CN106474813A - A kind of filtration liquor separator - Google Patents
A kind of filtration liquor separator Download PDFInfo
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- CN106474813A CN106474813A CN201510549589.5A CN201510549589A CN106474813A CN 106474813 A CN106474813 A CN 106474813A CN 201510549589 A CN201510549589 A CN 201510549589A CN 106474813 A CN106474813 A CN 106474813A
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- cup
- filtrate
- drainage screen
- liquor separator
- filtration
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Abstract
The present invention relates to a kind of filter liquor separator, it includes：Top is provided with charging aperture and bottom is provided with the cup of liquid outlet, the drainage screen group separated in described cup and by described charging aperture and described discharging opening, from liquid outlet to deviating from the transparent tube that described charging aperture direction extends and being arranged on valve described transparent tube, form the filtrate chamber for accommodating filtrate in described cup between described drainage screen group and the bottom of described cup.Filtered using this filtration liquor separator and divided liquid operation can simplify to filter and point liquid operation, reduced the total duration filtering and dividing liquid.Further, since filtering and all realizations in filtration liquor separator of point liquid, filtrate loss is little, and the result of the test drawing is also more accurate.
Description
Technical field
The present invention relates to a kind of experimental provision, filter liquor separator particularly to a kind of.
Background technology
Filter is the equipment for separating liquid from solid that laboratory is commonly used, and the difference according to its principle can be divided into gravity filtration
Device, centrifugal filter etc..Wherein gravity filter utilizes solidliquid mixture through filtration under self gravitation effect,
Medium is discharged, and the method for conventional natural filtration is to make filter using simple glass funnel, makes of drainage screen
Filter medium, mixture is filtered, and obtains filtrate and the solid particle staying on drainage screen.Separatory funnel is
Laboratory frequently with liquid distributing device, separate for the liquid immiscible by two kinds..
A lot of experiment all includes filter and point two steps of liquid.For example, need to contain in a test
When the solidliquid mixture of water, oil and rock dust carries out separating, it usually needs first solidliquid mixture will be entered
Row filters and filters out rock dust, and then Jiang Shui, oily mixed liquor carry out point liquid and separate again.So, filter
Typically require with point liquid and carry out in filter and separatory funnel, complex operation, time-consuming.Meanwhile, mixture
Can remain on the inwall of filter, and mixed liquor remains on the inwall of separatory funnel although in single assembly
On residue may less, but the accumulation of the residue of two devices still can largely affect test knot
Really.
Content of the invention
The technical problem to be solved be how to shorten filter and point liquid overall time, simplify filter and
Divide the operation of liquid.
For above-mentioned technical problem, the present invention proposes a kind of filtration liquor separator, including：Top is provided with charging
Mouthful and bottom is provided with the cup of liquid outlet, the filtration separated in cup and by charging aperture and discharging opening
Net group, to the transparent tube deviating from the extension of described charging aperture direction and is arranged on the valve transparent tube from liquid outlet
Door, forms the filtrate chamber for accommodating filtrate in cup between drainage screen group and the bottom of cup.
In a specific embodiment, drainage screen group includes outer rim and is connected to the internal perisporium of cup and in cup
Multiple drainage screens that depth direction is arranged in order, the closer to the drainage screen of liquid outlet in multiple drainage screens, its mesh
Smallest cross-section area less.
In a specific embodiment, in multiple drainage screens near charging aperture drainage screen mesh horizontal stroke
Section is tapered to the direction near liquid outlet.
In a specific embodiment, in multiple drainage screens, the drainage screen near liquid outlet includes being respectively provided with
The multiple filtration mesh sheet having the through hole of vertical bar shaped and stacking gradually,
One end pair of the through hole of one end of the through hole in each filter net sheet filter net sheet adjacent with this filter net sheet
Connect, the not parallel mesh with formation bending of bearing of trend of two being mutually butted through hole.
In a specific embodiment, the quantity of drainage screen is more than or equal to 3, near the filtration of liquid outlet
Net and near the drainage screen between the drainage screen of charging aperture mesh cross-sectional area near charging aperture side
To tapered.
In a specific embodiment, filter liquor separator and also include being arranged on drainage screen group and deviate from liquid outlet side
Fan assembly, fan assembly is towards the air-out of liquid outlet direction.
In a specific embodiment, fan assembly includes being arranged in cup and diameter parallel in cup deeply
Spend the blast fan in direction, support or oppose from the extension of liquid outlet direction centrally along the axis of blast fan from blast fan
Main shaft and drive shaft rotate the first motor.
In a specific embodiment, filter the filtrate stirring wheel that liquor separator also includes being arranged on filtrate intracavity,
Filtrate stirring wheel is used for the filtrate mix homogeneously of filtrate intracavity.
In a specific embodiment, filtrate stirring wheel is coaxial with main shaft, and one end of main shaft connects filtrate stirring
Wheel.
In a specific embodiment, the filter screen that filtration liquor separator also includes being arranged in drainage screen group deviates from
The screening stirring wheel of liquid mouth side, the rotating shaft of screening stirring wheel is coaxial with main shaft.
