Utility model content
In view of this, the utility model embodiment provides a kind of oily wastewater separator, and main purpose solution must not divide
From oil droplet of the particle diameter more than 40 microns, the problem of sewage isolated is not up to standard, low separation efficiency.
To reach above-mentioned purpose, the utility model mainly provides following technical solution:
On the one hand, the utility model embodiment provides a kind of oily wastewater separator, and one end of the separator is at least
Equipped with oily wastewater import, the other end is at least provided with sewage discharge outlet;From the import to the outlet, in the separator
Include successively:Pretreatment unit, for separating sludge in the oily wastewater;
Inclined plate separator, its top and bottom are closely connected with the top of the separator and bottom respectively, described oblique
Plate separator is used for water-oil separating;The top of the separator is equipped with fuel-displaced for accommodating the inclined plate separator separation
Oil groove;
The outlet connection delivery pump, for the sewage in the oily wastewater to be extracted out from the separator.
Preferably, the pretreatment unit includes input duct, splashing separator disk and sludge hopper, the input duct
To be stretched into through the import in the pretreatment unit, the top of the splashing separator disk is connected with the top of the separator,
The splashing separator disk is arranged in the pretreatment unit vertically, the bottom of the splashing separator disk and the bottom of the separator
With spacing, the spacing is used for the oily wastewater by the way that the bottom of the pretreatment unit is equipped with sludge hopper, the dirt
Mud hopper is used to accommodate the sludge for settling and filtering out in the oily wastewater.
Preferably, the separator includes sewage delivery device, separated for accommodating and conveying in the oily wastewater
The sewage gone out;The first liquid level sensor, first liquid are equipped between the inclined plate separator and the sewage delivery device
Level sensor through the through hole opened up at the top of the separator be inserted into the inclined plate separator and the sewage delivery device it
Between liquid in detect sewage level;The second liquid level sensor is equipped with the sewage delivery device, second liquid level passes
Sensor is inserted into the sewage delivery device through the through hole that the separator opens up at the top of the sewage delivery device
Liquid is to detect sewage level.
Preferably, Sewage baffle, the sewage are equipped between the inclined plate separator and the sewage delivery device
Corresponding and the separator top and bottom closely connect respectively on the top and bottom of baffle, and the Sewage baffle bottom is equipped with
One through hole, conveyance conduit one end are stretched into the sewage delivery device straight up after passing through the through hole, the conveyance conduit
The other end discharge sewage, the sewage is from the exit of the separator by the conveying pumped;Outside the separator
Equipped with control panel, for controlling the drain separator to run.
Preferably, the inclined plate separator includes frame and inclined plate, the inclined plate has opposite two sides, simultaneously for
Plane, another side are corrugated surface;The plane of the inclined plate is upward, ripple is face-down and the inclined plate is fixed with the horizontal acute angle
In in the frame;The plane of the trough end of the corrugated surface of upper strata inclined plate to lower floor's inclined plate of face forms the first space, upper strata
The plane of the wave crest end of the corrugated surface of inclined plate to lower floor's inclined plate of face forms second space;First space and described second
Space alternates setting to form complete fluid passage along liquid flow direction;Oily wastewater is cut from the vertical of the corrugated surface
Face shape is that rectangular side enters, and forms turbulent flow when flowing through the fluid passage, the oil droplet in the oily wastewater is in institute
State and be intercepted at the first space, water droplet is flowed out by the fluid passage, realizes water-oil separating.
Preferably, in the inclined plate separator, trough end to the lower floor of the corrugated surface of the upper strata inclined plate
First vertical range of the plane of inclined plate is 1mm-8mm;The wave crest end of the corrugated surface of the upper strata inclined plate is to lower floor's inclined plate
The second vertical range of plane be 15mm-30mm;
The frame includes the connector of two side plates being oppositely arranged and fixed side panel;The inclined plate passes through fixing piece
It is fixed in the frame, the fixing piece is U-type groove, and the notch of U-type groove is opposite on two side plates;The U-type groove is described
Setting direction on side plate is from the horizontal by 15 ° of -45 ° of angles.
Preferably, first vertical range is 1mm-5mm, second vertical range is 15mm-25mm;The U
Setting direction of the type groove on the side plate is from the horizontal by 20 ° of -30 ° of angles.
