CN105864213A - Hydraulic system filtering method adopting electrification, separation, adsorption and centrifugation - Google Patents

Hydraulic system filtering method adopting electrification, separation, adsorption and centrifugation Download PDF

Info

Publication number
CN105864213A
CN105864213A CN201610315811.XA CN201610315811A CN105864213A CN 105864213 A CN105864213 A CN 105864213A CN 201610315811 A CN201610315811 A CN 201610315811A CN 105864213 A CN105864213 A CN 105864213A
Authority
CN
China
Prior art keywords
module
oil
solenoid
inner core
separation
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.)
Pending
Application number
CN201610315811.XA
Other languages
Chinese (zh)
Inventor
王雅莉
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN201610315811.XA priority Critical patent/CN105864213A/en
Publication of CN105864213A publication Critical patent/CN105864213A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F15FLUID-PRESSURE ACTUATORS; HYDRAULICS OR PNEUMATICS IN GENERAL
    • F15BSYSTEMS ACTING BY MEANS OF FLUIDS IN GENERAL; FLUID-PRESSURE ACTUATORS, e.g. SERVOMOTORS; DETAILS OF FLUID-PRESSURE SYSTEMS, NOT OTHERWISE PROVIDED FOR
    • F15B21/00Common features of fluid actuator systems; Fluid-pressure actuator systems or details thereof, not covered by any other group of this subclass
    • F15B21/04Special measures taken in connection with the properties of the fluid
    • F15B21/041Removal or measurement of solid or liquid contamination, e.g. filtering

Abstract

The invention relates to a hydraulic system filtering method adopting electrification, separation, adsorption and centrifugation. Separation of solid particles is achieved through a U-shaped particle separating module, the solid particles in oil are made to move to the pipe wall, and at an outlet of the U-shaped particle separating module, the oil which is rich in solid particle and located near the pipe wall enters an oil return barrel through an oil return barrel module oil inlet pipe and then flows back into an oil tank, and the oil which contains trace of small-diameter particles and is located in the pipe center enters an inner barrel through an inner barrel oil inlet pipe to be subjected to high-precision filtering, so that the service life of a filter element is prolonged, and filtering cost is lowered; the oil entering the inner barrel oil inlet pipe flows into a spiral flow channel of the inner barrel in a tangential inflow mode, the inner barrel wall is used as the filter element, filter liquor flows by tightly attaching the filter element under the effect of centrifugal force, the filter liquor quickly flows in parallel to the surface of the filter element, and the filtered hydraulic oil flows out to an outer barrel in the direction perpendicular to the surface of the filter element; polluting particles deposited at the bottom of the inner barrel can be regularly discharged to the oil return barrel through an electrically operated check valve, and therefore the service life of the filter element is prolonged.

