CN109675727A - Multistage dish-style cyclone separator - Google Patents
Multistage dish-style cyclone separator Download PDFInfo
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- CN109675727A CN109675727A CN201910051033.1A CN201910051033A CN109675727A CN 109675727 A CN109675727 A CN 109675727A CN 201910051033 A CN201910051033 A CN 201910051033A CN 109675727 A CN109675727 A CN 109675727A
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- disk
- rotary drum
- hollow shaft
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- pipe
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B11/00—Feeding, charging, or discharging bowls
- B04B11/02—Continuous feeding or discharging; Control arrangements therefor
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B15/00—Other accessories for centrifuges
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B7/00—Elements of centrifuges
- B04B7/02—Casings; Lids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B7/00—Elements of centrifuges
- B04B7/08—Rotary bowls
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B7/00—Elements of centrifuges
- B04B7/08—Rotary bowls
- B04B7/12—Inserts, e.g. armouring plates
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Abstract
The present invention relates to a kind of multistage dish-style cyclone separators, including rack, it is provided with eddy flow and the synchronous separation of solid and liquid of multistage rotary drum and continuous discharging slag system on the rack, it includes closed swirl cylinder, swirl cylinder coaxial is provided with the drum assembly that multistage rotary drum is formed by stacking, the drum assembly is fixed in hollow shaft and is and then rotated in swirl cylinder by the hollow shaft that driving motor drives, drum assembly is step by step centrifuged raw sewage to be separated or dust, driving eddy flow tube inner chamber sewage to be separated or the high-speed rotating impeller of dust are provided in the drum assembly lower end hollow shaft.The invention also includes raw sewage or dust continuous discharging slag system and swirl cylinder secondary timing dreg removing system, water inlet system and drainage system, complete machine can reach full-automatic continuously into sewage or dust, continuous discharging slag and the continuous purpose for emptying water or net gas when operation.It is used suitable for operations such as high pollution sewage treatment plant and cement plants.
Description
Technical field
The present invention relates to a kind of solid-liquid and dust separation equipment, the dust removal machine separated as solid-liquid separating machine and air-borne dust
It uses, belongs to sewage and dust processing technology field.
Background technique
Disc centrifugal separator on the market at present is that the centrifugal force that the superfast operating of disk in rotary drum generates makes
Solid-liquid in rotary drum is separated, and passes through complicated slag-draining device again after the detritus tank steric bulk in rotary drum is to certain altitude
It is timed deslagging, this knot design has the disadvantage in that one, since its revolving speed nearly all will be in 6000 revs/min or more superelevation
Speed operation, cause complete machine structure organism stability it is poor, design it is sufficiently complex, production required precision it is very high, prototype fabrication difficulty, at
This is very big；Two, since rotary drum disk belongs to single-stage, direct current is designed from bottom to up, and the processed liquid of institute is entered from disk lower end
The contact disk centrifuge separation time is short when upper end is flowed out, and solid-liquid separation efficiency is low；Three, when the sediment of sediment pool space can not be timely
Discharge causes to be stacked into after certain altitude when being timed deslagging by the slag-draining device of complexity again, the sediment above detritus tank
It is easy to that separated liquid is followed up to be discharged outside machine, to lower solid-liquid separation effect, while structure is complicated for slag-draining device
And in due course deslagging is not easy to accurately control.
Summary of the invention
In view of the above technical problems, the object of the present invention is to provide a kind of multistage dish-style cyclone separator, current city is solved
Disc centrifugal separator on face exists because revolving speed is high, manufacture is complicated, precision is high, investment cost is big, and solid-liquid separation efficiency is low, row
Slag device is complicated, is not easy the shortcomings that accurately controlling.
In order to achieve the above objectives, the invention adopts the following technical scheme:
A kind of multistage dish-style cyclone separator, including rack are provided with eddy flow and the synchronous solid-liquid of multistage rotary drum on the rack
Separation and continuous discharging slag system, eddy flow is separated by solid-liquid separation and regular cinder-discharge system, water inlet system, drainage system；The eddy flow and
The synchronous separation of solid and liquid of multistage rotary drum and continuous discharging slag system, including closed swirl cylinder, eddy flow tube inner chamber is provided with drum assembly,
Drum assembly is provided centrally with the hollow shaft being fixed to each other with flat key and is and then rotated by the hollow shaft that driving motor drives, rotary drum
Various disks carry out multistage separation of solid and liquid to the sewage for inputting its inner cavity from bottom to up in assembly, set below the drum assembly
It is equipped with the impeller of driving eddy flow tube inner chamber sewage high-speed rotational.