Preferably, the angle that two plate faces of trough are formed on the corrugated surface is 60 ° -120 °, on the corrugated surface
The angle for forming two plate faces of wave crest is 60 ° -120 °;Horizontal distance phase on the corrugated surface between two neighboring wave crest
Deng.
Preferably, the angle that two plate faces of the trough are formed on the corrugated surface is 90 °, shape on the corrugated surface
Angle into two plate faces of the wave crest is 90 °;The length of the inclined plate is 0.5m-1m, width 0.5m-1m, it is described tiltedly
The shape of plate is square, and the quantity of the inclined plate is 5-20.
Preferably, the cross sectional shape of the vertical direction of described inclined plate a side forms for peak line and wave, it is described
The cross sectional shape of the vertical direction of another side of inclined plate is rectangle, and described a side and another side are intersected;It is described oblique
The material of plate is polyvinyl chloride;The plane of the inclined plate passes through oxidation processes.
The utility model compared with prior art, has the following advantages:
The surface area of the inclined plate separator of the utility model is three times of traditional inclined plate separator surface area, this practicality
The separative efficiency of new inclined plate separator is far above traditional inclined plate separator, in unit volume, the utility model
The increase of inclined plate surface area after, it can be achieved that particle diameter is the separation of more than 40 microns oil droplets, the inclined plate separator of the utility model
The increase of inclined plate surface area, but overall volume diminishes, and convenient operation, reduces cost.
After the oily wastewater separator that oily wastewater passes through the utility model, sludge is received at pretreatment unit by sedimentation
Receive, oil is isolated in inclined plate separator and floated up in oil groove, and the sewage isolated is discharged through sewage delivery device.
The separator of the utility model separates the oil droplet that particle diameter is more than 40 microns, and oil removal rate is higher, small, separation
Area is big, service life 5-8.
The oily wastewater separator of the utility model and traditional separator structure are entirely different, separating effect and efficiency
Greatly improve, belong to innovation research in this area, have great application prospect and very big economic interests.
Embodiment 1
As shown in figs 1 to 6, a kind of oily wastewater separator 1, above-mentioned separator one end is at least provided with for oily wastewater
The import 201 of entrance, at least provided with the outlet 501 discharged for sewage on the housing of the above-mentioned separator other end;From it is above-mentioned into
Mouthfuls 201 to above-mentioned outlet 501, is equipped with successively in above-mentioned separator:Pretreatment unit 2, above-mentioned contains greasy dirt for settling and storing
Sludge in water;Inclined plate separator 3, its top and bottom are closely connected with the top of above-mentioned separator and bottom respectively, above-mentioned
Inclined plate separator is used for water-oil separating;Above-mentioned separator is equipped with above-mentioned 3 top end of inclined plate separator to be used to receive and hold
The oily oil groove 10 that above-mentioned inclined plate separator of receiving is isolated;Above-mentioned outlet 501 is connected with delivery pump 6, for by above-mentioned oil-containing
Sewage in sewage is extracted out from above-mentioned separator.
As the preferred of above-described embodiment, above-mentioned inclined plate separator 3 includes frame 301 and inclined plate 303, above-mentioned inclined plate
303 have opposite two sides, are simultaneously plane 3031, and another side is corrugated surface 3032;The plane 3031 of above-mentioned inclined plate upward,
Ripple is face-down and above-mentioned inclined plate 303 is fixed in said frame 301 with the horizontal acute angle;The ripple of the corrugated surface of upper strata inclined plate
The plane of Gu Duan to lower floor's inclined plate of face forms the first space 3033, under wave crest end to the face of the corrugated surface of upper strata inclined plate
The plane of layer inclined plate forms second space 3034;Above-mentioned first space 3033 and above-mentioned second space 3034 are along liquid flow direction
Setting is alternateed to form complete fluid passage;Oily wastewater from the vertical cross-section shape of above-mentioned corrugated surface be rectangular one
Side enters, and forms turbulent flow when flowing through above-mentioned fluid passage, and the oil droplet in above-mentioned oily wastewater is intercepted at above-mentioned first space,
Water droplet is flowed out by above-mentioned fluid passage, realizes water-oil separating.