Description

A kind of hydraulic system filter method using electrification, separating, adsorb and be centrifuged
[technical field]
The present invention relates to a kind of hydraulic oil filter, be specifically related to a kind of use electrification, the hydraulic pressure separating, adsorb and being centrifuged System filter method, belongs to technical field of hydraulic equipment.
[background technology]
Statistics both domestic and external show, the fault of hydraulic system about 70%~85% is owing to oil contamination causes 's.Solid particle is then the pollutant the most universal in oil contamination, damaging effect is maximum.The liquid caused by solid grain contamination The pressure system failure accounts for the 70% of gross contamination fault.In particulate pollutant in hydraulic system oil liquid, metal filings accounting exists Between 20%~70%.Adopt an effective measure the solid grain contamination filtering in fluid, be the pass of Pollution Control in Hydraulic System Key, is also the Reliable guarantee of system safety operation.
Filter is the key element that hydraulic system filters solid grain contamination.Solid particle pollution in hydraulic oil Thing, outside the precipitable a part of larger particles of oil removal box, filters mainly by oil-filtering apparatus.Especially high pressure filtering device, mainly It is used for filtering the hydraulic oil of flow direction control valve and hydraulic cylinder, to protect the Hydraulic Elements of this kind of contamination resistance difference, therefore to liquid The cleannes of force feed require higher.
But, the high pressure filter that existing hydraulic system uses has the disadvantage that (1) all kinds of Hydraulic Elements are to fluid Cleannes require different, the size of the solid particle in fluid is the most different, for this need in hydraulic system Diverse location install multiple dissimilar wave filter, thus bring cost and install complexity problem;(2) hydraulic system In filter mainly use cake filtration mode, during filtration filtrate be perpendicular to filter element surface flowing, trapped solid Microgranule forms filter cake progressive additive, and the rate of filtration is gradually reduced the most therewith until filtrate stops flowing out, and reduces filter element Service life.
Therefore, for solving above-mentioned technical problem, the employing of a kind of innovation of necessary offer electrifies, separate, adsorb and from The hydraulic system filter method of the heart, to overcome described defect of the prior art.
[summary of the invention]
For solving above-mentioned technical problem, it is an object of the invention to provide a kind of strainability good, adaptability and integration Height, service life length the employing hydraulic system filter method that electrifies, separate, adsorb and be centrifuged.
For achieving the above object, the technical scheme that the present invention takes is: a kind of uses electrification, separate, adsorb and be centrifuged Hydraulic system filter method, it uses a kind of filter, this filter include base plate, U-shaped separation of particles module, oil returning tube, Inner core, helical flow path, filter element, outer barrel and end cap;Wherein, described U-shaped separation of particles module, oil returning tube, outer barrel are sequentially placed into On base plate;Described U-shaped separation of particles module is provided with a hydraulic oil inlet, and it includes a U-tube, and U-tube is sequentially installed with Electrification module, separation module, the first adsorption module, mechanical centrifugal module, the second adsorption module and demagnetization module;Described U-shaped micro- The top of grain separation module and oil returning tube is connected by an oil returning tube oil inlet pipe;Described inner core is placed in outer barrel, and it is by a top If plate and bolt stem are installed on end cap;Described helical flow path is contained in inner core, logical between itself and U-shaped separation of particles module Cross an inner core oil inlet pipe to connect;Described inner core oil inlet pipe is positioned at oil returning tube oil inlet pipe, and extends into U-shaped separation of particles module Central authorities, its diameter is less than oil returning tube oil inlet pipe diameter, and is coaxially disposed with oil returning tube oil inlet pipe;Described filter element is arranged on inner core On inwall, its precision is 1-5 micron;The bottom of said tub is provided with a hydraulic oil oil-out;
It comprises the steps:
1), backflow force feed enters the electrification module of U-shaped separation of particles module, makes the particulate matter in fluid charged, it After deliver to separation module;
2), making the charged corpuscle in fluid be polymerized to tube wall under the effect of external force by segregation apparatus, oil return afterwards is sent To the first adsorbent equipment;
3), by the magnetic polymeric microgranule in the first adsorption module absorption oil return, mechanical centrifugal module is delivered in oil return afterwards;
4), magnetic microparticles not to be adsorbed is centrifuged by mechanical centrifugal module, and the second adsorption module is delivered in oil return afterwards;
5), the magnetic polymeric microgranule in the second adsorption module second adsorption oil return;
6), magnetic particle magnetic is eliminated by demagnetization module;
7), the fluid of the most U-shaped separation of particles module near-wall refluxes after entering oil returning tube by oil returning tube oil inlet pipe To fuel tank, the fluid of the pipeline center containing trace small particle microgranule then enters inner core by inner core oil inlet pipe and carries out high-precision spending Filter;
8), the fluid carrying small particle microgranule flows into the helical flow path of inner core in the way of tangential influent stream, and fluid is centrifugal It is close to filter core flow under the effect of power, and carries out high-precision filtration;
9), the fluid after high-precision filtration enters urceolus, and is discharged by the hydraulic oil oil-out bottom urceolus.
The hydraulic system filter method that the employing of the present invention electrifies, separates, adsorbs and is centrifuged is further: described electrification Module includes some electrodes and an electrode controller;Described some electrodes are installed on the first oil return pipe, and it is respectively connecting to Electrode controller.
The hydraulic system filter method that the employing of the present invention electrifies, separates, adsorbs and is centrifuged is further: described separation Module uses uniform magnetic field separation module, and this uniform magnetic field separation module includes that aluminum matter pipeline, two magnetic poles and magnetic pole control Device;Wherein, said two magnetic pole is separately positioned on aluminum matter pipeline, the opposite polarity of these two magnetic poles, and in being oppositely arranged;Institute State two magnetic poles to be respectively and electrically connected on magnetic pole controller.
The hydraulic system filter method that the employing of the present invention electrifies, separates, adsorbs and is centrifuged is further: described separation Module uses rotating excitation field separation module, and this rotating excitation field separation module includes aluminum matter pipeline, iron shell, three-phase symmetric winding And three-phase symmetrical current module;Described three-phase symmetric winding is wound on outside aluminum matter pipeline;Described iron shell is coated on aluminum matter pipe On road;Described three-phase symmetrical current module connects described three-phase symmetric winding.
The hydraulic system filter method that the employing of the present invention electrifies, separates, adsorbs and is centrifuged is further: described separation Module use helical pipe magnetic field separation module, this helical pipe magnetic field separation module include aluminum matter helical pipe, solenoid with And solenoid control circuit;Wherein, described aluminum matter helical pipe is arranged in solenoid;Described solenoid and solenoid control electricity Road is electrically connected with.