Further, the eddy flow is separated by solid-liquid separation and dreg removing system includes closed swirl cylinder, upper section be cylindrical tube,
Lower section is up big and down small conical pipe, and the upper end is provided with upper end cover, and its underpart barrel is provided with mud hole, is arranged outside mud hole
There are the scum pipe and automatic emptying machine that auger is had in pipe.
Further, the water inlet system includes hollow shaft and the top chock being connected, top chock upside
Wall is provided with water inlet one and water inlet pipe, and center hollow shaft corresponding position is provided with several inlet openings two；Hollow shaft is in middle section
Several inlet openings three are provided with above the bottom disk of bottom grade rotary drum.
Further, the upper drainage system of the drainage system point and lower drainage system: upper drainage system includes top turn
Drum center upper end is provided with diversion pipe, and diversion pipe upper end, which is protruded into top chock, to be connected, and top chock lower wall is provided with
Apopore one and upper water-out pipe；Lower drainage system includes the several apopores two being arranged in above impeller in hollow shaft, hollow shaft
With in sealing device step, step side wall is provided with apopore three and outlet pipe, outlet pipe for lower port setting
On be provided with control valve.
Further, the fulcrum bearing higher than top chock is provided with above the upper end cover, lower end and upper end cover are used
Bolt is mutually permanently connected, and fulcrum bearing upper end center is provided with centre bore one, and top is provided with driving motor, driving motor machine
Seat and fulcrum bearing are mutually permanently connected with bolt, and the arbor of driving motor extends downwardly into below fulcrum bearing directly from centre bore one
Drive hollow shaft operation.
Further, drum assembly is provided in the swirl cylinder, drum assembly is by bottom grade rotary drum, one to several middle ranks
Rotary drum and top rotary drum are formed by stacking step by step.
Further, the intermediate rotary drum by overall diameter is less than the outer tube of swirl cylinder cylinder diameter, lower disk, leads
Flow disk, one into several pieces disk, upper disk, pushing off the slag pipe and diameter be greater than hollow shaft diameter inner sleeve constitute, inner sleeve with
The same length setting of outer tube, inner sleeve and outer tube level height are arranged higher than 30-45 degree, and upper disk lower end is provided with several
Lower water inlet, upper end are provided with several upper water-out mouths, and lower end setting is fixed in outer sleeve upper next point, and upper end setting is fixed
In interior sleeve upper end next point, lower disk upper end is provided with several upper water-out mouths, and lower end setting is fixed on outer tube lower end
On a bit, upper end setting is fixed on inner sleeve lower end on a bit, and pushing off the slag pipe, the setting of pushing off the slag pipe are provided with above lower disk lower section
At up big and down small conical pipe, pushing off the slag pipe upper end is provided with the slag inlet apart from outer tube one fixed width, and lower end setting is fixed on down
On disk, pushing off the slag pipe and outer tube and lower tab (s) constitute detritus tank, and middle disk is arranged in parallel in disk following distance,
Lower end is provided with several lower water inlets, and upper end is provided with several upper water-out mouths, and lower end setting is fixed on pushing off the slag pipe upper end, leads
Stream disk is arranged in parallel among middle disk and lower disk, and lower end is provided with several lower water inlets, and lower end setting is fixed on
On pushing off the slag pipe, the upper end setting is fixed on inner sleeve, and outer tube is provided with several scum holes on the tube wall above lower disk.
Further, the bottom grade rotary drum is arranged below intermediate rotary drum, and bottom disk is not provided on several
The mouth of a river, several inlet openings three are provided on the inner sleeve between bottom disk upper end and the water conservancy diversion disk of top, and bottom grade rotary drum removes
Other than these above-mentioned settings are different, other structures and intermediate rotary drum all same design.
Further, the upper disk lower end of the top rotary drum is not provided with lower water inlet, the upper end top layer water outlet
Top is provided with the diversion pipe that diameter is greater than inner sleeve, and the setting of diversion pipe lower end is fixed on disk, during upper end is upward through
Heart hole three and sealing device three enter top chock inner cavity and with sealing device three together in rotation connection, and top rotary drum is except above-mentioned
Other than these settings are different, other structures and intermediate rotary drum all same design.
Further, the hollow shaft is arranged at swirl cylinder center, and the upper end is upward through and is fixed to each other with flat key
Each casing in drum assembly center after, then sequentially pass through upwards from top chock sealing device two, sealing device one, upper bearing (metal) and
Centre bore two, by the arbor of shaft coupling and driving motor in transmission connection, hollow shaft top is provided with upper plug head, close on top
Several inlet openings two are provided in hollow shaft between seal apparatus one and sealing device two, in the bottom disk upper end of bottom grade rotary drum
The same inlet opening three communicated, inlet opening in hollow shaft are provided in the hollow shaft for three position of inlet opening being arranged on casing
Three lower sections are provided with lower end cap, are provided with several apopores two under lower end cap on tube wall, are arranged on two lower section outer tube wall of apopore
There is the impeller with several blades, impeller is fixedly connected with hollow shaft with flat key, and hollow shaft lower end sequentially passes through centre bore four, close
Seal apparatus four, lower bearing and sealing device five enter three top of apopore in step.
