirl cylinder is provided with
Lower cover plate 23 is simultaneously mutually fixedly connected with welding manner, and lower cover plate 23 is provided centrally with centre bore 2 39, swirl cylinder 32 it is outer in
Portion is provided with several rack fixing seats 36, and rack 46 is arranged below rack fixing seat 36 and is mutually fixedly connected with bolt, revolved
32 upper end of flow cartridge is provided with upper cover plate 10 and is mutually permanently connected by the outward flange of swirl cylinder 32 with bolt, sets on upper cover plate 10
It is equipped with centre bore 1, upper mud hole 11 and rodding eye 29.
Sealing device 3 30 is provided with below the rodding eye 29 of upper cover plate 10, upper mud hole 11 is provided with scum pipe above
It 7 and is mutually permanently connected with welding manner, is provided with residual cake valve 8 on upper scum pipe 7, above the centre bore 1 of upper cover plate 10
It is provided with 6 blending bolt of top chock to be mutually permanently connected, is provided with upper bearing (metal) 9 and sealing dress in top chock 6 from top to bottom
1 are set, lower bearing support 5 is provided with above upper cover plate 10, lower end is fixed on upper cover plate 10 with spiral shell plate, 5 top of lower bearing support
It is provided with driving motor 3, lower end base is mutually permanently connected with upper branching holder 2 with bolt, is provided with above driving motor 3
Fulcrum bearing 2, lower end are fixed by bolts to 5 upper end of lower bearing support, are provided with step 43, step below lower cover plate 23
43 are provided centrally with centre bore 3 24, are provided with sealing device 2 40, lower bearing 41 and sealing in step 43 from top to bottom
Device 3 42 is provided with reducer pipe 44 below step 43 and is mutually permanently connected with welding manner, is arranged on reducer pipe 44
There is outlet pipe 45, and be connected with pipe tooth mode, the setting of 45 water outlet of outlet pipe is higher than 32 upper port of swirl cylinder.
It is provided with cartridge filter 31 in swirl cylinder 32, upper end cover 15 and lower cover 21 of the cartridge filter 31 by center with axis hole,
Strainer 17, orifice plate cylinder 18 are constituted, and are provided with several piece paddle piece 16 above upper end cover 15 and are mutually permanently connected with welding manner, hole
Plate cylinder 18 is cylindrical, is made of orifice plate, and 18 upper end of orifice plate cylinder is fixedly connected with upper end cover 15 with welding manner, under orifice plate cylinder 18
End is fixedly connected with lower cover 21 with welding manner, and strainer 17 is arranged in 18 outer wall of orifice plate cylinder and is mutually permanently connected, cartridge filter
31 are provided centrally with hollow shaft 34 of the upper end with end socket, are provided with several apopores 35, hollow shaft 34 and upper end in hollow shaft 34
Lid 15 is mutually permanently connected with flat key.
34 upper end of hollow shaft is upward through centre bore 1, sealing device 1, top chock 6, top and driving motor 3
Arbor by shaft coupling 4 in transmission connection, 34 lower end of hollow shaft is passed down through centre bore 2 39, sealing device 2 40, lower axle
Hold 41, sealing device 3 42, centre bore 3 24 enters in reducer pipe 44.
The sparge pipe 33 that lower end has plug is provided with outside the strainer 17 of cartridge filter 31, close to the pipe in 31 direction of cartridge filter
It is provided with several threaded holes 48 on wall, nozzle 49 is provided in threaded hole 48 and is connect with sparge pipe 33 with bolt fixing method,
It is mutual with pipe tooth with three-way connection 26 above upper cover plate 10 that 33 upper end of sparge pipe is upward through sealing device 3 30, rodding eye 29
Connection, 26 upper end of three-way connection are provided with connector 25 and are mutually fixedly connected with welding manner, and lift clutch 1 is arranged upper
Blending bolt is mutually permanently connected in fulcrum bearing 2, and the telescopic rod of lift clutch 1 is by connector 25 and three-way connection 26 in biography
It is dynamic to connect, water inlet pipe 27 is provided on three-way connection 26 and is connected with pipe tooth.