The hydraulic system filter method that the employing of the present invention electrifies, separates, adsorbs and is centrifuged is further: described first Adsorption module and second is inhaled adsorption module and is used homopolarity adjacent type absorbing ring, and this homopolarity adjacent type absorbing ring includes aluminium ring shape pipe Road, forward solenoid, reverse solenoid and irony magnetic conduction cap;Described forward solenoid and reverse solenoid are respectively arranged in aluminum In matter circulating line, both are connected with electric current in opposite direction so that forward solenoid and reverse solenoid adjacent produce the same sex Magnetic pole;Described irony magnetic conduction cap is arranged on the inwall of aluminium ring shape pipeline, and it is positioned at forward solenoid and reverse solenoid phase At Lin and forward solenoid and the intermediate point of reverse solenoid axis.
The hydraulic system filter method that the employing of the present invention electrifies, separates, adsorbs and is centrifuged is further: described first Adsorption module and second is inhaled adsorption module and is used the homopolarity adjacent type absorbing ring of charged hammer, the adjacent type of homopolarity of this charged hammer Absorbing ring includes aluminium ring shape pipeline, forward solenoid, reverse solenoid, irony magnetic conduction cap, dividing plate, electric shock hammer and electromagnetism Ferrum;Described forward solenoid and reverse solenoid are respectively arranged in aluminium ring shape pipeline, and both are connected with electric current in opposite direction, Forward solenoid and reverse solenoid adjacent is made to produce like pole;Described irony magnetic conduction cap is arranged in aluminium ring shape pipeline Inwall on, it is positioned at forward solenoid and reverse solenoid adjacent and forward solenoid and reverse solenoid axis Intermediate point;Described dividing plate is between forward solenoid and reverse solenoid;Described electric shock hammer and electric magnet are between dividing plate; Described electric magnet connects and can promote electric shock hammer, makes electric shock hammer tap aluminium ring shape inner-walls of duct.
The hydraulic system filter method that the employing of the present invention electrifies, separates, adsorbs and is centrifuged is further: described machinery Centrifugal module uses eddy flow to be centrifuged module;Described eddy flow be centrifuged module include eddy flow tube wall, the first flow deflector, the second flow deflector, Motor and flow transducer;Wherein, described first flow deflector is provided with 3, and these 3 first flow deflectors are along tube wall inner periphery Being uniformly distributed every 120 °, its laying angle is set to 18 °;Described second flow deflector and the first flow deflector structure are identical, and it is arranged on After one flow deflector, and and the first flow deflector stagger 60 ° and be connected in tube wall, its laying angle is set to 36 DEG C;Described first flow deflector Long limit be connected with tube wall, minor face along tube wall axis extend;Its leading edge frustrates into obtuse, and trailing edge is processed into wing, and its height is 0.4 times of tube wall diameter, 1.8 times of a length of tube wall diameter;Described motor connects and drives the first flow deflector and second Flow deflector, to regulate laying angle;Described flow transducer is arranged on the central authorities in tube wall.
The hydraulic system filter method that the employing of the present invention electrifies, separates, adsorbs and is centrifuged is further: described oil return The bottom of cylinder is provided with an overflow valve, is provided with an automatically controlled set screw bottom this overflow valve;Described overflow valve is provided with an oil drain out, This oil drain out is connected to a fuel tank by pipeline.
The hydraulic system filter method that the employing of the present invention electrifies, separates, adsorbs and is centrifuged is also: the end of described inner core Portion is rounding mesa-shaped, and it is connected by an inner core oil exit pipe and oil returning tube, and inner core oil exit pipe is provided with an automatically controlled check-valves;Described The center upright of inner core is provided with a hollow cylinder, hollow cylinder be arranged over pressure difference indicator, this pressure difference indicator is installed on On end cap;Described inner core oil inlet pipe and the tangent connection of helical flow path.
Compared with prior art, there is advantages that
1. hydraulic oil realizes the separation of solid particle in U-shaped separation of particles module, makes the solid particle in fluid to pipe Wall moves, and at U-shaped separation of particles module outlet, the fluid rich in the near-wall of solid particle is entered by oil returning tube oil inlet pipe Being back to fuel tank after entering oil returning tube, the only fluid of the pipeline center containing trace small particle microgranule is then entered by inner core oil inlet pipe Inner core carries out high-precision filtration, improves the service life of filter element, reduces filtering cost and complexity;Enter inner core oil inlet pipe Fluid in the way of tangential influent stream, flow into the helical flow path of inner core, inner tube wall is filter element, then filtrate is under the influence of centrifugal force Being close to filter core flow, filtrate is parallel to the surface of filter element and quickly flows, and the hydraulic oil after filtration is then perpendicular to cartridge surface direction Flowing out to urceolus, the microgranule of cartridge surface is implemented to sweep stream effect by this cross flow filter type, it is suppressed that the increasing of filter cake thickness Add, be deposited on the pollution granule bottom inner core and regularly can be discharged to oil returning tube by automatically controlled check-valves, thus improve filter element and use Life-span.
2. by controlling the temperature of hydraulic oil and making the particulate matter charged polymeric in fluid to electrode applying voltage, and promote Make colloidal particles decompose to melt;Efficient absorption is formed by adsorption module;Mechanical centrifugal is utilized " to be divided by the molecule in fluid From " and gather near-wall, capture molecule with adsorbent equipment;Avoid endangering to residual particles demagnetization by degaussing gear Hydraulic Elements, so that solid particle is gathered into bulky grain and moves to near-wall in fluid.
3. the generation of non-uniform magnetic-field that magnetization needs, need multipair forward and reverse coil to and pass through different size of electric current, And current values can numeral set online.
[accompanying drawing explanation]
Fig. 1 is the structural representation of the hydraulic system filter that the employing of the present invention electrifies, separates, adsorbs and is centrifuged.
Fig. 2 is the schematic diagram of the U-shaped separation of particles module in Fig. 1.
Fig. 3 is the structural representation of the electrification module in Fig. 2.
Fig. 4 be the separation module in Fig. 2 be the structural representation of uniform magnetic field separation module.
Fig. 5 be the separation module in Fig. 2 be the structural representation of rotating excitation field separation module.
Fig. 6 be the separation module in Fig. 2 be the structural representation of helical pipe magnetic field separation module.
Fig. 7 is the structural representation that the first adsorption module (the second adsorption module) is homopolarity adjacent type absorbing ring in Fig. 2.
Fig. 8 is the homopolarity adjacent type absorbing ring that the first adsorption module (the second adsorption module) is charged hammer in Fig. 2 Structural representation.
Fig. 9 is the horizontal schematic diagram of the mechanical centrifugal module of Fig. 2.
Figure 10 is the radial direction schematic diagram of the mechanical centrifugal module of Fig. 2.
[detailed description of the invention]
Referring to shown in Figure of description 1 to accompanying drawing 10, the present invention is a kind of to use electrification, separate, adsorb and be centrifuged Hydraulic system filter, its by base plate 6, U-shaped separation of particles module 3, oil returning tube 7, inner core 15, helical flow path 17, filter element 18, Several parts compositions such as outer barrel 19 and end cap 25.