Beneficial effect
Multistage butterfly cyclone separator provided by the invention, overcome existing butterfly seperator can not continuously timely deslagging and
The former solid-liquid or dust separated residence time between tab (s) is short, and separative efficiency is poor, separately since complete machine wants ultrahigh speed to run, sample
Machine manufactures precision prescribed height, the big disadvantage of investment cost that structure is complicated.The machine is existing since running speed design can be significantly less than
Butterfly centrifugal machine, by isolated solid-liquid or dust, the residence time is long between tab (s), and separative efficiency is high, with simple structure, tightly
Gather, solid-liquid or dust separation and when slagging-off do not have direct mechanical abrasion, complete machine few easy workout part, manufacturing expense is low, can be continuous
It runs durable, high efficiency solid-liquid automatically continuously can be carried out to raw sewage or dust or gas dirt separates, it is continuous early period by rotary drum
Regular deslagging reaches efficient automatic discharge purpose in deslagging and later period swirl cylinder.
The industries such as the especially suitable high pollution sewage treatment plant of the present invention and cement plant use, since complete machine structure is simple, accounts for
Ground area is small, energy-efficient, so as to save largely found the factory land area and investment operating cost.
Detailed description of the invention
Attached drawing is section view organigram of the embodiment of the present invention:
In figure: 1, driving motor, 2, centre bore one, 3, shaft coupling, 4, fulcrum bearing, 5, bearing cap, 6, upper plug head, 7, upper axis
Hold seat, 8, upper water-out pipe, 9, apopore one, 10, upper end cover, 11, centre bore three, 12, diversion pipe, 13, top rotary drum, 14, rotation
Flow cartridge, 15, upper disk, 16, lower water inlet, 17, outer tube, 18, pushing off the slag pipe, 19, detritus tank, 20, scum hole, 21, Di Jizhuan
Drum, 22, rack fixing seat, 23, bottom disk, 24, mud hole, 25, scum pipe, 26, automatic emptying machine, 27, lower cover, 28,
Apopore three, 29, step, 30, centre bore two, 31, upper bearing (metal), 32, sealing device one, 33, inlet opening one, 34, water inlet
Pipe, 35, inlet opening two, 36, sealing device two, 37, hollow shaft, 38, sealing device three, 39, clamp nut, 40, top layer water outlet
Mouthful, 41, drum assembly, 42, inner sleeve, 43, upper water-out mouth, 44, middle disk, 45, water conservancy diversion disk, 46, intermediate rotary drum, 47, under
Disk, 48, inlet opening three, 49, lower end cap, 50, apopore two, 51, impeller, 52, centre bore four, 53, sealing device four, 54,
Lower bearing, 55, sealing device five, 56, rack, 57, control valve, 58, lower discharging tube.
Specific embodiment
The embodiment of multistage dish-style cyclone separator of the invention is described in detail with reference to the accompanying drawing: for the ease of retouching
It states, this specific embodiment carries out raw material i.e. to be separated by taking the sewage that solid-liquid mixes as an example by multistage dish-style cyclone separator, is related to
When to dust separation, raw material to be separated is replaced by dust, and select admission line bore, hole number of slagging tap and shape appropriate
And the components such as rotary drum volume, the conventional skill accordingly changed can be made by following specific embodiments by belonging to those skilled in the art
Art.
Multistage dish-style cyclone separator of the invention, including rack 56, are provided with eddy flow in rack 56 and multistage rotary drum is same
Centrifugal solid-liquid separation and continuous discharging slag system are walked, eddy flow is separated by solid-liquid separation and regular cinder-discharge system, water inlet system, drainage system.
The eddy flow and the synchronous separation of solid and liquid of multistage rotary drum and continuous discharging slag system include closed swirl cylinder 14, eddy flow
14 inner cavities of cylinder are provided with the drum assembly 41 being formed by stacking by bottom grade rotary drum 21, intermediate rotary drum 46 and top rotary drum 13, and described turn
Drum assembly 41 is provided centrally with the hollow shaft 37 being fixed to each other with flat key and and then hollow shaft 37 rotates, various in drum assembly 41
Disk carries out multistage separation of solid and liquid to the sewage for inputting its inner cavity from bottom to up, continuous from the sediment in rotary drum inner cavity detritus tank 19
Inflow 14 inner cavity of swirl cylinder is discharged from scum hole 20 to be separated by solid-liquid separation again, is provided with driving below the drum assembly 41
The impeller 51 of 14 inner cavity sewage high-speed rotational of swirl cylinder.
