CN207227068U - Equipment for water-oil separating - Google Patents
Equipment for water-oil separating Download PDFInfo
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- CN207227068U CN207227068U CN201720751209.0U CN201720751209U CN207227068U CN 207227068 U CN207227068 U CN 207227068U CN 201720751209 U CN201720751209 U CN 201720751209U CN 207227068 U CN207227068 U CN 207227068U
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Abstract
The utility model discloses a kind of equipment for water-oil separating, including cylinder, intake chamber, separation chamber are divided into by front baffle and rear bulkhead and go out grease chamber in cylinder, double M types coalescing-plate groups adjustable in pitch are equipped with separation chamber, it is fixed on above double M types coalescing-plate groups by fixed press strip on barrel wall, fixed press strip is equipped with handle, and bottom plate is equipped with below double M types coalescing-plate groups, string column is equipped between fixed press strip and bottom plate, string column passes through double M type coalescing-plate groups；The barrel top of intake chamber is equipped with inlet tube, and the position away from inlet tube, which is equipped with, in front baffle can make the passage that intake chamber communicates with separation chamber；The position away from passage is equipped with the secondary separation room being made of secondary separation plate and barrel in separation chamber, Gravity Separation is combined by equipment disclosed in the utility model with coalescence technology, farthest improves oil removal efficiency, good separating effect, residence time is short, and disposal ability is big.
Description
Technical field
It the utility model is related to a kind of equipment for water-oil separating.
Background technology
Oily wastewater of the Produced Liquid in oil field after three phase separator separates by settling tank, it is necessary to further settle
Separation, at present mainly there is oils existing forms in oily wastewater：(1) floating oil：Particle diameter >=100 micron, slightly take standing or half
The method of standing, you can float on the water surface and be easy to remove；(2) dispersed oil：Particle diameter is at 10 100 microns, if enough quiet
Put the time, oil droplet can also shift to the water surface, need to generally stand 12 it is small when more than, oily removal rate is more than 80%；(3) oil emulsion：
About 0.1 to 10 micron of particle diameter, has certain stability, is merely that can not separate itself and water by gravitational settling, it is necessary to through broken
It could be separated after breast or flocculation, seriously affect production.
If separating treatment is carried out, it is necessary to add flocculant, flocculation aid to the oil emulsion in oily wastewater by traditional method
And reverse demulsifier.If the sewage quantity containing oil emulsion of required processing is very big, then certainly will will consume substantial amounts of manpower, financial resources
And material resources.Oily waste water treatment technology improves at present, and biochemical treatment oily wastewater technology has been obtained for very well
Ground application, but the oil emulsion problem in settling tank does not solve also, and the biochemical treatment to sewage plant brings burden.
Utility model content
In order to solve the above technical problems, the utility model provides a kind of equipment for water-oil separating, to reach separation
Effect is good, and separative efficiency is high, and the residence time is short, the big purpose of disposal ability.
To reach above-mentioned purpose, the technical solution of the utility model is as follows：
A kind of equipment for water-oil separating, including cylinder, in the cylinder by front baffle and rear bulkhead be divided into intake chamber,
Separation chamber and go out grease chamber, double M types coalescing-plate groups adjustable in pitch, double M types coalescing-plate groups tops are equipped with the separation chamber in
It is fixed on by fixed press strip on barrel wall, the fixed press strip is equipped with handle, and bottom plate is equipped with below double M types coalescing-plate groups,
String column is equipped between the fixed press strip and bottom plate, the string column passes through double M types coalescing-plate groups；The barrel of the intake chamber
Top is equipped with inlet tube, and the position away from inlet tube is logical equipped with intake chamber can be made to be communicated with separation chamber in the front baffle
Road；The position away from passage is equipped with the secondary separation room that is made of secondary separation plate and barrel in the separation chamber, and described two
Secondary separating plate bottom is equipped with overflow pipe, and the cylinder of secondary separation room lower part is equipped with the secondary outlet pipe that can be periodically turned on, described
The cylinder lower part of separation chamber is equipped with water outlet；It is respectively equipped with out in the separation chamber positioned at the front and rear sides of double M type coalescing-plate groups
Mouth oil exit pipe one and oil exit pipe two upward, the oil exit pipe one and oil exit pipe two are L-type, the outlet of L-type be welded in after every
On plate；It is described go out grease chamber cylinder be equipped with flowline.