In a specific embodiment, filter liquor separator also include being arranged in cup and vertical multiple every
Plate, the superjacent air space in filtrate chamber in cup is divided into multiple vertical passages by multiple dividing plates.
In a specific embodiment, filter the vibration section on the outer wall that liquor separator also includes be arranged on cup
Part.
Solidliquid mixture enters into the cup filtering liquor separator from charging aperture, and solidliquid mixture passes through drainage screen group
When, solid particle is filtered in drainage screen group, and filtrate is flowed into filtrate intracavity.Filtrate is static in filtrate intracavity
After layering, can operate valve that filtrate is carried out with point liquid and operate to separate filtrate.As can be seen here, solid-liquid mixes
Compound can be realized filtering and point liquid operation filtering liquor separator, simplify filtration and point liquid operation, decrease filtration
Total duration with point liquid.Further, since filtering and all realizations in filtration liquor separator of point liquid, filtrate loss is little,
The result of the test drawing is more accurate.
Brief description
Hereinafter will be based on embodiment and refer to the attached drawing is being described in more detail to the present invention.Wherein：
Fig. 1 is the complete section schematic diagram of the filtration liquor separator of one embodiment of the present invention；
Fig. 2 is the close-up schematic view of the single filter net in Fig. 1；
Fig. 3 is the close-up schematic view of the cascade filtration net in Fig. 1；
Fig. 4 is the close-up schematic view of the three-stage filtration net in Fig. 1；
Fig. 5 is the partial enlarged drawing of the single filter net in Fig. 1 and rubber seal；
Fig. 6 is the partial enlarged drawing of the fixed frame in Fig. 1 and rubber seal；
Fig. 7 is a kind of complete section schematic diagram of the filtration liquor separator of preferred implementation of the present invention；
Fig. 8 be Fig. 7 in G-G to complete section schematic diagram；
Fig. 9 is a kind of complete section schematic diagram of the filtration liquor separator of preferred implementation of the present invention；
Figure 10 is the structural representation of the screening stirring wheel in Fig. 9；
Figure 11 is a kind of complete section schematic diagram of the filtration liquor separator of preferred implementation of the present invention.
In the accompanying drawings, identical part uses identical reference.Accompanying drawing is not drawn according to actual ratio.
Specific embodiment
Below in conjunction with accompanying drawing, the invention will be further described.
Fig. 1 shows the schematic diagram of the filtration liquor separator in a kind of embodiment of the present invention.Filter liquor separator to include
Cup 10, bowl cover 120, fan assembly, drainage screen group, lens tube and valve 241.Cup 10 is in tubbiness.
Cup 10 is preferably barrel-shaped.The open top of cup 10, this opening is rim of a cup.The side wall of cup 10 sets
It is equipped with charging aperture 100.The bottom of cup 10 is provided with liquid outlet 11.This charging aperture 100 leans on into cup 10
Rim of a cup.Preferably, the side wall of cup 10 is transparent.Bowl cover 120 covers on the rim of a cup of cup 10.Bowl cover 120
Construction is discoid, covers on the rim of a cup of cup 10.Preferably, bowl cover 120 is disc.Drainage screen group
For filtering solid particles.
Fan assembly include blast fan 131, main shaft 13, the first motor 111, the first decelerator 112,
Fixed frame 12.First motor 111 and the first decelerator 112 can be arranged in above bowl cover 120.First
Motor 111 is in transmission connection with the first decelerator 112, the output shaft of the first motor 111 and the first decelerator
112 input shaft is connected.First decelerator 112 and cup 10 are relatively fixed.For example, the first decelerator 112
It is fixed on bowl cover 120.Preferably, the first decelerator 112 is coaxial speed reducer.Fan assembly goes out downwards
Wind.
Blast fan 131 includes wheel disc and blade.Blade is evenly distributed on the outer peripheral face of wheel disc in paddle-like.
Main shaft 13 is connected to wheel disc.Main shaft 13 is coaxial with wheel disc.The upper end of main shaft 13 passes through the top of bowl cover 120
And be in transmission connection with the first decelerator 112.Preferably, main shaft 13 and bowl cover 120 are coaxially disposed.
Fixed frame 12 is arranged in cup 10.Preferably, fixed frame 12 is arranged on charging aperture 100
Top.Fixed frame 12 is in box type frame structure substantially.The top of fixed frame 12 and bottom ventilation.Gu
The sidepiece determining framework 12 is connected to cup 10.For example, fixed frame 12 includes top board and base plate, top board and bottom
Plate is in network.Further for example, the top of fixed frame 12 and bottom are all provided with being set to beam structure.Fan leaf
Wheel 131 is arranged in fixed frame 12.Fixed frame 12 carries out spacing to blast fan 131, it is to avoid fan
Impeller 131 axially rocks.