The cyclonic separation and dreg removing system include swirl cylinder 14 be upper section be cylindrical tube, lower section is up big and down small cone
Shape pipe, the upper end are provided with upper end cover 10, and its underpart barrel is provided with mud hole 24, and the outer imperial palace of bore is provided with outside mud hole 24
The scum pipe 25 and automatic emptying machine 26 of auger are had in tubule.
The water inlet system includes hollow shaft 37 and the top chock being connected 7, and 7 upper side wall of top chock is provided with
Inlet opening 1 and water inlet pipe 34,37 corresponding position of center hollow shaft are provided with several inlet openings 2 35,37 middle section of hollow shaft
Several inlet openings three are provided with above the bottom disk 23 of bottom grade rotary drum 21.
The upper drainage system of the drainage system point and lower drainage system, upper drainage system include top 13 center upper end of rotary drum
It is provided with diversion pipe 12,12 upper end of diversion pipe, which is protruded into top chock 7, to be connected, and 7 lower wall of top chock is provided with water outlet
Hole 1 and upper water-out pipe 8；Lower drainage system includes the several apopores 2 50 being arranged in 51 top hollow shaft 37 of impeller, empty
37 lower end of mandrel is arranged in the step 29 with sealing device, 29 lower wall of step be provided with apopore 3 28 and
Outlet pipe 58 is provided with control valve 57 on outlet pipe 58.
Specifically, swirl cylinder 14 be upper section be cylindrical tube, lower section is up big and down small conical pipe and mutually solid with welding
Fixed, cylindrical tube upper end, which is provided with, is welded to each other fixed outward flange, and 14 lower part of swirl cylinder is provided with mud hole 24, mud hole 24
It is inside provided with the scum pipe 25 with auger in the outer imperial palace tubule of bore and is fixedly connected with swirl cylinder 14 with welding manner, eddy flow
14 lower ports of cylinder are provided with lower cover 27 and are mutually fixedly connected with welding manner, and lower cover 27 is provided centrally with centre bore four
52, the outer middle part of swirl cylinder 14 is provided with several rack fixing seats 22, and rack 56 is arranged below rack fixing seat 22 and mutually uses
Bolt is fixedly connected, and 14 upper end of swirl cylinder is provided with upper end cover 10 and is fixed to each other company by the outward flange of swirl cylinder 14 with bolt
It connects, upper end cover 10 is provided centrally with centre bore 3 11.
10 centre bore 3 11 of upper end cover is provided with 7 blending bolt of top chock above and is mutually permanently connected, in top chock 7
It is provided centrally with hollow shaft 37, is provided with upper bearing (metal) 31, sealing between 37 outer diameter of 7 inner wall of top chock and hollow shaft from top to bottom
Sealing device three between device 1,12 outer diameter of sealing device 2 36, diversion pipe 12 and 7 inner wall of top chock and diversion pipe
38,7 upper end of top chock is provided with center and is mutually permanently connected with 5 blending bolt of bearing cap of centre bore 2 30, upper bearing (metal)
7 upper side walls of seat are provided with inlet opening 1, and water inlet pipe 34 is provided with outside inlet opening 1 and uses welding mutually solid with top chock 7
Fixed connection, 7 lower wall of top chock are provided with apopore 1, be provided with outside apopore 1 upper water-out pipe 8 and with top chock 7
It is mutually permanently connected with welding.
The fulcrum bearing 4 higher than top chock 7 is provided with above upper end cover 10, lower end is mutually solid with bolt with upper end cover 10
Fixed connection, 4 upper end center of fulcrum bearing are provided with centre bore 1, and top is provided with driving motor 1,1 base of driving motor and branch
It holds seat 4 to be mutually permanently connected with bolt, the arbor of driving motor 1 extends downwardly into 4 lower section of fulcrum bearing from centre bore 1, eddy flow
14 lower ends of cylinder are provided with the lower cover 27 with centre bore 4 52 and are mutually permanently connected with welding, are provided with below lower cover 27
29 blending bolt of step is mutually permanently connected, and is provided with sealing device 4 53, lower bearing in step 29 from top to bottom
54 and sealing device 5 55,29 lower sides of step are provided with apopore 3 28, and lower water outlet is provided with outside apopore 3 28
Pipe 58 is simultaneously connect with step 29 with being welded and fixed, and control valve 57 is provided on lower discharging tube 58.