In such scheme, double M types coalescing-plate groups include the coalescing-plate several stacked on top together, the coalescing-plate
Coalescing-plate body including cross section for double M types, the coalescing-plate body is along longitudinal direction in wavy, pair of the coalescing-plate body
Oil slick hole is equipped with wavy wave crest along longitudinal direction on M types top, trough is equipped with raised stepped fore-set, the coalescence
Double M types bottom centers of plate body distribute sedimentation hole along the longitudinal；The back side of the coalescing-plate body is located at stepped fore-set
Lower position is equipped with stepped groove, and the side of the stepped groove is equipped with groove, the stepped fore-set front end insertion of lower floor's coalescing-plate
In the stepped groove or groove of upper strata coalescing-plate.
In such scheme, the intake chamber bottom is equipped with the silt discharge pipe that can be periodically turned on, and is located in the intake chamber
Tilted upward on inner wall below silt discharge pipe equipped with every husky plate.
In such scheme, the spout tops position of the oil exit pipe one and oil exit pipe two is less than the top of double M type coalescing-plate groups
End position.
It is described to be welded in every husky plate on cylinder in such scheme, and horizontal by 45° angle.
In such scheme, the inlet tube is L-type.
In such scheme, the cylinder body bottom is equipped with fixed groove body, and the backplane card is in fixing groove body.
Through the above technical solutions, the equipment good separating effect provided by the utility model for water-oil separating, separation effect
Rate is high, and the residence time is short, and disposal ability is big, and floor space is small, meets water-oil separating to efficient, miniaturization trend.Tool
Body surface is present：
(1) Gravity Separation farthest improves oil removal efficiency after coalescence technology is combined.
(2) horizontal stream water intake mode, increases coalescence area, and to force current to be formed special for the tortuous passageway of coalescing-plate
Fluidised form so that increase stream pearl between collision probability, promote it is small trip pearl coalescence.
(3) double M types coalescing-plate groups can carry out integral installation and dismounting by fixed press strip and string column, easy to use；
(4) spacing between double M types coalescing-plate groups can be according to the different adjustment spacing of the viscosity of separated liquid, to adapt to
The separation requirement of different viscosities liquid.
Brief description of the drawings
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described.
Fig. 1 is a kind of equipment overall structure schematic diagram for water-oil separating disclosed in the utility model embodiment；
Fig. 2 is the top view of the equipment for water-oil separating disclosed in the utility model embodiment；
Fig. 3 is the equipment inner structure schematic diagram for water-oil separating for pulling down double M type coalescing-plate groups；
Fig. 4 coalesces plate structure schematic diagram for single M types；
Fig. 5 is the top view of Fig. 4；
Fig. 6 is section plan where the stepped fore-set of the coalescing-plate disclosed in the utility model embodiment；
Fig. 7 is A-A diagrammatic cross-sections in Fig. 4；
Fig. 8 is the schematic cross-section that the stepped fore-set of next strata knot tying is inserted into the stepped groove of last layer coalescing-plate；
Fig. 9 is part B enlarged diagram in Fig. 8；
The schematic cross-section of the groove of the stepped fore-set insertion last layer coalescing-plate of the next strata knot tyings of Figure 10；
Figure 11 is C portion enlarged diagram in Figure 10；
Figure 12 is fixed press strip, bottom plate and string rod structure schematic diagram.