Drainage screen group includes multiple drainage screens.Multiple drainage screens are all disc-shaped.The outer rim of multiple drainage screens all abuts
Internal perisporium in cup 10.The mesh of connection drainage screen opposite sides is provided with multiple drainage screens.Preferably
Ground, drainage screen is perpendicular to the depth direction of cup 10.Drainage screen is preferably stainless (steel) wire.Multiple drainage screens divide
Wei not single filter net 141, cascade filtration net 142, three-stage filtration net 143.141, two grades of single filter net
Drainage screen 142, three-stage filtration net 143 are arranged in order in the depth direction, and wherein, single filter net 141 is
Near charging aperture 100.Single filter net 141, cascade filtration net 142, three-stage filtration net 143 mesh
Little cross-sectional area is sequentially reduced.Cavity between cup 10 filtering net group and cup 10 bottom is filtrate chamber.
Transparent tube 15 one end is connected in liquid outlet 11.The other end of transparent tube 15 extends downwardly.Transparent tube 15
Generally it is made of clear material, this transparent material can be for example clear glass or transparent plastic.Valve 241 sets
Put on the pipeline of transparent tube 15.Valve 241 is used for closing or open transparent tube 15.
By comprise oil, water, solid particle mixture put in cup 10 from charging aperture 100, warp successively
Cross single filter net 141, cascade filtration net 142, three-stage filtration net 143 and by the solid particle in mixture
Filter, remaining filtrate is flowed into filtrate intracavity.Due to single filter net 141, cascade filtration net 142, three
The smallest cross-section area of the mesh of level drainage screen 143 is sequentially reduced, and the particle diameter of solid particle is sieved, that is,
Particle diameter maximum, cascade filtration net 142 and the single filter net 141 of the solid particle of single filter net 141 top
Between the solid particle than cascade filtration net 141 top for the solid grain size particle diameter little, cascade filtration net 142
The particle diameter of the solid particle and three-stage filtration net 143 between is minimum.In filter process, open fan assembly,
Fan assembly is dried downwards.Air-flow blows to the liquid level of mixture straight down.So, air-flow applies to mixture
Downward pressure promotes mixture accelerated filtration, reduces filtration time.
After the completion of filtering, close fan assembly so that the filtrate stratification of the oil-water mixing of filtrate intracavity.
After filtrate layered, carry out a point liquid operation：First measuring cup is placed on the lower end of transparent tube 15, opens transparent
Valve 241 on pipe 15, water is all flowed into first measuring cup along transparent tube 15, when water-oil interface reaches valve
Valve 241 is closed after at 241.Then second measuring cup is placed into the lower end of transparent tube 15, opens valve 241,
Oil is all flowed into second measuring cup along transparent tube 15.This completes a point liquid.When transparent tube 15 carries out discharge opeing
When, fan assembly can also be opened to accelerate discharge opeing simultaneously, shorten drain time.
After the completion of dividing liquid, open fan assembly, the solid particle of attachment in drainage screen group is air-dried, reduce
The time that solid particle is dried.Quick-air-drying solid particle can avoid solid particle hardened together, is easy to back
Receive solid particle.
Thus, when the mixture of two liquid phases and a solid-state being carried out separate using filtration liquor separator, filter and point liquid
All carry out in filtering liquor separator, simplify experiment process so that filtering and dividing liquid operation easier.And
Disposably filtered in filtration liquor separator and point liquor ratio is filtered respectively in two devices and divided liquid to operate
The filtrate loss in a device of middle residual is less.Further, since being provided with single filter net 141, cascade filtration
Net 142, three-stage filtration net 143, also complete the screening to solid particle while filtering, subtract further
Lack test period.
As shown in Fig. 2 the mesh of single filter net 141 is transversal tapered towards the direction near liquid outlet 11.
So, mesh hole is conducive to the less solid particulate matter of particle diameter to pass through single filter net 141.Single filter net 141
On mesh be preferably funnel-form.The mesh of single filter net 141 can be the mesh that inwall is taper seat, net
The larger one end of bore dia is upward.I.e. the vertical section of this mesh is trapezoidal, under the upper bottom length in vertical section is more than
Bottom length.
As shown in figure 3, the cross-sectional area of the mesh of cascade filtration net 142 is to the direction near charging aperture 100 gradually
Contracting.So, mesh is conducive to stoping the larger solid particulate matter of particle diameter filtered by drainage screen entrance next stage
Journey.The mesh of cascade filtration net 142 can be the mesh that inwall is taper seat, the larger one end court of mesh diameter
Under.I.e. the vertical section of this mesh is trapezoidal, and the length of going to the bottom in vertical section is more than upper bottom length.
As shown in figure 4, three-stage filtration net 143 includes the multiple filtration mesh sheet being laminated.In every layer of filter net sheet all
It is provided with the through hole of vertical bar shaped.The bearing of trend of the adjacent through hole of two filter net sheets is different.It is located at phase respectively
Two through hole one end close to each other on two adjacent filter net sheets are docking together.Through hole on different filter discs
Being corresponding in turn to is docking together forms the mesh of bending.Tortuous mesh desirably prevents solid particulate matter and enters filter
In sap cavity.Meanwhile, when reclaiming the solid particle being attached on three-stage filtration net 143, can be by multiple filtration
Mesh sheet splits and comes, and so can be easier to strip down solid particle from three-stage filtration net 143.