Drum assembly 41 is provided in swirl cylinder 14, drum assembly 41 is by bottom grade rotary drum 21, one to several intermediate rotary drums 46
And top rotary drum 13 is formed by stacking step by step.
Intermediate rotary drum 46 is less than outer tube 17, lower disk 47, the water conservancy diversion disk of the cylindrical diameter of swirl cylinder 14 by overall diameter
45, an inner sleeve 42 that disk 44, upper disk 15, pushing off the slag pipe 18 and diameter are greater than 37 diameter of hollow shaft into several pieces is constituted, interior
Casing 42 and the same length of outer tube 17 are arranged, and inner sleeve 42 and 17 level height master-hand's 30-45 degree of outer tube are arranged, upper disk
15 lower ends are provided with several lower water inlets 16, upper end is provided with several upper water-out mouths 43, and lower end is arranged under 17 upper end of outer tube
A little and with connection is welded and fixed, upper end is arranged in 42 upper end next point of inner sleeve and is fixedly connected with welding manner, lower disk
47 upper ends are provided with several upper water-out mouths 43, and lower end is arranged on 17 lower end of outer tube a little and is connected with being welded and fixed, upper end
It is arranged on 42 lower end of inner sleeve a little and with connection is welded and fixed, is provided with pushing off the slag pipe 18, pushing off the slag above lower 47 lower section of disk
Pipe 18 is arranged to up big and down small conical pipe, and 18 upper end of pushing off the slag pipe is provided with the slag inlet apart from 17 one fixed width of outer tube, lower end
It is arranged on lower disk 47 and is mutually permanently connected with welding, pushing off the slag pipe 18 and outer tube 17 and lower tab (s) constitutes detritus tank 19；
Middle disk 44 is arranged in parallel in 15 following distance of disk, and lower end is provided with several lower water inlets 16, and upper end is provided with
Several upper water-out mouths 43, lower end are arranged on 18 upper end of pushing off the slag pipe and with connection are welded and fixed, and water conservancy diversion disk 45 is arranged in parallel
Among middle disk 44 and lower disk 47, lower end is provided with several lower water inlets 16, and lower end is arranged on pushing off the slag pipe 18 simultaneously
With connection is welded and fixed, the upper end is arranged on inner sleeve 42 and with connection is welded and fixed, and outer tube 17 is on lower disk 47
Tube wall on be provided with several scum holes 20；
Bottom grade rotary drum 21 is arranged below intermediate rotary drum 46, and bottom disk 23 is not provided with several upper water-out mouths 43, bottom
Several inlet openings 3 48, bottom grade rotary drum 21 are provided on inner sleeve 42 between 23 upper end of portion's disk and the water conservancy diversion disk 44 of top
In addition to these above-mentioned settings are different, other structures and intermediate rotary drum 46 all same design；
15 lower end of upper disk of top rotary drum 13 is not provided with lower water inlet 16, is arranged above the upper end top layer water outlet 40
There is diameter to be greater than the diversion pipe 12 of inner sleeve 42,12 lower end of diversion pipe is arranged on upper disk 15 and is connected with being welded and fixed, on
End is upward through centre bore 3 11, and sealing device 3 38 enters 7 inner cavity of top chock and with sealing device 3 38 together in rotation
Connection, top rotary drum 13 in addition to these above-mentioned settings are different, other structures and intermediate rotary drum 46 all same design.