As the preferred of above-described embodiment, above-mentioned pretreatment unit 2 includes input duct 203, splashing separator disk 202 and dirt
Mud hopper 204, above-mentioned input duct 203 are stretched into above-mentioned pretreatment unit 2 through above-mentioned import 201, above-mentioned splashing separator disk
202 top is connected with the top shell of above-mentioned separator, and above-mentioned splashing separator disk is arranged in above-mentioned pretreatment unit vertically, on
Stating the bottom of splashing separator disk and the bottom of above-mentioned separator has a spacing, above-mentioned spacing for above-mentioned oily wastewater by, on
The bottom for stating pretreatment unit is equipped with sludge hopper, and above-mentioned sludge hopper is used to accommodate the dirt for settling and filtering out in above-mentioned oily wastewater
Mud.
As the preferred of above-described embodiment, above-mentioned separator includes sewage delivery device 5, for accommodating and conveying above-mentioned contain
The sewage isolated in oily water;The first level sensing is equipped between above-mentioned inclined plate separator and above-mentioned sewage delivery device
Device, the through hole that above-mentioned first liquid level sensor is opened up through above-mentioned separator top are inserted into above-mentioned inclined plate separator and above-mentioned dirt
To detect sewage level in liquid between water conveying device;The second liquid level sensor is equipped with above-mentioned sewage delivery device, on
State the second liquid level sensor and be inserted into above-mentioned dirt through the through hole that above-mentioned separator opens up at the top of above-mentioned sewage delivery device
Liquid is to detect sewage level in water conveying device.
Sewage is equipped with as the preferred of above-described embodiment, between above-mentioned inclined plate separator and above-mentioned sewage delivery device to keep off
Plate 4, corresponding and above-mentioned separator top and bottom closely connect respectively for the top and bottom of above-mentioned Sewage baffle, above-mentioned sewage
Baffle bottom is equipped with a through hole, and conveyance conduit one end is stretched into above-mentioned sewage delivery device straight up after passing through above-mentioned through hole,
The other end discharge sewage of above-mentioned conveyance conduit, above-mentioned sewage is from the exit of above-mentioned separator by above-mentioned conveying pumped;On
State and be equipped with control panel outside separator, for controlling above-mentioned drain separator to run.
As the preferred of above-described embodiment, the plane at the trough end of the corrugated surface of above-mentioned upper strata inclined plate to above-mentioned lower floor's inclined plate
The first vertical range be 1mm-8mm;The wave crest end of the corrugated surface of above-mentioned upper strata inclined plate to above-mentioned lower floor's inclined plate plane
Two vertical ranges are 15mm-30mm;Above-mentioned vertical range be according to the density of oily wastewater it is different from viscosity and institute it is to be separated
Oil droplet size different designs;The utility model designs above-mentioned distance according to oily wastewater to be processed, main purpose be in order to
Oil droplet of the particle separation diameter more than 40 microns, is increased to more than 100-150 microns by 40 microns of oil droplet coalescence, reaches oil droplet
Float the buoyancy needed;Preferably, above-mentioned first vertical range is 1mm-5mm, and above-mentioned second vertical range is 15mm-25mm;
It is further preferred that above-mentioned first vertical range is 1mm-3mm, above-mentioned second vertical range of stating is 15-20mm, preferred using this
Size, is to improve water-oil separating efficiency and separate oil droplet of the particle diameter more than 40 microns as far as possible.
As the preferred of above-described embodiment, the material of above-mentioned inclined plate is polyvinyl chloride, and pvc material is easier to adsorb
Oil droplet, i.e., easily hang oil, is conducive to oil droplet convergence increase;The plane of above-mentioned inclined plate passes through oxidation processes, by oxidation processes
Pvc material is further easier absorption oil droplet.