Preferably, filter liquor separator and also include heat-insulation layer 221 and heater block.Heat-insulation layer is around cup 10
Periphery wall is arranged.Heater block is arranged between heat-insulation layer and cup 10.Heat-insulation layer can be for example rock wool guarantor
Warm carpet veneer, phenolic foam board or polystyrol plastic foam plate.Heater block is arranged on heat-insulation layer and cup 10
Between.Heater block can be heating wire.Heater block heats to promote filtrate to be sufficiently mixed to cup 10,
It can in addition contain accelerate to dry moist solid particulate matter, prevent its caking.
Preferably, filter liquor separator and also include vibrating mass 230.Vibrating mass 230 can be arranged on cup 10
Outer wall on.Vibrating mass 230 can also be arranged on the outer wall of heat-insulation layer 221.Vibrating mass 230 is preferred
For rotary and centrifugal type vibrator.Vibrating mass 230 applies to vibrate in filter process, can effectively facilitate solid
The screening further of grain.The early stage that vibrating mass 230 carries out point liquid in filtrate is vibrated, and filtrate can be accelerated to divide
Layer.
Preferably, filter liquor separator and be provided with two valves 241, two valves 241 are arranged at transparent tube 15
Pipeline on.Two valves 241 are separated.So setting can facilitate the carrying out of the filtrate to two liquid phases to separate
Operation.
Preferably, cup 10 is provided with handle, experimenter easily can take to filter by handle and divide
Liquid device.
In a preferred embodiment, as shown in fig. 7, single filter net 141, cascade filtration net 142 and
Three-level filter screen 143 by cup 10 inner space be separated into 251, two grades of filter chambers 252 of one-level filter chamber from top to bottom,
Precipitation chamber 253 and filtrate chamber 254.Filter liquor separator and also include multiple dividing plates 144.Multiple dividing plates 144 are parallel
Depth direction in cup 10.One side of multiple dividing plates mutually abuts, separately multiple dividing plates a side
It is connected to the inwall of cup 10.
Dividing plate extends to the top of single filter net 141 from three-level filter screen 143.In the present embodiment, dividing plate group
Arrange around the axis circumference in equal parts of cup 10 including 144,3 dividing plates 144 of 3 dividing plates, material is thus formed
3 filtration channels from top to bottom.So, dividing plate 144 by 251, two grades of filter chambers 252 of one-level filter chamber, precipitation
Several independent sieves sub-chamber of 253 one-tenth of chamber.Specifically drainage screen group also includes dividing plate group, dividing plate group bag
Include at least 2 and cover axle from drainage screen group and extend out to the dividing plates 144 of drainage screen group outer rim, dividing plate 144 is by one
Level 251, two grades of filter chambers 252 of filter chamber and precipitation chamber 253 are separated into the sub-chamber of respective amount, phase up and down respectively
Adjacent sub-chamber is interconnected the filtration channel being formed from top to bottom.Fig. 8 shows the optimal way of this programme,
I.e. dividing plate group includes 144,3 dividing plates 144 of 3 dividing plates around the arrangement of axis circumference in equal parts, material is thus formed 3
Individual top-down filtration channel.When using filtering liquid separating cup, only can use an above-mentioned filtration channel,
Can also be simultaneously using 3 filtration channels.This programme is not limited to the scheme of above 3 filtration channels, also may be used
To be other more deciles or the not decile plan of establishment, for example, it is separated into more than 4 around axle using dividing plate 144
Line decile or the scheme of not circumference in equal parts arrangement, thus form more than 4 uiform section areas or unequal section area
Filtration channel.In order to strengthen filtering the service efficiency of liquid separating cup, increase the solid-liquid that its singlepass can be processed
Mixing species or the use reducing filter area in the case of processing a kind of solidliquid mixture,
In a preferred embodiment, filter the filtrate stirring wheel that liquor separator also includes being arranged on filtrate intracavity
151.Main shaft 13 passes through drainage screen group to be connected on filtrate stirring wheel 151.Filtrate stirring wheel 151 and main shaft
13 are coaxially disposed.Biphase filtrate, before carrying out filtrate static layering, can be sufficiently mixed by filtrate stirring wheel 151.
In a preferred embodiment, filter the filtrate stirring wheel that liquor separator also includes being arranged on filtrate intracavity
151 and the filtrate coaxial with filtrate stirring wheel 151 stirring wheel shaft.Main shaft 13 is not connected to filtrate stirring wheel 151.
Filtrate glue stirring wheel shaft stretches out from the middle part of filtrate stirring wheel 151.Main shaft 13 is tubulose.Filtrate stirs wheel shaft
It is inserted into main shaft 13 and be in transmission connection with the first decelerator 112.Main shaft 13 is coaxially disposed with filtrate stirring wheel shaft.