Hollow shaft 37 is arranged at 14 center of swirl cylinder, the drum assembly 41 that the upper end is upward through and is fixed to each other with flat key
After each casing in center, then from top chock 7 sequentially pass through upwards sealing device 2 36, sealing device 1, upper bearing (metal) 31 and in
Heart hole 2 30, by the arbor of shaft coupling 3 and driving motor 1 in transmission connection, 37 top of hollow shaft is provided with stifled on top
First 6, several inlet openings 2 35, bottom grade rotary drum 21 are provided in the hollow shaft 37 between sealing device 1 and sealing device 2 36
23 upper end inner sleeve 42 of bottom disk on be provided with same communicate in the hollow shaft 37 of 3 48 position of inlet opening that is arranged
Inlet opening 3 48,3 48 lower section of inlet opening is provided with lower end cap 49 in hollow shaft 37, is provided on the lower supervisor's wall of lower end cap 49
Several apopores 2 50, are provided with the impeller 51 with several blades on 2 50 lower section outer tube wall of apopore, impeller 51 with it is hollow
Axis 37 is fixedly connected with flat key, and 37 lower end of hollow shaft sequentially passes through centre bore 4 52,4 53 lower bearing 54 of sealing device and sealing
Device 5 55 enters 3 28 top of apopore, hollow shaft 37 in step 29 and is provided with clamp nut above drum assembly 41
39。
Working principle and the course of work:
Control valve 57 and automatic emptying machine 26 are first closed when operation, then start the sewage being arranged outside driving motor 1 and machine
Raw sewage to be processed is first entered hollow shaft from water inlet pipe 34 through inlet opening 1, inlet opening 2 35 after preposition coarse filtration by pump
It is conveyed down in 37, the space between bottom disk 23 and lower disk 47 in the grade rotary drum 21 of bottom is then inputted from inlet opening 3 48
It is flow to pushing off the slag pipe 18 toward lower end, is then passed through the lower water inlet 16 of water conservancy diversion disk 45, the lower water inlet 16 of middle disk 44 and upper dish
The lower water inlet 16 of piece 15 is flowed into full of 21 inner cavity of entire bottom grade rotary drum, then be centrifuged by high-speed rotating various disks solid
Liquid separation, when bringing into operation, the sewage in rotary drum can continuously flow into 14 inner cavity of swirl cylinder from each detritus tank 19 through scum hole 20, to
14 inner cavity of swirl cylinder will be automatically stopped inflow after being full of, because under the high-speed rotating centrifugal force effect of rotary drum, rotary drum edge
The pressure for the sewage that scum hole 20 flows out is greater than the pressure of sewage existing in rotary drum, and since the inner cavity of swirl cylinder 14 is close
It closes, therefore the pressure of sewage that the pressure of sewage existing in swirl cylinder 14 and each scum hole 20 flow out is equal, institute
With when rotary drum runs well, after 14 inner cavity of swirl cylinder is full of sewage, the sewage in rotary drum is will not to flow into swirl cylinder 14 again
Inner cavity, but when opening control valve 57 separated water purification discharge, the pressure of 14 inner cavity of swirl cylinder can be fallen below immediately
The pressure of scum hole 20, at this moment the sediment in rotary drum will continuously flow into 14 inner cavity of swirl cylinder from scum hole 20 through detritus tank 19；
When the sewage of 14 inner cavity of swirl cylinder is operated normally full of complete machine, into bottom grade rotary drum 21 inner cavity sewage can from
Under the action of mental and physical efforts centrifuge separation, after separation cleaner water purification can space between water conservancy diversion disk 45 and middle disk 44, in
The space between the lower disk 47 in space and upper disk 15 and upper level rotary drum between disk 44 and upper disk 15 is toward upper end
Respective upper water-out mouth 43 up flow into through being then further centrifugated by former mode in rotary drum 46, again separate after
Water purification up flows into top rotary drum 13 from respective upper water-out mouth 43 again and is finally centrifugated, last separated to come out
Water purification flows into 6 inner cavity of top chock by diversion pipe 12 from the top layer water outlet 40 of top rotary drum 13, then passes through from apopore 1
It crosses outside 8 discharge machine of upper water-out pipe.
When the sewage of 14 inner cavity of swirl cylinder is operated normally full of complete machine, by hollow shaft 37 with high-speed rotating impeller 51
Also it is separated by solid-liquid separation with the sewage high-speed rotational in swirl cylinder 14, after moderately opening control valve 57, after separation net
Water flows into hollow shaft 37 from apopore 2 50 and flows downstream into 29 inner cavity of step, then flows into lower water outlet from apopore 3 28
Outside 58 discharge machine of pipe, such as separates water quality and standard is not achieved, sewage pump can be sent into and carry out secondary treatment, handle after opening control valve 57
When outside water purification discharge machine, hypotension in swirl cylinder 14, at this moment the sediment in rotary drum in each detritus tank 19 will be from respectively slagging tap
Hole 20 is discharged to 14 inner cavity of swirl cylinder and carries out secondary centrifuging separation of solid and liquid, and the bed drain purge size of scum hole 20 depends on control valve 57
The displacement of unlatching is how much, thus the present invention multistage dish-style cyclone separator after normal operation, the centrifugal separating effect of sewage
As long as the flow for controlling the draining of control valve 57 reaches setting requirements, when the sediment in swirl cylinder 14 deposits to centainly
After height, time opening automatic emptying machine 26 is sediment outside 25 discharge machine of scum pipe.
Identical knot can be used when in face of dust processing problem on the basis of foregoing description in those skilled in the art
Structure, identical principle, as long as being adjusted to the parameter for being suitable for sewage treatment according to routine techniques to be suitable for the ginseng of dust processing
Number, this specification no longer describe.