Working principle and the course of work:
First start the sewage pump being arranged outside driving motor 3, lift clutch 1 and machine or air-introduced machine when operation to be processed
Raw sewage or dust are increased to certain pressure and first enter sparge pipe 33 from water inlet pipe 27 through three-way connection 26 after preposition coarse filtration,
Then enter in swirl cylinder 32 from 49 high speed of each nozzle being arranged in sparge pipe 33, the driving motor 3 at this moment having been turned on drives
16 high speed rotation of cartridge filter 31 and paddle piece, and in swirl cylinder 3 sewage or dust with high speed rotation, while swirl cylinder 32
Interior high-speed rotating centrifugal force the solid matter in handled sewage or dust can be carried out effective solid-liquid and gas dirt separates,
The separated solid matter come out can continuously screw in cylinder bottom automatically and wait arranging, through 31 strainer 17 of cartridge filter it is separated come out it is clean
Liquid, gas enter 31 inner cavity of cartridge filter by orifice plate cylinder 18, then enter in hollow shaft 34 from apopore 35, then flow through down down
Outside the 45 discharge machine of reducer pipe 44 and outlet pipe of port.
After lift clutch 1 is activated, sparge pipe 33 is driven to move back and forth up and down, and and then sparge pipe 33 of nozzle 49
It is moved back and forth up and down by 31 strainer 17 of cartridge filter, since cartridge filter 31 is always maintained at synchronous rotary state, at this moment from nozzle 49
High speed spray water or gas can be comprehensive 31 external surface area of cartridge filter is all washed away in place, so as to handle be sticked to strainer 17
On filter residue all wash away.
When paddle piece 16 is with sewage or dust high speed rotation in swirl cylinder 32, since pressure reductor 47 is in fixing
Stationary state, at this moment the outer high-speed rotating sewage 32 inner wall of swirl cylinder between of cartridge filter 31 or dust understand continuous high speed from subtracting
47 lateral surface of pressing plate washes away the past, to generate certain jet function, makes to generate certain negative pressure simultaneously on the inside of pressure reductor 47
The negative pressuren zone of one fixed width is formed, the negative pressure of the generation, which can come out the filter residue continuous sucking in 17 hole of negative pressuren zone strainer, to be removed
And it is thrown toward barrel and carries out solid-liquid or dust separation again.
When this machine operation after a certain period of time, be then turned on automatic emptying machine 22, the concentrated filter for being deposited to 32 bottom of swirl cylinder
Slag drives auger timing to draw off outside machine through lower dreg discharging pipe 37 by automatic emptying machine, and the dross of upper end is through upper mud hole in swirl cylinder 32
11 and upper scum pipe 7 by upper 8 self-timing discharge machine of residual cake valve outside, each electrical equipment and electrical of the machine is by automatic control set in addition
The control of system.
Identical knot can be used when in face of dust processing problem on the basis of foregoing description in those skilled in the art
The parameter for being suitable for sewage treatment need to only be adjusted to be suitable for the ginseng of gas dirt processing according to routine techniques by structure, identical principle
Number, this specification repeat no more.
Claims (10)
1. a kind of Multifunctional solid-liquid or dust separation machine, including rack are provided with the concentration of eddy flow strainer synchronous filtering on the rack
Continuous slag removing system, dreg removing system, draining or exhaust system, it is characterised in that: the eddy flow strainer synchronous filtering, which is concentrated, to be connected
Continuous slag removing system includes closed swirl cylinder, and swirl cylinder coaxial is provided with cartridge filter, is had time between swirl cylinder and cartridge filter
Raw sewage to be separated or dust are inputted the cavity into sewage or dust mechanism by chamber；The cartridge filter is fixed in hollow shaft simultaneously
It is rotated in swirl cylinder by hollow shaft driving, cartridge filter is filtered the raw sewage or dust to be separated in swirl cylinder, described
Cartridge filter upper end be provided with driving eddy flow tube inner chamber raw sewage to be separated or the high-speed rotating paddle piece of dust.