First decelerator 112 can distinguish drive shaft 13 at different rates and filtrate stirring wheel shaft rotates.So,
Even if blast fan quick rotation also will not make the filtrate of filtrate intracavity splash.Meanwhile, can be by biphase filtrate
It is sufficiently mixed.
In a preferred embodiment, main shaft 13 is tubular structure.Filter liquor separator also to include and main shaft 13
Coaxial support bar.Support bar runs through multiple drainage screens, and is fixedly connected with drainage screen.One end of support bar is inserted
Enter in main shaft 13 and be fixed on the first decelerator 112.So, support bar is just by the mistake in drainage screen group
Screen support is got up, and prevents the middle part of drainage screen sagging.
In a preferred embodiment, as shown in figure 9, filter liquor separator also include multiple screening stirring wheels 161,
162.The axis of screening stirring wheel is each parallel to the depth direction of cup 10.As shown in Figure 10, screening stirring
Wheel includes base wheel 162 and the multiple supporting legs 163 extending radially outwardly from base wheel 162, it is preferred to use six will
The supporting leg 163 of circumference equal dividing arrangement.The section of supporting leg 163 can be in " U ", is conducive to solid high for heap
Particulate matter is bulldozed, but this programme is not limited to above-mentioned specific structure, and can be that other can play similar work(
The structure of energy, for example with two or more supporting leg, adopts above-mentioned circumference supporting leg of decile arrangement etc..Multiple
In screening stirring wheel, one-level screening stirring wheel 161 is arranged on one-level filter chamber 251 bottom near single filter net 141
Position, two grades screening stirring wheels 162 be arranged on two grades of filter chamber 252 bottoms near the portion of cascade filtration net 142
Position.Multiple screening stirring wheels are all coaxial with main shaft 13, and main shaft 13 extends downwardly wears one-level screening stirring wheel and
Level screening stirring wheel and two grades of screening stirring wheels are connected with each other, and main shaft 13 rotates and can drive one-level screening stirring
Wheel and two grades of screening stirring wheels rotate.So, screening stirring wheel can be deposited in the solid particle on drainage screen
Thing shakeouts extruding, thus promoting to be passed to drainage screen, to improve the screening degree of solid particle.
Screening stirring wheel can also be using another kind of kind of drive.Screening stirring wheel is not connected with main shaft 13,
Main shaft 13 is tubulose.Filter liquor separator and also include screening stirring wheel shaft.Screening stirring wheel shaft is coaxial with main shaft 13.
One end of screening stirring wheel shaft passes through one-level screening stirring wheel and two grades of screening stirring wheels and sieves stirring with one-level
Wheel and two grades of screening stirring wheels form a fixed connection.The other end of screening stirring wheel shaft be inserted into main shaft 13 and with
First decelerator 112 is in transmission connection.Preferably, filtrate stirring wheel shaft is arranged to tubulose, and filtrate stirring wheel shaft is inserted
Enter in main shaft 13 and its one end is formed with the first decelerator 112 and is in transmission connection.Screening stirring wheel shaft insertion
To in filtrate stirring wheel shaft, one end of screening stirring wheel is formed with the first decelerator 112 and is in transmission connection.So,
Different rotating speeds can will can be set on demand between blast fan, filtrate stirring wheel 151 and screening stirring wheel.
It is highly preferred that screening stirring wheel shaft and main shaft 13 are tubulose.Screening stirring wheel shaft, main shaft 13 and filtrate are stirred
Mix wheel shaft all coaxial.It is in transmission connection in screening stirring wheel shaft one end insertion main shaft 13 and with the first decelerator 112.
Filtrate is stirred in one end insertion screening stirring wheel shaft of wheel shaft and is in transmission connection with the first decelerator 112.Such
One speed reducer 112 can simultaneously drive screening stirring wheel shaft, main shaft 13 and filtrate stirring wheel shaft, and sieves
The rotating speed that stirring wheel shaft, main shaft 13 and filtrate are stirred between wheel shaft can differ.
In a preferred embodiment, filter liquor separator and also include driving for the centrifugation driving cup 10 to rotate
Dynamic device and rotary shaft rack.Rotary shaft rack is arranged on the middle part at the cup bottom of cup 10.Centrifugal driving device includes
Second decelerator 172, the second motor 171.Second motor 171 is connected to the defeated of the second decelerator 172
Enter axle.The output shaft of the second decelerator 172 is fixedly connected on rotary shaft rack.The axis of this output shaft and cup 10
Dead in line.Centrifugal driving device can drive cup 10 to rotate about the axis thereof.So, centrifugation drives dress
Put screening and the mixed effect that can strengthen mixture when driving cup 10 rotation.It is highly preferred that in power set
During second drives rotation, the axis of cup 10 and plumb line are in 30 ° of angles.The scheme of this Sloped rotating
It is more beneficial for sieving and mix a point liquid.