Claims (10)
1. a kind of multistage dish-style cyclone separator, including rack are provided with eddy flow and the synchronous solid-liquid point of multistage rotary drum on the rack
From and continuous discharging slag system, eddy flow be separated by solid-liquid separation and regular cinder-discharge system, water inlet system, drainage system, it is characterized in that: described
Eddy flow and the synchronous separation of solid and liquid of multistage rotary drum and continuous discharging slag system, including closed swirl cylinder, eddy flow tube inner chamber, which is provided with, to be turned
Drum assembly, drum assembly are provided centrally with the hollow shaft being fixed to each other with flat key and are and then revolved by the hollow shaft that driving motor drives
Turn, various disks carry out multistage separation of solid and liquid to the sewage for inputting its inner cavity from bottom to up in drum assembly, and the rotary drum is total
The impeller of driving eddy flow tube inner chamber sewage high-speed rotational is provided at lower section.
2. multistage dish-style cyclone separator according to claim 1, it is characterized in that: eddy flow is separated by solid-liquid separation and dreg removing system packet
Closed swirl cylinder is included, upper section is cylindrical tube, lower section is up big and down small conical pipe, and the upper end is provided with upper end cover,
Lower part barrel is provided with mud hole, and the scum pipe and automatic emptying machine that auger is had in pipe are provided with outside mud hole.
3. multistage dish-style cyclone separator according to claim 1, it is characterized in that: water inlet system includes hollow shaft and communicates
The top chock of connection, top chock upper side wall are provided with water inlet one and water inlet pipe, the setting of center hollow shaft corresponding position
There are several inlet openings two, hollow shaft is provided with several inlet openings three above the bottom disk of middle section bottom grade rotary drum.
4. multistage dish-style cyclone separator according to claim 1, it is characterized in that: the upper drainage system of drainage system point and under
Drainage system: upper drainage system includes that top rotary drum center upper end is provided with diversion pipe, and diversion pipe upper end is protruded into top chock
It is connected, top chock lower wall is provided with apopore one and upper water-out pipe；Lower drainage system includes being arranged above impeller
Several apopores two in hollow shaft, the setting of hollow shaft lower port are having in sealing device step, step side wall
It is provided with apopore three and outlet pipe, is provided with control valve on outlet pipe.
5. multistage dish-style cyclone separator according to claim 1, it is characterized in that: being provided with above upper end cover higher than upper axis
The fulcrum bearing of seat is held, lower end is mutually permanently connected with upper end cover bolt, and fulcrum bearing upper end center is provided with centre bore one,
Top is provided with driving motor, and driving motor base and fulcrum bearing are mutually permanently connected with bolt, and the arbor of driving motor is therefrom
Heart hole one extends downwardly into below fulcrum bearing and directly drives hollow shaft operation.
6. multistage dish-style cyclone separator according to claim 1, it is characterized in that: drum assembly is provided in swirl cylinder,
Drum assembly is formed by stacking step by step by bottom grade rotary drum, one to several intermediate rotary drums and top rotary drum.
7. multistage dish-style cyclone separator according to claim 6, it is characterized in that: intermediate rotary drum is less than eddy flow by overall diameter
The outer tube of the cylindrical diameter of cylinder, lower disk, water conservancy diversion disk, one disk, upper disk, pushing off the slag pipe and diameter into several pieces are greater than sky
The inner sleeve of mandrel diameters is constituted, and inner sleeve length setting same as outer tube, inner sleeve and outer tube level height are higher than 30-
45 degree of settings, upper disk lower end is provided with several lower water inlets, upper end is provided with several upper water-out mouths, and lower end setting is fixed on outer
In sleeve upper end next point, upper end setting is fixed in the next point of inner sleeve upper end, and lower disk upper end is provided with several upper water-outs
Mouthful, lower end setting is fixed on outer tube lower end on a bit, and upper end setting is fixed on inner sleeve lower end on a bit, under lower disk
Section is provided with pushing off the slag pipe above, and pushing off the slag pipe is arranged to up big and down small conical pipe, and pushing off the slag pipe upper end is provided with certain apart from outer tube
The slag inlet of width, lower end setting are fixed on lower disk, and pushing off the slag pipe and outer tube and lower tab (s) constitute detritus tank, and middle disk is flat
Row is arranged in upper disk following distance, and lower end is provided with several lower water inlets, and upper end is provided with several upper water-out mouths,
Lower end setting is fixed on pushing off the slag pipe upper end, and water conservancy diversion disk is arranged in parallel among middle disk and lower disk, and lower end is provided with
Several lower water inlets, lower end setting are fixed on pushing off the slag pipe, and the upper end setting is fixed on inner sleeve, and outer tube is in lower disk
Several scum holes are provided on tube wall above.