Wherein, described U-shaped separation of particles module 2, oil returning tube 7, outer barrel 19 are sequentially placed on base plate 6.Described U-shaped microgranule divides Being provided with one for being passed through the hydraulic oil inlet 1 of hydraulic oil from module 3, it includes a U-tube 31, and U-tube 31 is installed successively There are electrification module 32, separation module the 33, first adsorption module 34, the 36, second adsorption module 37 and the demagnetization of mechanical centrifugal module Module 35.
Described electrification module 32 makes the metallic particles material in fluid charged, and it is by some electrodes 321 and an electrode control Device 322 processed forms.Described some electrodes 321 are installed in U-tube 31, and it is respectively connecting to electrode controller 252.Described electrode Controller 322 is electrically connected with and applies voltage to electrode 321, makes the particulate matter in fluid charged.
Described separation module 33 makes poly-being incorporated under centrifugal action of particle charge that quality is bigger get rid of to cavity wall, and it can be adopted By uniform magnetic field separation module, rotating excitation field separation module or helical pipe magnetic field separation module.
When described separation module 33 uses uniform magnetic field separation module, its by 331, two magnetic poles 332 of aluminum matter pipeline and Magnetic pole controller 333 forms.Wherein, said two magnetic pole 332 is separately positioned on aluminum matter pipeline 331, these two magnetic poles 332 Opposite polarity, and in being oppositely arranged.Said two magnetic pole 332 is respectively and electrically connected on magnetic pole controller 333.
The design principle of described uniform magnetic field separation module 33 is as follows: charged particle flows into uniform magnetic field with speed V and separates Module 33, two magnetic poles 332 of uniform magnetic field separation module 33 produce the uniform magnetic field vertical with speed V direction, according to left hand Rule, then charged particle in uniform magnetic field separation module 33 by being perpendicular to the Loulun magnetism of velocity attitude and magnetic direction Effect, this power does not change the speed of charged particle, and it only changes the direction of motion of charged particle, makes charged particle at the work of this power With the lower vessel wall motion to aluminum matter pipeline 331, so that the granule in fluid " separates " out from fluid, assemble to tube wall, It is easy to subsequent adsorbtion capture.Owing to fluid has certain viscosity, granule during vessel wall motion also by viscous drag Effect.In order to ensure separating effect, need to regulate magnetic field intensity B and make the granule of distance tube wall farthest can be at the work of separation module Moving at tube wall within the time, quantitative analysis is as follows:
Assuming that particle mass is m, speed is v, and magnetic field intensity is B, and carried charge is q, a diameter of D of separation module, length For L, then:
Acting on the Loulun magnetism on charged particle is
Fl=qvB
The viscous drag that charged particle is subject to is
Fd=6 π η r v
The radius v charged particle movement velocity of η hydraulic pressure oil viscosity r charged particle
It not general, it is assumed that the granule in fluid has reached stable state when entering separation module, then charged particle is by dividing Can approximate from the time of module and represent with following formula
t 1 = L v
The charged particle of distance tube wall farthest moves to the time t at tube wall2Can be solved by following formula
D = m g q B - 6 π η r t - ( m g q B - 6 π η r ) 2 ( 1 - e - q B - 6 π η r m t )
Regulation B so that t1>t2, i.e. can reach separating effect.
When described separation module 33 uses rotating excitation field separation module, it is by aluminum matter pipeline 331, iron shell 334, three-phase The parts compositions such as symmetric winding 335 and three-phase symmetrical current module 336.Described three-phase symmetric winding 335 is wound on aluminum matter pipeline Outside 331.Described iron shell 334 is coated on aluminum matter pipeline 335.Described three-phase symmetrical current module 336 connects described three-phase Symmetric winding 335.
The design principle of described rotating excitation field separation module 33 is as follows: charged particle flows into rotating excitation field with speed V and separates Module 33, three-phase symmetrical current module 336 makes to flow through in three-phase symmetric winding 335 three-phase symmetrical electric current, and this electric current is at aluminum matter pipe Producing rotating excitation field in road 331, charged particle is subject to be perpendicular to the Lip river of velocity attitude and magnetic direction under rotating excitation field effect The effect of logical sequence magnetic force, this power does not change the speed of charged particle, and it only changes the direction of motion of charged particle, makes charged particle exist Spirally advance under the effect of this power, and to vessel wall motion.Reasonable adjusting magnetic field intensity can make the granule in fluid from oil Liquid " separates " out, is gathered in near-wall, it is simple to subsequent adsorbtion captures.Owing to fluid has certain viscosity, granule to Also acted on by viscous drag during vessel wall motion.In order to ensure separating effect, need to make on aluminum matter pipeline 331 axis Microgranule can move at tube wall within the action time of separation module, and quantitative analysis is as follows:
Assuming that particle mass is m, speed is v, and magnetic field intensity is B, and carried charge is q, a diameter of D of separation module, length For L, then:
Acting on the Loulun magnetism on charged particle is
Fl=qvB
The viscous drag that charged particle is subject to is
Fd=6 π η r v
The radius v charged particle movement velocity of η hydraulic pressure oil viscosity r charged particle
Assuming that the granule in fluid has reached stable state, the then charged particle time by separation module when entering separation module Can approximate and represent with following formula
t 1 = L v
Charged particle on conduit axis moves to the time t at tube wall2Can be solved by following formula
D 2 = m g q B - 6 π η r t - ( m g q B - 6 π η r ) 2 ( 1 - e - q B - 6 π η r m t )
Regulation B so that t1>t2, i.e. can reach separating effect.
When described separation module 33 uses helical pipe magnetic field separation module, it is by aluminum matter helical pipe 338, solenoid 339 and solenoid control circuit 336 form.Wherein, described aluminum matter helical pipe 338 is arranged in solenoid 339.Described spiral shell Spool 339 and solenoid control circuit 336 are electrically connected with.Described solenoid control circuit 336 is electrically connected to ECU3.
The design principle of described helical pipe magnetic field separation module 33 is as follows: carry the fluid of charged particle along aluminum matter spiral Pipeline 338 advances, thus produces at pipeline exit and have the eddy flow of certain spin direction, the charged particle of heavier mass along with Fluid rotates, and produces the radial motion to tube wall under the influence of centrifugal force;Simultaneously as the entrance of aluminum matter helical pipe 338 Direction is vertical with the axial magnetic field direction of energization solenoid 339, and the charged particle entering aluminum matter helical pipe 338 with speed v is subject to To the effect of Loulun magnetism, direction is perpendicular to magnetic direction and the Way in of aluminum matter helical pipe 338.Loulun magnetism makes charged Granule is spinned forward travel in pipeline, owing to the Way in of aluminum matter helical pipe 338 and magnetic direction are close to vertical, and band Electricity granule mainly rotates in a circumferential direction motion, and fluid is the most unaffected, thus realizes granule " separation " from fluid, in order to reality The now absorption to granule.For ensureing " separation " effect, need to make the microgranule on aluminum matter conduit axis can be in the effect of separation module Moving in time at tube wall, quantitative analysis is as follows:
Assuming that particle mass is m, speed is v, and carried charge is q, a diameter of D of aluminum matter helical pipe, aluminum matter helical pipe The number of turn be n, the angle in the Way in of aluminum matter helical pipe and the axial magnetic field direction of energization solenoid is θ, solenoid circle Number is N, and electric current is I, and magnetic field intensity is B, and permeability of vacuum is μ0, then:
Acting on the Loulun magnetism on charged particle is
Fl=qvB
The viscous drag that charged particle is subject to is
Fd=6 π η r v
The radius v charged particle movement velocity of η hydraulic pressure oil viscosity r charged particle
Charged particle can be approximated by the time of separation module and represent with following formula
t 1 = q B n D 2 π m v c o s θ
Charged particle on conduit axis moves to the time t at tube wall2Can be solved by following formula
D 2 = v s i n θ m q B + 6 π η r ( 1 - e - q B + 6 π η r m t )
Magnetic field intensity within solenoid can be approximately constant
I = B μ N
Regulation I so that t1>t2, i.e. can reach separating effect.
Described first adsorption module 34 is for adsorbing the big microgranule of magnetic polymeric after separated module 33 separates, and it can use Homopolarity adjacent type absorbing ring, this homopolarity adjacent type absorbing ring is by aluminium ring shape pipeline 341, forward solenoid 342, reverse solenoid 343 and the parts such as irony magnetic conduction cap 344 composition.Wherein, described forward solenoid 342 and reverse solenoid 343 are respectively arranged In aluminium ring shape pipeline 341, both are connected with electric current in opposite direction so that forward solenoid 342 and reverse solenoid 343 are adjacent Place produces like pole.Described irony magnetic conduction cap 344 is arranged on the inwall of aluminium ring shape pipeline 341, and it is positioned at forward helical Pipe 342 and reverse solenoid 343 adjacent and forward solenoid 342 and the intermediate point of reverse solenoid 343 axis.
The design principle of described homopolarity adjacent type absorbing ring is as follows: energising forward solenoid 342, reverse solenoid 343, phase Adjacent forward solenoid 342, reverse solenoid 343 are connected with electric current in opposite direction so that forward solenoid 342, reverse helical Pipe 343 adjacent produces like pole;Meanwhile, aluminium ring shape pipeline 341 can improve magnetic circuit, strengthens the magnetic field at inner-walls of duct Intensity, strengthens the irony magnetic conduction cap 344 capture absorbability to granule.Each forward solenoid 342, reverse solenoid 343 electric current Can be different with concentration and change, to obtain optimal adsorption performance according to the size of granule.
Further, described first adsorption module 34 may be used without the homopolarity adjacent type absorbing ring of charged hammer, and this is charged The homopolarity adjacent type absorbing ring of hammer is by aluminium ring shape pipeline 341, forward solenoid 342, reverse solenoid 343, irony magnetic conduction The parts compositions such as cap 344, dividing plate 345, electric shock hammer 346 and electric magnet 347.Wherein, described forward solenoid 342 and reverse spiral shell Spool 343 is respectively arranged in aluminium ring shape pipeline 341, and both are connected with electric current in opposite direction so that forward solenoid 342 is with anti- Like pole is produced to solenoid 343 adjacent.Described irony magnetic conduction cap 344 is arranged on the inwall of aluminium ring shape pipeline 341, It is positioned at forward solenoid 342 and reverse solenoid 343 adjacent and forward solenoid 342 and reverse solenoid 343 axis Intermediate point.Described electric shock hammer 346 and electric magnet 347 are between dividing plate 345.Described electric magnet 347 connects and can promote electricity Hammer 346, makes electric shock hammer 346 percussion aluminium ring shape pipeline 342 inwall.
The design principle of the homopolarity adjacent type absorbing ring of described charged hammer is as follows: energising forward solenoid 342, reverse spiral shell Spool 343, adjacent forward solenoid 342, reverse solenoid 343 are connected with electric current in opposite direction so that forward solenoid 342, reverse solenoid 343 adjacent produces like pole;Meanwhile, aluminium ring shape pipeline 341 can improve magnetic circuit, strengthens pipeline Magnetic field intensity at inwall, strengthens the irony magnetic conduction cap 344 capture absorbability to granule.Each forward solenoid 342, reverse spiral shell Spool 343 electric current can be different with concentration and change, to obtain optimal adsorption performance according to the size of granule.And by electric shock The setting of hammer 346, prevents granule bulk deposition at irony magnetic conduction cap 344, affects adsorption effect.Now, by electric magnet 347 Control the inwall of electric shock hammer 346 percussion pipeline 341 so that adsorbed granule scatter to both sides.Meanwhile, pipeline is being cleaned When 341, the percussion of electric shock hammer 346 can also improve cleaning performance.
Described first adsorption module 34 is designed to U-shaped, and when fluid enters U-shaped absorption pipeline, granule is at gravity, centrifugal force Effect under, to side, tube wall moves, and plus magnetic field force effect, moves radially speed and accelerates, and the efficiency of granular absorption is able to Improve;Fluid leave U-shaped absorption pipeline rise time, transport so that the direction that granule is diagonally lower gravity and magnetic field force with joint efforts Dynamic, extend the numerical density time, improve the efficiency of granular absorption.
Described mechanical centrifugal module 36 makes the magnetization aggregated particles not to be adsorbed in fluid be thrown toward under the action of the centrifugal Tube wall.Described mechanical centrifugal module 36 selects eddy flow to be centrifuged module 36, and this eddy flow is centrifuged module 36 and uses the mode of energy loss, Its design principle is as follows: arranges the flow deflector of the distortion of certain altitude and length in the duct, and makes blade face tangent line become with axis Certain angle, can make fluid produce spiral flow in pipes because pipe flow border changes, and this spiral flow can be analyzed to the week around pipe axle To flowing and axial straight flowing, the particulate matter carried in fluid produces off-axis alignment heart screw.This eddy flow centrifugal device 36 is several by eddy flow tube wall the 361, first flow deflector the 362, second flow deflector 363, motor 364 and flow transducer 365 etc. Part composition.
Wherein, described first flow deflector 362 is provided with 3, these 3 first flow deflectors 362 along tube wall 361 inner periphery every 120 ° Being uniformly distributed, its laying angle (angle between the first flow deflector 362 and eddy flow tube wall 361) is set to 18 °, optimal tangential to ensure Flowing.Described second flow deflector 363 is identical with the first flow deflector 362 structure, after it is arranged on the first flow deflector 362, and and the One flow deflector 362 staggers 60 ° and is connected in tube wall 361, and its laying angle is set to 36 DEG C, is used for reducing resistance and strengthening circumferential flow Intensity.It addition, the 3rd or more flow deflector can be arranged the most again according to actual separation effect, laying angle gradually increases.Institute State motor 364 connect and drive the first flow deflector 362 and the second flow deflector 363, to regulate laying angle, thus can obtain more Good centrifugal effect, knows and makes flow deflector 362,363 adapt to different operating modes.Described flow transducer 365 is arranged on tube wall 361 Interior central authorities, by the numerical analysis cyclonic separation effect of reading flow quantity sensor 365, and control motor 364, step accordingly Enter motor 364 and regulate the laying angle of each flow deflector 362,363, to obtain more separating effect.