In a preferred embodiment, as shown in figure 5, filter liquor separator also to include being arranged on drainage screen and cup
Rubber seal 14 between the inwall of body 10.Rubber seal 14 is used for preventing the solid particulate matter of different layers
Move to lower floor's screening space not over drainage screen from the gap at edge.Rubber seal 14 preferable configuration
For the annular element of annular groove is provided with inwall.Rubber seal 14 is fixed on the inwall of cup 10.Cross
The edge of filter screen is embedded in rubber seal 14.After so arranging, rubber seal 14 can be fixed
Filter screen and avoid drainage screen to come off or rock.In addition, in vibrating mass 230 vibration cup 10, due to cup
Rubber seal 14 between body 10 and drainage screen plays cushioning effect, collides between drainage screen and cup 10
The noise producing is reduced, or even is eliminated.Preferably, as shown in fig. 6, periphery in fixed frame 12
Suit rubber seal 14 on wall, so that forming cushion between fixed frame 12 and cup 10, reduces fan
Device work produce noise, and vibrating mass 230 vibration when between cup 10 and cup 10 due to collision
The noise producing.Meanwhile, when the periphery wall of fixed frame 12 is embedded into rubber seal 14, can be fixed
To on cup 10.
In a preferred embodiment, filter liquor separator and also include gate 211.Gate 211 is arranged on charging
To switch charging aperture 100 on mouth 100.Close when rotating in a point liquid stirring wheel, blast fan and screening stirring wheel
Gate, does not thus have mixture and spills from charging aperture 100.Meanwhile, extraneous impurity is also difficult to enter into
In cup 10.One end of valve 211 is embedded in the side wall of cup 10 it is possible to slide up and down.Preferably,
Gate is provided with gate pushing hands, pushes up throttle valve to facilitate, downward closed shutter.Preferably, valve 211
Upper end is stretched into partly can be formed with cup body wall in this 10 wall of cup and is contacted frictional fit, prevents gate easily
Glide.
Present invention additionally comprises filtering the using method of liquor separator, comprise the following steps：
Step one：Solidliquid mixture is inputted in cup 10, solid particle in mixture by single filter net,
Cascade filtration net and three-stage filtration net leach, and the liquid in mixture sinks to filtrate intracavity.Solidliquid mixture is permissible
Add in it is also possible to by opening a charging aperture 100 on cup 10 outer wall top at cup 10 opening,
Mixture is added in this charging aperture 100 is to cup 1.
Step 2：Drive filtrate stirring wheel 151 to rotate, open heater block and vibrating mass, make filtrate intracavity
Filtrate be sufficiently mixed, stratification, open transparent tube 15, in batches release cup 10 in liquid.Heating
Part ensures filtrate constant temperature or keeps filtrate within specified temperatures or in temperature range, filtrate stirring wheel 151 He
Vibrating mass makes filtrate be sufficiently mixed.Carry out stratification after the completion of filtration, can be by switching transparent tube
Valve on 15 is so that layered filtrate is smoothly detached.
Step 3：Drive blast fan, one-level screening stirring wheel and two grades of screening stirring wheel rotations.Single filter net,
Cascade filtration net and the online solid particulate matter of three-stage filtration are oven-dried, and single filter net and cascade filtration are online
Solid particle sieves further.Blast fan promotes solid particulate matter to pass through drainage screen, and prevents its humidity knot
Block, can also promote filtrate exclusion cup 10 bottom, and screening stirring wheel can will be deposited in consolidating on drainage screen
Body particulate matter shakeouts and suitably extrudes, and promotees to be passed to drainage screen, and meanwhile, heater block promotes solid on drainage screen
Moisture evaporation in body granulate mixture, prevents its caking, and vibrating mass is same to be promoted to be passed to drainage screen, increases
Strong screening effect.
Step 4：Close blast fan, outer wall is dried in insulation, vibrating mass, one-level sieve stirring wheel and two grades
Screening stirring wheel.Take out dynamic filter device from cup 10, by single filter net, cascade filtration net and three
Solid particulate matter classification on level drainage screen preserves.When filtrate excludes cup 10 completely, can be by power mistake
Filter device takes out cup 10, and the solid particulate matter on every layer of drainage screen is collected according to the numerical classification setting particle diameter
Preserve.
In order to strengthen filtering the effect of liquor separator filtration screening and mixing, can also pass through in above-mentioned operation
Apply revolving force and reach object above outside cup 10, be specifically also associated with centrifugation in cup 10 bottom and drive
Dynamic device, opens centrifugal driving device so that cup 10 is defeated around power set second in step one and step 2
Shaft rotates, and strengthens solid particulate matter and filters and liquid mixing effect.Further, it is possible to make cup 10
In the state of axis is in 30 ° of angles with plumb line, carry out rotation process.
Filter the screening operation that liquor separator carries out solid particle while carrying out and filter and divide liquid, wherein blast fan
The introducing of part not only can promote filtrate exclusion cup and additionally it is possible to play, solid particulate matter to be sieved be promoted to lead to
Cross drainage screen and air-dry scattered effect, multistage filter screen structure, not only solid particulate matter is separated with filtrate,
But also the solid particulate matter leaching can be carried out classification screening according to the difference of its particle diameter, unique cup revolves
Turn and can also promote to mix and sieve.