As the preferred of above-described embodiment, said frame includes the connection of two side plates and fixed side panel being oppositely arranged
Part;Above-mentioned inclined plate is fixed in frame by fixing piece, and fixing piece is U-type groove, and the notch of U-type groove is opposite on two side plates;It is U-shaped
Setting direction of the groove on side plate is from the horizontal by 15 ° of -45 ° of angles.The angle is based on crude density, viscosity, containing greasy dirt
Water component and to separating effect requirement design different length fluid passage and angle;It is further preferred that this practicality is new
The inclined plate of type is inserted into above-mentioned U-type groove with 20 ° -30 ° of angle relative to horizontal direction;Above-mentioned fixing piece can also be buckle
Deng, the component that can be fixed on inclined plate on side plate, the U-type groove of the utility model design is bar shaped, U-type groove length and inclined plate
Length is identical, and the notch size of U-type groove just can be inserted inclined plate and not slide, i.e., the accommodation space in U-type groove and tiltedly
Plate thickness matches, and inclined plate quantity can be increased or decreased according to actual needs, easy to operate.
As the preferred of above-described embodiment, angle that two plate faces of above-mentioned trough are formed on above-mentioned corrugated surface is 60 °-
120 °, the utility model is designed as 90 ° according to the density and viscosity of oil water mixture to be processed, preferably angle;Above-mentioned ripple
The angle that two plate faces of above-mentioned wave crest are formed on face is 60 ° of -120 ° of the utility model according to oil water mixture to be processed
Density and viscosity, preferably wave crest angle are 90 °.
As the preferred of above-described embodiment, above-mentioned inclined plate is integral, and is simultaneously plane, and another side is above-mentioned flat for corrugated surface
The length of panel and corrugated-sheet paneling corresponds to identical respectively with width;It is solid between plane and corrugated surface on above-mentioned same inclined plate
Or hollow body, in order to save material and mitigate the weight of separator, convenient operation, the same inclined plate of the utility model
On plane and corrugated surface between be hollow body.
As the preferred of above-described embodiment, the cross sectional shape of the vertical direction of above-mentioned inclined plate a side is peak line and wave
Line forms, and the cross sectional shape of the vertical direction of above-mentioned another side of inclined plate is rectangle, above-mentioned a side and above-mentioned another side
It is intersecting.
As the preferred of above-described embodiment, the horizontal distance on above-mentioned wave between two neighboring wave crest is equal;Work as institute
The density of oily wastewater to be processed and viscosity are bigger, and the horizontal distance on above-mentioned wave between two neighboring wave crest is bigger,
It is on the contrary.
As the preferred of above-described embodiment, a length of 0.5m-1m of above-mentioned inclined plate, width 0.5m-1m, the shape of inclined plate is just
It is square;The quantity of inclined plate is 5-20;The length and width of inclined plate can be designed with, shape and quantity according to actual needs, such as may be used
Designed according to the treating capacity of oily wastewater.
As shown in Fig. 2-Fig. 6, the two sides of the utility model inclined plate is different, is simultaneously plane, and another side is corrugated surface, is formed
First space (narrow passage) and second space (fat pipe), above-mentioned first space and above-mentioned second space are in the horizontal direction (tiltedly
Horizontal direction when plate level is placed) fluid course of setting is alternateed, width-narrow-wide-narrow combination of the fluid course is set
Meter forms multiple turbulent flow to flowing into oily wastewater therein, and the formation of the turbulent flow adds the machine that oil droplet collides in oily wastewater
Meeting, and then add small particle oil droplet and converge the chance to form big particle diameter oil droplet, after big particle diameter oil droplet increases to a certain extent
First intercepted by second space (narrow passage) and stop flow forward, buoyancy increases and then shakes off inclined plate surface beam after oil droplet size increase
Binding force, spins off from inclined plate and passes through fluid course to floating combinate form into target oil reservoir, hydrone, it is thus achieved that containing
Oil and the preferable separating effect of water in oily water.
After the separator that oily wastewater passes through the utility model, sludge goes out in pretreatment unit to be stored by sedimentation, and oil exists
Inclined plate separator is isolated and floated up in oil groove, and the sewage isolated is discharged through sewage delivery device;The utility model
Separator separates the oil droplet that particle diameter is more than 40 microns, and oil removal rate is higher, small, and separating area is big, service life 5-8
Year.The oily wastewater separator of the utility model and traditional separator structure are entirely different, and separating effect and efficiency are significantly
Improve, belong to innovation research in this area, have great application prospect and very big economic interests.