Described second adsorbent equipment 37 is identical with described first adsorbent equipment 34 structure, and function is the most identical with the mechanism of action, It can adsorb the granule separated through mechanical centrifugal module 36 further.
Described demagnetization module 35 gives magnetized particles demagnetization, prevents residual magnetism microgranule from entering hydraulic pressure by oil returning tube oil inlet pipe Loop, sensitive to pollution Hydraulic Elements cause damage.
The top of described U-shaped separation of particles module 3 and oil returning tube 7 is connected by an oil returning tube oil inlet pipe 22;By U-shaped micro- After grain separation module 3 processes, the fluid of U-tube 31 near-wall, rich in aggregated particles, is entered back by oil returning tube oil inlet pipe 22 It is back to fuel tank after oil cylinder 7.
The bottom of described oil returning tube 7 is provided with an overflow valve 8, is provided with an automatically controlled set screw 9 bottom this overflow valve 8;Described Overflow valve 8 is provided with an oil drain out 10, and this oil drain out 10 is connected to a fuel tank 11 by pipeline 20.
Described inner core 15 is placed in outer barrel 19, if it is installed on end cap 25 by a top board 13 and bolt stem 21.Institute State helical flow path 17 to be contained in inner core 15, connected by an inner core oil inlet pipe 12 between itself and U-shaped separation of particles module 3, tool Saying of body, described inner core oil inlet pipe 12 and the tangent connection of helical flow path 17.The fluid of the U-tube 31 pipeline center only granule Han trace Footpath microgranule, enters inner core 15 by inner core oil inlet pipe 12 and realizes high-precision filtration, thus realize solid particle and separate.Further , described inner core oil inlet pipe 12 is positioned at oil returning tube oil inlet pipe 22, and extends into the central authorities of U-shaped separation of particles module 3, its diameter Less than oil returning tube oil inlet pipe 22 diameter, and it is coaxially disposed with oil returning tube oil inlet pipe 22.
Further, the bottom of described inner core 15 is rounding mesa-shaped, and it is connected by an inner core oil exit pipe 23 and oil returning tube 7 Connecing, inner core oil exit pipe 23 is provided with an automatically controlled check-valves 24.The center upright of described inner core 15 is provided with a hollow cylinder 16, hollow Cylinder 16 be arranged over pressure difference indicator 14, this pressure difference indicator 14 is installed on end cap 25.
Described filter element 18 is arranged on the inwall of inner core 15, and its precision is 1-5 micron.
The bottom of said tub 19 is provided with a hydraulic oil oil-out 5, the hydraulic oil that will have been filtered by hydraulic oil oil-out 5 Discharge.
In the present invention, owing to U-shaped separation of particles module 3 is to solid particle separation of polymeric effect in fluid, at U-shaped microgranule In the fluid in separation module 3 exit, the fluid at the center only small particle microgranule Han trace, this part fluid is from inner core oil inlet pipe 12 It is flowed into inner core 15 and carries out high-precision filtration;And the fluid of near-wall is rich in aggregated particles, this part fluid passes through oil returning tube Oil inlet pipe 22 enters oil returning tube 7, then flows back to fuel tank 11 through the oil drain out 10 of overflow valve 8, thus realizes solid particle by particle Footpath shunting filtering.Herein, oil returning tube 7 and overflow valve 8 serve aforesaid macrofiltration, thus save filter number, fall Low system cost and complexity.The automatically controlled set screw 9 of overflow valve 8 is used for regulating oil pressure relief, is adjusted to by its pressure slightly Less than pressure at filtering outlet, to ensure inner core 15 filtering traffic.
It addition, traditional filter mainly uses cake filtration mode, during filtration, filtrate is perpendicular to filter element surface stream Dynamic, trapped solid particle forms filter cake progressive additive, and the rate of filtration is gradually reduced the most therewith, until filtrate stops stream Go out, reduce the service life of filter element.In this present invention, carry the filtrate of small particle microgranule from inner core oil inlet pipe 12 Flowing into the helical flow path 17 of inner core 15 in the way of tangential influent stream, inner core 15 wall of helical duct 17 side is high-precision filter element 18, filtrate is close to filter element 18 surface under the influence of centrifugal force, and filtrate is parallel to the surface of filter element 18 and quickly flows, after filtration Hydraulic oil is then perpendicular to filter element 18 surface direction and flows out to urceolus 19, and the direction of the two flowing is orthogonal staggered, therefore claims it Filter for cross flow.The quickly flowing of filtrate is applied with shearing to the microgranule being gathered in filter element 18 surface and sweeps stream effect, thus presses down Having made the increase of filter cake thickness so that rate of filtration near constant, filter pressure also will not raise with the passing of time, filter element Service life thus increase substantially.Along with the accumulation of filtration time, it is deposited on the pollution granule bottom inner core 15 inverted round stage Being stepped up, the rate of filtration slowly declines, and in inner core 15, unfiltered filtrate rises along the hollow cylinder 16 at center, now, and pressure Difference indicator 14 works, and monitors the change of its pressure, that is the stopping state of filter element 18 bottom inner core 15, if exceeding threshold value, then Regulate automatically controlled set screw 9 and reduce oil pressure relief, and open check-valves 24 simultaneously, make bottom inner core 15 containing more pollution granule Filtrate is discharged to oil returning tube 7 by inner core oil exit pipe 23 under differential pressure action, it is to avoid bottom, filter element 18 blockage deteriorates, from And extend filter element 18 service life.
Use above-mentioned oil filter that backflow is pressed with the processing step of process as follows:
1), backflow force feed enters the electrification module 32 of U-shaped separation of particles module 3, makes the particulate matter in fluid charged, Deliver to separation module 33 afterwards;
2), the charged corpuscle in fluid is made to be polymerized to tube wall under the effect of external force by segregation apparatus 33, oil return afterwards Deliver to the first adsorbent equipment 34;
3), being adsorbed the magnetic polymeric microgranule in oil return by the first adsorption module 34, mechanical centrifugal mould is delivered in oil return afterwards Block 36;
4), magnetic microparticles not to be adsorbed is centrifuged by mechanical centrifugal module 36, and the second absorption mould is delivered in oil return afterwards Block 37;
5), the magnetic polymeric microgranule in the second adsorption module 37 second adsorption oil return;
6), magnetic particle magnetic is eliminated by demagnetization module 35;
7) after, the fluid of the most U-shaped separation of particles module 3 near-wall enters oil returning tube 7 by oil returning tube oil inlet pipe 22 Being back to fuel tank, the fluid of the pipeline center containing trace small particle microgranule then enters inner core 15 by inner core oil inlet pipe 12 to be carried out High-precision filtration;
8), the fluid carrying small particle microgranule flows into the helical flow path 17 of inner core 15 in the way of tangential influent stream, and fluid exists It is close to filter core flow under the effect of centrifugal force, and carries out high-precision filtration;
9), the fluid after high-precision filtration enters urceolus 19, and is discharged by the hydraulic oil oil-out 5 bottom urceolus 19.
Above detailed description of the invention is only the preferred embodiment of this creation, not in order to limit this creation, all in this wound Any modification, equivalent substitution and improvement etc. done within the spirit made and principle, should be included in this creation protection domain it In.