Although by reference to preferred embodiment, invention has been described, without departing from the scope of the present invention
In the case of, it can be carried out with various improvement and part therein can be replaced with equivalent.Especially, only
Otherwise there is structural hazard, the every technical characteristic being previously mentioned in each embodiment all can combine in any way
Come.The invention is not limited in specific embodiment disclosed herein, but include falling within the scope of the appended claims
All technical schemes.
Claims (12)
1. a kind of filtration liquor separator, including：Top is provided with charging aperture and bottom is provided with the cup of liquid outlet,
The drainage screen group separated in described cup and by described charging aperture and described discharging opening, from liquid outlet to
Deviate from the transparent tube that described charging aperture direction extends and be arranged on valve in described transparent tube,
Formed for accommodating filtrate between described drainage screen group and the bottom of described cup in described cup
Filtrate chamber.
2. filtration liquor separator according to claim 1 is it is characterised in that described drainage screen group is included outward
Edge is connected to internal perisporium and the multiple drainage screens that are arranged in order of depth direction in described cup of described cup, many
The closer to the drainage screen of described liquid outlet in individual described drainage screen, the smallest cross-section area of its mesh is less.
3. filtration liquor separator according to claim 2 is it is characterised in that in multiple described drainage screens
Tapered near the transversal direction towards close described liquid outlet of the mesh of the drainage screen of described charging aperture.
4. filtration liquor separator according to claim 3 is it is characterised in that in multiple described drainage screens
Drainage screen near described liquid outlet includes the multiple filtration that is provided with the through hole of vertical bar shaped and stacks gradually
Mesh sheet,
The one of one end of through hole in each described filter net sheet through hole of filter net sheet adjacent with this filter net sheet
End docking, the bearing of trend of two being mutually butted through hole not parallel to form the mesh of bending in drainage screen.
5. filtration liquor separator according to claim 4 is it is characterised in that the quantity of described drainage screen is big
In or be equal to 3, near the drainage screen of described liquid outlet and near the mistake between the drainage screen of described charging aperture
The cross-sectional area of the mesh of filter screen is tapered to the direction near described charging aperture.
6. filtration liquor separator according to any one of claim 1 to 5 is it is characterised in that described mistake
Filter liquor separator also includes being arranged on the fan assembly that described drainage screen group deviates from described liquid outlet side, described fan
Device can be towards described liquid outlet direction air-out.
7. filtration liquor separator according to claim 6 is it is characterised in that described fan assembly includes setting
Put in described cup and diameter parallel in the blast fan of described cup depth direction, from described blast fan
The axis centrally along described blast fan to deviating from the main shaft that described liquid outlet direction extends and drive described
First motor of main axis.
8. filtration liquor separator according to claim 7 is it is characterised in that described filtration liquor separator also wraps
Include the filtrate stirring wheel being arranged on described filtrate intracavity, described filtrate stirring wheel is used for the filter of described filtrate intracavity
Liquid mix homogeneously.
9. filtration liquor separator according to claim 8 is it is characterised in that described filtrate stirring wheel and institute
State main shaft coaxially, one end of described main shaft connects described filtrate stirring wheel.
10. filtration liquor separator according to claim 7 is it is characterised in that described filtration liquor separator also wraps
Include the screening stirring wheel that the drainage screen being arranged in described drainage screen group deviates from described liquid outlet side, described screening
The rotating shaft of stirring wheel is coaxial with described main shaft.
11. liquor separators that filter according to any one of claim 1 to 5 are it is characterised in that described mistake
Filter liquor separator also includes being arranged in described cup and vertical multiple dividing plates, and multiple described dividing plates are by institute in cup
The superjacent air space stating filtrate chamber is divided into multiple vertical passages.
12. liquor separators that filter according to any one of claim 1 to 5 are it is characterised in that described mistake
Filter liquor separator also includes the vibrating mass being arranged on the outer wall of described cup.