8. multistage dish-style cyclone separator according to claim 6, it is characterized in that: bottom grade rotary drum is arranged under intermediate rotary drum
Side, bottom disk are not provided with several upper water-out mouths, on the inner sleeve between bottom disk upper end and the water conservancy diversion disk of top
Be provided with several inlet openings three, bottom grade rotary drum in addition to these above-mentioned settings are different, other structures and intermediate rotary drum all
Same design.
9. multistage dish-style cyclone separator according to claim 6, it is characterized in that: the upper disk lower end of top rotary drum does not have
Lower water inlet is set, the diversion pipe that diameter is greater than inner sleeve, the setting of diversion pipe lower end are provided with above the top layer water outlet of the upper end
Be fixed on disk, upper end be upward through centre bore three and sealing device three enter top chock inner cavity and with sealing device three
Together in rotation connection, for top rotary drum in addition to these above-mentioned settings are different, other structures and intermediate rotary drum are all equally identical
Design.
10. multistage dish-style cyclone separator according to claim 1, it is characterized in that: hollow shaft is arranged at swirl cylinder center,
The upper end is upward through and after each casing in drum assembly center that is fixed to each other with flat key, then sequentially passes through upwards from top chock
Sealing device two, sealing device one, upper bearing (metal) and centre bore two, top is by the arbor of shaft coupling and driving motor in transmission
Connection, hollow shaft top is provided with upper plug head, be provided in the hollow shaft between sealing device one and sealing device two it is several into
Water hole two is provided with and its phase in the hollow shaft of three position of inlet opening being arranged on the bottom disk upper end inner sleeve of bottom grade rotary drum
With the inlet opening three that communicates, be provided with lower end cap below inlet opening three in hollow shaft, be provided on tube wall under lower end cap it is several go out
Water hole two is provided with the impeller with several blades, impeller and hollow shaft on two lower section outer tube wall of apopore and fixes company with flat key
It connects, hollow shaft lower end sequentially passes through centre bore four, sealing device four, lower bearing and sealing device five and enters water outlet in step
Three top of hole.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910051033.1A CN109675727A (en) | 2019-01-14 | 2019-01-14 | Multistage dish-style cyclone separator |
| PCT/CN2019/114738 WO2020147375A1 (en) | 2019-01-14 | 2019-10-31 | Multi-stage disk-type solid-liquid separation or dust removal machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910051033.1A CN109675727A (en) | 2019-01-14 | 2019-01-14 | Multistage dish-style cyclone separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109675727A true CN109675727A (en) | 2019-04-26 |
Family
ID=66193567
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910051033.1A Pending CN109675727A (en) | 2019-01-14 | 2019-01-14 | Multistage dish-style cyclone separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109675727A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2020147375A1 (en) * | 2019-01-14 | 2020-07-23 | 沈智奇 | Multi-stage disk-type solid-liquid separation or dust removal machine |
| CN114894935A (en) * | 2022-05-23 | 2022-08-12 | 湖南省长康实业有限责任公司 | Sesame oil adulteration prevention rapid detection method and device |
| CN116947159A (en) * | 2023-09-20 | 2023-10-27 | 山西绿景环保科技工程有限公司 | Efficient sand-water separation equipment |
| CN117839881A (en) * | 2024-03-07 | 2024-04-09 | 山东深海生物科技股份有限公司 | Fermentation liquor refining device for producing 5-aminolevulinic acid by synthetic biological method |
-
2019
- 2019-01-14 CN CN201910051033.1A patent/CN109675727A/en active Pending
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2020147375A1 (en) * | 2019-01-14 | 2020-07-23 | 沈智奇 | Multi-stage disk-type solid-liquid separation or dust removal machine |
| CN114894935A (en) * | 2022-05-23 | 2022-08-12 | 湖南省长康实业有限责任公司 | Sesame oil adulteration prevention rapid detection method and device |
| CN114894935B (en) * | 2022-05-23 | 2023-11-21 | 湖南省长康实业有限责任公司 | Sesame oil adulteration prevention rapid detection method and device |
| CN116947159A (en) * | 2023-09-20 | 2023-10-27 | 山西绿景环保科技工程有限公司 | Efficient sand-water separation equipment |
| CN116947159B (en) * | 2023-09-20 | 2023-12-12 | 山西绿景环保科技工程有限公司 | Efficient sand-water separation equipment |
| CN117839881A (en) * | 2024-03-07 | 2024-04-09 | 山东深海生物科技股份有限公司 | Fermentation liquor refining device for producing 5-aminolevulinic acid by synthetic biological method |
| CN117839881B (en) * | 2024-03-07 | 2024-05-03 | 山东深海生物科技股份有限公司 | Fermentation liquor refining device for producing 5-aminolevulinic acid by synthetic biological method |
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