Claims (10)

1. the hydraulic system filter method using electrification, separating, adsorb and be centrifuged, it is characterised in that: it uses one Filter, this filter includes base plate, U-shaped separation of particles module, oil returning tube, inner core, helical flow path, filter element, outer barrel and end Lid;Wherein, described U-shaped separation of particles module, oil returning tube, outer barrel are sequentially placed on base plate;Set in described U-shaped separation of particles module Having a hydraulic oil inlet, it includes a U-tube, U-tube is sequentially installed with electrification module, separation module, the first adsorption module, Mechanical centrifugal module, the second adsorption module and demagnetization module;The top of described U-shaped separation of particles module and oil returning tube is passed through one time Oil cylinder oil inlet pipe connects;Described inner core is placed in outer barrel, if it is installed on end cap by a top board and bolt stem;Described spiral shell Eddy flow road is contained in inner core, is connected by an inner core oil inlet pipe between itself and U-shaped separation of particles module;Described inner core oil inlet pipe Being positioned at oil returning tube oil inlet pipe, and extend into the central authorities of U-shaped separation of particles module, its diameter is less than oil returning tube oil inlet pipe diameter, And be coaxially disposed with oil returning tube oil inlet pipe;Described filter element is arranged on the inwall of inner core, and its precision is 1-5 micron;Said tub Bottom be provided with a hydraulic oil oil-out;
It comprises the steps:
1), backflow force feed enters the electrification module of U-shaped separation of particles module, makes the particulate matter in fluid charged, send afterwards To separation module;
2), making the charged corpuscle in fluid be polymerized to tube wall under the effect of external force by segregation apparatus, oil return afterwards delivers to the One adsorbent equipment;
3), by the magnetic polymeric microgranule in the first adsorption module absorption oil return, mechanical centrifugal module is delivered in oil return afterwards;
4), magnetic microparticles not to be adsorbed is centrifuged by mechanical centrifugal module, and the second adsorption module is delivered in oil return afterwards;
5), the magnetic polymeric microgranule in the second adsorption module second adsorption oil return;
6), magnetic particle magnetic is eliminated by demagnetization module;
7), the fluid of the most U-shaped separation of particles module near-wall is back to oil after entering oil returning tube by oil returning tube oil inlet pipe Case, the fluid of the pipeline center containing trace small particle microgranule then enters inner core by inner core oil inlet pipe and carries out high-precision filtration;
8), the fluid carrying small particle microgranule flows into the helical flow path of inner core in the way of tangential influent stream, and fluid is at centrifugal force It is close to filter core flow under effect, and carries out high-precision filtration;
9), the fluid after high-precision filtration enters urceolus, and is discharged by the hydraulic oil oil-out bottom urceolus.
The hydraulic system filter method use electrification the most as claimed in claim 1, separating, adsorb and being centrifuged, its feature exists In: described electrification module includes some electrodes and an electrode controller;Described some electrodes are installed on the first oil return pipe, its It is respectively connecting to electrode controller.
The hydraulic system filter method use electrification the most as claimed in claim 1, separating, adsorb and being centrifuged, its feature exists Use uniform magnetic field separation module in: described separation module, this uniform magnetic field separation module include aluminum matter pipeline, two magnetic poles with And magnetic pole controller;Wherein, said two magnetic pole is separately positioned on aluminum matter pipeline, the opposite polarity of these two magnetic poles, and in It is oppositely arranged;Said two magnetic pole is respectively and electrically connected on magnetic pole controller.
The hydraulic system filter method use electrification the most as claimed in claim 1, separating, adsorb and being centrifuged, its feature exists Use rotating excitation field separation module in: described separation module, this rotating excitation field separation module include aluminum matter pipeline, iron shell, Three-phase symmetric winding and three-phase symmetrical current module;Described three-phase symmetric winding is wound on outside aluminum matter pipeline;Described iron shell It is coated on aluminum matter pipeline;Described three-phase symmetrical current module connects described three-phase symmetric winding.
The hydraulic system filter method use electrification the most as claimed in claim 1, separating, adsorb and being centrifuged, its feature exists In: described separation module uses helical pipe magnetic field separation module, and this helical pipe magnetic field separation module includes aluminum matter serpentine pipe Road, solenoid and solenoid control circuit;Wherein, described aluminum matter helical pipe is arranged in solenoid;Described solenoid and Solenoid control circuit is electrically connected with.
The hydraulic system filter method use electrification the most as claimed in claim 1, separating, adsorb and being centrifuged, its feature exists In: described first adsorption module and second is inhaled adsorption module and is used homopolarity adjacent type absorbing ring, this homopolarity adjacent type absorbing ring bag Include aluminium ring shape pipeline, forward solenoid, reverse solenoid and irony magnetic conduction cap;Described forward solenoid and reverse solenoid Being respectively arranged in aluminium ring shape pipeline, both are connected with electric current in opposite direction so that forward solenoid and reverse solenoid phase Like pole is produced at Lin;Described irony magnetic conduction cap is arranged on the inwall of aluminium ring shape pipeline, its be positioned at forward solenoid and Reverse solenoid adjacent and forward solenoid and the intermediate point of reverse solenoid axis.
The hydraulic system filter method use electrification the most as claimed in claim 1, separating, adsorb and being centrifuged, its feature exists In: described first adsorption module and second is inhaled adsorption module and is used the homopolarity adjacent type absorbing ring of charged hammer, this charged hammer Homopolarity adjacent type absorbing ring include aluminium ring shape pipeline, forward solenoid, reverse solenoid, irony magnetic conduction cap, dividing plate, electric shock Hammer and electric magnet;Described forward solenoid and reverse solenoid are respectively arranged in aluminium ring shape pipeline, and both are connected with direction Contrary electric current so that forward solenoid and reverse solenoid adjacent produce like pole;Described irony magnetic conduction cap is arranged in On the inwall of aluminium ring shape pipeline, it is positioned at forward solenoid and reverse solenoid adjacent and forward solenoid and reversely The intermediate point of solenoid axis;Described dividing plate is between forward solenoid and reverse solenoid;Described electric shock hammer and electric magnet Between dividing plate;Described electric magnet connects and can promote electric shock hammer, makes electric shock hammer tap aluminium ring shape inner-walls of duct.
8. the hydraulic system filter method that the employing described in claim 1 electrifies, separates, adsorbs and is centrifuged, it is characterised in that: Described mechanical centrifugal module uses eddy flow to be centrifuged module;Described eddy flow be centrifuged module include eddy flow tube wall, the first flow deflector, second Flow deflector, motor and flow transducer;Wherein, described first flow deflector is provided with 3, and these 3 first flow deflectors are along pipe Wall inner periphery is uniformly distributed every 120 °, and its laying angle is set to 18 °;Described second flow deflector and the first flow deflector structure are identical, its After being arranged on the first flow deflector, and and the first flow deflector stagger 60 ° and be connected in tube wall, its laying angle is set to 36 DEG C;Described The long limit of one flow deflector is connected with tube wall, and minor face extends along the axis of tube wall;Its leading edge frustrates into obtuse, and trailing edge is processed into wing, Its height is 0.4 times of tube wall diameter, 1.8 times of a length of tube wall diameter;Described motor connects and drives the first water conservancy diversion Sheet and the second flow deflector, to regulate laying angle;Described flow transducer is arranged on the central authorities in tube wall.
9. the hydraulic system filter method that the employing described in claim 1 electrifies, separates, adsorbs and is centrifuged, it is characterised in that: The bottom of described oil returning tube is provided with an overflow valve, is provided with an automatically controlled set screw bottom this overflow valve;Described overflow valve is provided with One oil drain out, this oil drain out is connected to a fuel tank by pipeline.
10. the hydraulic system filter method that the employing described in claim 1 electrifies, separates, adsorbs and is centrifuged, its feature exists In: the bottom of described inner core is rounding mesa-shaped, and it is connected by an inner core oil exit pipe and oil returning tube, and inner core oil exit pipe is provided with one Automatically controlled check-valves;The center upright of described inner core is provided with a hollow cylinder, hollow cylinder be arranged over pressure difference indicator, this pressure Difference indicator is installed on end cap;Described inner core oil inlet pipe and the tangent connection of helical flow path.
CN201610315811.XA 2016-05-12 2016-05-12 Hydraulic system filtering method adopting electrification, separation, adsorption and centrifugation Pending CN105864213A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610315811.XA CN105864213A (en) 2016-05-12 2016-05-12 Hydraulic system filtering method adopting electrification, separation, adsorption and centrifugation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610315811.XA CN105864213A (en) 2016-05-12 2016-05-12 Hydraulic system filtering method adopting electrification, separation, adsorption and centrifugation