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| CN201510549589.5A CN106474813B (en) | 2015-08-31 | 2015-08-31 | A kind of filtering dispenser |
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| CN201510549589.5A CN106474813B (en) | 2015-08-31 | 2015-08-31 | A kind of filtering dispenser |
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| CN106474813A true CN106474813A (en) | 2017-03-08 |
| CN106474813B CN106474813B (en) | 2018-09-11 |
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Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108854335A (en) * | 2018-07-05 | 2018-11-23 | 合肥连森裕腾新材料科技开发有限公司 | A kind of processing cleaner of high performance composites |
| CN108907960A (en) * | 2018-07-08 | 2018-11-30 | 马晏 | A kind of waste material recovery device for glass production |
| CN109266371A (en) * | 2018-08-28 | 2019-01-25 | 湖南远扬煤机制造有限公司 | A kind of particle blanking mechanism and fall the net gas tower of stream |
| CN111359576A (en) * | 2020-03-03 | 2020-07-03 | 王鑫 | Reation kettle with solid-liquid separation equipment |
| CN111544938A (en) * | 2020-05-21 | 2020-08-18 | 赵曼利 | Self-interacting sewage filter equipment |
| CN112191017A (en) * | 2020-10-16 | 2021-01-08 | 张伶柯 | Screening device for squeezed wood sesame oil |
| CN112263861A (en) * | 2020-10-09 | 2021-01-26 | 嘉兴晶铸生物科技有限公司 | Sample cup, cell pretreatment method and sample slide device |
| CN112474077A (en) * | 2020-11-06 | 2021-03-12 | 重庆化工职业学院 | Chemical and chemical solid-liquid classification recovery processing device and using method thereof |
| CN112933687A (en) * | 2021-03-22 | 2021-06-11 | 四川省分析测试服务中心 | Multifunctional filtrate receiving cup |
| CN113426166A (en) * | 2021-07-01 | 2021-09-24 | 上饶师范学院 | Pressure filter is used in mine |
| WO2023279729A1 (en) * | 2021-07-09 | 2023-01-12 | 青岛海尔空调器有限总公司 | Liquid dispenser, air conditioner, and control method |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0642373B1 (en) * | 1991-07-12 | 1997-11-12 | Nordic Water Products Aktiebolag | Method and apparatus for separating gaseous bubbles and sand fro m a liquid flow |
| CN201001993Y (en) * | 2007-02-10 | 2008-01-09 | 杨建丽 | Sewage filter |
| CN201541542U (en) * | 2009-10-21 | 2010-08-11 | 甘肃大禹节水股份有限公司 | Sand stone net type manual backwashing filter fertilizer apparatus |
| CN202427234U (en) * | 2011-12-13 | 2012-09-12 | 吉林大学 | Solid-liquid separation device of three-phase separator |
| CN202724836U (en) * | 2012-05-31 | 2013-02-13 | 森田化工(张家港)有限公司 | Solid-liquid separation device |
| CN202822948U (en) * | 2012-09-28 | 2013-03-27 | 新疆水利水电科学研究院 | Vertical dual-stage self-cleaning screen filter driven by motor |
-
2015
- 2015-08-31 CN CN201510549589.5A patent/CN106474813B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0642373B1 (en) * | 1991-07-12 | 1997-11-12 | Nordic Water Products Aktiebolag | Method and apparatus for separating gaseous bubbles and sand fro m a liquid flow |
| CN201001993Y (en) * | 2007-02-10 | 2008-01-09 | 杨建丽 | Sewage filter |
| CN201541542U (en) * | 2009-10-21 | 2010-08-11 | 甘肃大禹节水股份有限公司 | Sand stone net type manual backwashing filter fertilizer apparatus |
| CN202427234U (en) * | 2011-12-13 | 2012-09-12 | 吉林大学 | Solid-liquid separation device of three-phase separator |
| CN202724836U (en) * | 2012-05-31 | 2013-02-13 | 森田化工(张家港)有限公司 | Solid-liquid separation device |
| CN202822948U (en) * | 2012-09-28 | 2013-03-27 | 新疆水利水电科学研究院 | Vertical dual-stage self-cleaning screen filter driven by motor |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108854335A (en) * | 2018-07-05 | 2018-11-23 | 合肥连森裕腾新材料科技开发有限公司 | A kind of processing cleaner of high performance composites |
| CN108907960A (en) * | 2018-07-08 | 2018-11-30 | 马晏 | A kind of waste material recovery device for glass production |
| CN109266371A (en) * | 2018-08-28 | 2019-01-25 | 湖南远扬煤机制造有限公司 | A kind of particle blanking mechanism and fall the net gas tower of stream |
| CN111359576A (en) * | 2020-03-03 | 2020-07-03 | 王鑫 | Reation kettle with solid-liquid separation equipment |
| CN111359576B (en) * | 2020-03-03 | 2022-04-29 | 王鑫 | Reation kettle with solid-liquid separation equipment |
| CN111544938A (en) * | 2020-05-21 | 2020-08-18 | 赵曼利 | Self-interacting sewage filter equipment |
| CN112263861A (en) * | 2020-10-09 | 2021-01-26 | 嘉兴晶铸生物科技有限公司 | Sample cup, cell pretreatment method and sample slide device |
| CN112191017A (en) * | 2020-10-16 | 2021-01-08 | 张伶柯 | Screening device for squeezed wood sesame oil |
| CN112474077A (en) * | 2020-11-06 | 2021-03-12 | 重庆化工职业学院 | Chemical and chemical solid-liquid classification recovery processing device and using method thereof |
| CN112933687A (en) * | 2021-03-22 | 2021-06-11 | 四川省分析测试服务中心 | Multifunctional filtrate receiving cup |
| CN113426166A (en) * | 2021-07-01 | 2021-09-24 | 上饶师范学院 | Pressure filter is used in mine |
| WO2023279729A1 (en) * | 2021-07-09 | 2023-01-12 | 青岛海尔空调器有限总公司 | Liquid dispenser, air conditioner, and control method |
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