2. Multifunctional solid-liquid according to claim 1 or dust separation machine, it is characterised in that: into sewage or dust mechanism packet
It includes raw sewage or dust washes away continuous slag removing system, it includes protruding into swirl cylinder that the raw sewage or dust, which wash away continuous slag removing system,
Interior alignment is provided with several nozzles towards cartridge filter on jet pipe close to the jet pipe in cartridge filter direction, and jet pipe connects automatic lifting
Device simultaneously can be such that nozzle moves back and forth up and down in cartridge filter altitude range under the action of lift clutch, raw sewage to be filtered
Or dust is entered in swirl cylinder by entering after sparge pipe injects on cartridge filter from nozzle for sewage or dust pump.
3. Multifunctional solid-liquid according to claim 1 or 2 or dust separation machine, it is characterised in that: the seperator further includes
The continuous slag removing system of negative-pressure ward, the continuous slag removing system of negative-pressure ward include that cartridge filter excircle close to strainer is provided with number
Pressure reductor that block is distributed with even circumferential and being arranged with cartridge filter in tangential angle.
4. Multifunctional solid-liquid according to claim 3 or dust separation machine, it is characterised in that: the dreg removing system is included in
Swirl cylinder upper end is provided with upper cover plate, and mud hole is provided on upper cover plate, and upper mud hole is connected with the upper of residual cake valve
Scum pipe is provided with lower dreg discharging hole in swirl cylinder lower part, and lower dreg discharging pipe with auger and automatic is provided with outside lower dreg discharging hole
Unloader.
5. Multifunctional solid-liquid according to claim 4 or dust separation machine, it is characterised in that: the swirl cylinder upper section is circle
Column tube, lower section are up big and down small conical pipe, and lower dreg discharging hole is arranged in swirl cylinder lower end side.
6. Multifunctional solid-liquid according to claim 3 or dust separation machine, it is characterised in that: the draining or exhaust system
Including the hollow shaft in cartridge filter, hollow shaft be located in cartridge filter one section is provided with several taps, and the upper end of hollow shaft is set
End socket is set, lower end connects output mechanism.
7. Multifunctional solid-liquid according to claim 6 or dust separation machine, it is characterised in that: the discharge of the output mechanism
Mouth setting is higher than swirl cylinder upper port.
8. Multifunctional solid-liquid according to claim 3 or dust separation machine, it is characterised in that: the pressure reductor passes through branch
Frame is fixed on swirl cylinder inner wall.
9. Multifunctional solid-liquid according to claim 3 or dust separation machine, it is characterised in that: the pressure reductor and filtering
Cylinder refers to pressure reductor along cartridge filter direction of rotation far from cartridge filter in tangential angle setting.
10. Multifunctional solid-liquid according to claim 3 or dust separation machine, it is characterised in that: cartridge filter is had by center
Upper end cover and lower cover, strainer, the orifice plate cylinder of axis hole are constituted, and orifice plate cylinder is cylindrical, and strainer is arranged in orifice plate drum outer wall, upper end
It covers and is provided with several piece paddle piece.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822011340.0U CN209405812U (en) | 2018-11-24 | 2018-11-24 | Multifunctional solid-liquid or dust separation machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822011340.0U CN209405812U (en) | 2018-11-24 | 2018-11-24 | Multifunctional solid-liquid or dust separation machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209405812U true CN209405812U (en) | 2019-09-20 |
Family
ID=67936199
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201822011340.0U Expired - Fee Related CN209405812U (en) | 2018-11-24 | 2018-11-24 | Multifunctional solid-liquid or dust separation machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209405812U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113952785A (en) * | 2021-11-24 | 2022-01-21 | 深圳市福昌发电路板有限公司 | Sewage treatment system for manufacturing decorative printing paper |
-
2018
- 2018-11-24 CN CN201822011340.0U patent/CN209405812U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113952785A (en) * | 2021-11-24 | 2022-01-21 | 深圳市福昌发电路板有限公司 | Sewage treatment system for manufacturing decorative printing paper |
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Granted publication date: 20190920 |