In the utility model, the preparation process of inclined plate, oxidation processing technique are the prior art.
Water-oil separating processing is carried out to oily wastewater using the oily wastewater separator of the utility model, concrete application is for example
Under.
Application examples 1
The oily wastewater of A sewage treatment plants is handled, after testing, oil droplet size about exists in untreated preceding above-mentioned oily wastewater
280-310 μm or so, oil content 1337.94mg/L, suspension content 826.30mg/L;
Above-mentioned oily wastewater enters from the import of the oily wastewater separator (as shown in Figure 1) of the utility model, through pre- place
After managing device separated sludge, and separate oily and water, oil through inclined plate separator and float up to oil groove, sewage enters sewage delivery device
By conveying pumped;Sample detecting is carried out to the sewage after oil removing, after testing, the Oil in Sewage Water drop particle diameter isolated about exists
42-60 μm or so, oil content drops to 280-310mg/L or so, and suspension content drops to 89-92mg/L;
Wherein, inclined plate angle with horizontal plane is 20 °, and the angle that two plate faces of trough are formed on corrugated surface is 90 °, first
Vertical range is 3mm, and the second vertical range is 18mm, and the plane of inclined plate passes through oxidation processes, inclined plate long 0.8m, wide 0.8m, shape
Shape is square, and inclined plate quantity is 15.
Application examples 2
The oily wastewater of B sewage treatment plants is handled, after testing, oil droplet size about exists in untreated preceding above-mentioned oily wastewater
290-330 μm or so, oil content 9766.03mg/L, suspension content 4248.1mg/L;
Above-mentioned oily wastewater enters from the import of the oily wastewater separator (as shown in Figure 1) of the utility model, through pre- place
After managing device separated sludge, and separate oily and water, oil through inclined plate separator and float up to oil groove, sewage enters sewage delivery device
By conveying pumped;Sample detecting is carried out to the sewage after oil removing, after testing, the Oil in Sewage Water drop particle diameter isolated is about
45-63 μm, oil content drops to 501.47mg/L, and suspension content is reduced to 389.78mg/L;
Wherein, inclined plate angle with horizontal plane is 30 °, and the angle that two plate faces of trough are formed on corrugated surface is 90 °, first
Vertical range is 2mm, and the second vertical range is 20mm, and the plane of inclined plate passes through oxidation processes, inclined plate long 1m, wide 1m, and shape is
Square, inclined plate quantity are 10.
Application examples 3
The oily wastewater of C sewage treatment plants is handled, after testing, oil droplet size about exists in untreated preceding above-mentioned oily wastewater
223-289 μm or so, oil content 12351.78mg/L, suspension content 6509.24mg/L;
Above-mentioned oily wastewater enters from the import of the oily wastewater separator (as shown in Figure 1) of the utility model, through pre- place
After managing device separated sludge, and separate oily and water, oil through inclined plate separator and float up to oil groove, sewage enters sewage delivery device
By conveying pumped;Sample detecting is carried out to the sewage after oil removing, after testing, the Oil in Sewage Water drop particle diameter isolated is about
39-58 μm, oil content drops to 549.46mg/L, and suspension content is reduced to 498.12mg/L;
Wherein, inclined plate angle with horizontal plane is 15 °, and the angle that two plate faces of trough are formed on corrugated surface is 90 °, first
Vertical range is 4mm, and the second vertical range is 23mm, and the plane of inclined plate passes through oxidation processes, inclined plate long 0.5m, wide 0.5m, shape
Shape is square, and inclined plate quantity is 20.
By above application example 1-3, before oily waste water treatment with the oil droplet size after processing, oil content and suspension content
Understand, the inclined plate separator of the utility model can carry out water-oil separating to oily wastewater, and separating effect is preferable, Ke Yishi
Existing separation of the oil droplet size more than 40 microns.
Part, those skilled in the art can not select from the prior art to the greatest extent in the utility model embodiment.
Disclosed above is only specific embodiment of the present utility model, but the scope of protection of the utility model is not limited to
In this, any one skilled in the art can readily occur in change in the technical scope that the utility model discloses
Or replace, it should be covered within the scope of the utility model.Therefore, the scope of protection of the utility model should be with above-mentioned power
The protection domain that profit requires.