Publications (1)

Publication Number Publication Date
CN105864213A true CN105864213A (en) 2016-08-17

Family

ID=56631773

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610315811.XA Pending CN105864213A (en) 2016-05-12 2016-05-12 Hydraulic system filtering method adopting electrification, separation, adsorption and centrifugation

Country Status (1)

Country Link
CN (1) CN105864213A (en)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN85109568A (en) * 1985-12-26 1987-07-01 中国人民解放军工程兵工程学院野战工程系工程机械教研室 The purification mechanism and the structure of multimachine reason high accuracy oil conditioner
CN1546198A (en) * 2003-11-28 2004-11-17 邝念曾 Method and system for purifying hydraulic-oil
CN103949340A (en) * 2014-05-04 2014-07-30 上海岩川电磁科技有限公司 Magnetic separation process
CN104028391A (en) * 2013-03-08 2014-09-10 深圳中环科环保科技有限公司 Magnetic hydrocyclone separation method and magnetic hydrocyclone separation device
CN204102661U (en) * 2014-07-14 2015-01-14 郑铁 A kind of fluid magnetizer
WO2015012696A1 (en) * 2013-07-25 2015-01-29 Lomapro B.V. Filter device and method for removing magnetizable particles from a fluid

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN85109568A (en) * 1985-12-26 1987-07-01 中国人民解放军工程兵工程学院野战工程系工程机械教研室 The purification mechanism and the structure of multimachine reason high accuracy oil conditioner
CN1546198A (en) * 2003-11-28 2004-11-17 邝念曾 Method and system for purifying hydraulic-oil
CN104028391A (en) * 2013-03-08 2014-09-10 深圳中环科环保科技有限公司 Magnetic hydrocyclone separation method and magnetic hydrocyclone separation device
WO2015012696A1 (en) * 2013-07-25 2015-01-29 Lomapro B.V. Filter device and method for removing magnetizable particles from a fluid
CN103949340A (en) * 2014-05-04 2014-07-30 上海岩川电磁科技有限公司 Magnetic separation process
CN204102661U (en) * 2014-07-14 2015-01-14 郑铁 A kind of fluid magnetizer

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
赵扬等: "液体过滤技术现状与我国的发展趋势", 《合肥工业大学学报(自然科学版)》 *

Similar Documents

Publication Publication Date Title
CN105864213A (en) Hydraulic system filtering method adopting electrification, separation, adsorption and centrifugation
CN105864157A (en) Filter method utilizing electrification, separation, adsorption and rotational magnetic fields for hydraulic system
CN105909603A (en) Oil filter based on electrification, separation and adsorption and used for hydraulic system
CN105909604A (en) Filter based on electrification, separation, adsorption and centrifugation and used for hydraulic system
CN105909601A (en) Filtering device based on electrification, separation, adsorption and rotating magnetic field and used for hydraulic system
CN105889205A (en) Oil filtering method adopting electrification, separation and adsorption for hydraulic system
CN105889223A (en) Oil filtering method adopting magnetization, adsorption, rotating magnetic field and centrifuging and used for hydraulic system
CN105864173A (en) Hydraulic system filter adopting magnetizing, adsorbing and centrifuging
CN106015184A (en) Method of filtering oil through full-band filtering, electrification, separation and adsorption
CN105889209A (en) Filtering box based on full-band variable-structure filtration, electrification, separation and centrifugation
CN105864116A (en) Oil tank for treating hydraulic oil through electrification, separation and adsorption of electric control loop
CN105971997A (en) Filtering method adopting working condition self-adaptive filtering, electrification, centrifugation and rotating magnetic field
CN105889210A (en) Oil filtering method based on full-band variable-structure working condition self-adaptive filtration, electrification and centrifugation
CN105889189A (en) Filtering method adopting wave suppression, electrification, separation, adsorption and centrifugation
CN105971998A (en) Oil filtering method adopting full-band working condition self-adaptive filtering, electrification and centrifugation
CN105864177A (en) Filtering box adopting full-band variable-structure filtering, electrification, adsorption and rotating magnetic field
CN105889211A (en) Oil filtering method based on full-band filtration, electrification, separation and centrifugation
CN105889196A (en) Filter method adopting wave suppression, electrification, separation, adsorption and rotating magnetic fields
CN105864159A (en) Filter equipment utilizing full-band variable-structure working condition self-adaptive filtration, electrification and adsorption
CN105889212A (en) Oil filter based on full-band working condition self-adaptive filtration, electrification and centrifugation
CN105864218A (en) Filtering device adopting wave suppression, electrification, separation, adsorption and rotating magnetic field
CN105864207A (en) Filtering method adopting full-band variable structure filtering, electrification, separation and adsorption
CN105889208A (en) Filtering box adopting full-band variable-structure filtering, electrification, separation and adsorption
CN105864225A (en) Oil filter adopting full-frequency-band working-condition self-adaption smoothing, electrification and rotational magnetic field
CN105971993A (en) Filter tank adopting working condition adaptive filtering, electrification, centrifuging and rotating magnetic field

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20160817