In figure, 1, coalescing-plate body；2nd, oil slick hole；3rd, stepped fore-set；4th, sedimentation hole；5th, stepped groove；6th, groove；7th, it is solid
Level pressure bar；8th, bottom plate；9th, tabletting；10th, double M types coalescing-plate groups；11st, cylinder；12nd, front baffle；13rd, rear bulkhead；14th, secondary separation
Plate；15th, oil exit pipe one；16th, oil exit pipe two；17th, every husky plate；18th, water outlet；19th, inlet tube；20th, flowline；21st, it is secondary go out
Water pipe；22nd, intake chamber；23rd, separation chamber；24th, grease chamber is gone out；25th, secondary separation room；26th, silt discharge pipe；27th, passage；28th, overflow
Flow tube；29th, string column；30th, handle；31st, locking cap；32nd, fixed groove body.
Embodiment
The following is a combination of the drawings in the embodiments of the present utility model, and the technical scheme in the embodiment of the utility model is carried out
Clearly and completely describe.
The utility model provides a kind of equipment for water-oil separating, and as shown in Figure 1 to Figure 3, the equipment is by gravitational method
It is combined with coalescence technology, improves hydraulics, enhances the state of the water-oil separating of oil emulsion.
The equipment for water-oil separating as shown in Figure 1 to Figure 3, including cylinder 11, in cylinder 11 by front baffle 12 and after
Partition plate 13 is divided into intake chamber 22, separation chamber 23 and goes out grease chamber 24, and double M types coalescing-plate groups adjustable in pitch are equipped with separation chamber 23
10, double tops of M types coalescing-plate group 10 are fixed on 11 wall of cylinder by fixed press strip 7, and fixed press strip 7 is equipped with handle 30, double M
The lower section of type coalescing-plate group 10 is equipped with bottom plate 8, and string column 29 is equipped between fixed press strip 7 and bottom plate 8, and as shown in figure 12, string column 29 is worn
Double M types coalescing-plate groups 10 are crossed, upper end is fixed on fixed press strip 7 by locking cap, and bottom is welded on bottom plate 8；Fixed press strip 7
For concave structure, centre is pressed in double M type coalescing-plates groups 10, and both ends are pressed in front baffle 12 and rear bulkhead 13, and are fixed on cylinder
On 11 inner wall of body.11 bottom of cylinder is equipped with fixed groove body 32, and bottom plate 8 is stuck in fixed groove body 32.
The barrel top of intake chamber 22 is equipped with L-type inlet tube 19, and bottom is equipped with the silt discharge pipe 26 that can be periodically turned on, into
Tilted upward in liquid chamber 22 on the inner wall of the lower section of silt discharge pipe 26 equipped with every husky plate 17, cylinder 11 is welded in every husky plate 17
On, and horizontal by 45° angle.
The position away from inlet tube 19, which is equipped with, in front baffle 12 can make the passage 27 that intake chamber 22 communicates with separation chamber 23；
The position away from passage 27 is equipped with the secondary separation room 25 that is made of secondary separation plate 14 and barrel in separation chamber 23, secondary point
Overflow pipe 28 setting up and down is equipped with from 14 bottom of plate, the cylinder of 25 lower part of secondary separation room is secondary equipped with that can periodically turn on
Outlet pipe 21.
The cylinder lower part of separation chamber 23 is equipped with water outlet 18, and front and rear the two of double M type coalescing-plates groups 10 are located in separation chamber 23
Side is respectively equipped with opening up oil exit pipe 1 and oil exit pipe 2 16, and oil exit pipe 1 and oil exit pipe 2 16 are L-type, L-type
Outlet be welded on rear bulkhead 13；The spout tops position of oil exit pipe 1 and oil exit pipe 2 16 is less than double M type coalescing-plate groups
10 apical position.The cylinder for going out grease chamber 24 is equipped with flowline 20.
Double M types coalescing-plate groups 10 include the coalescing-plate 60 stacked on top together, as shown in Fig. 4 to Figure 11, coalescing-plate
Including the coalescing-plate body 1 that cross section is double M types, as shown in fig. 7, coalescing-plate body 1 is in wavy, coalescing-plate body along longitudinal direction
Oil slick hole 2 is equipped with wavy wave crest along longitudinal direction on 1 double M types tops, string column 9 passes through oil slick hole 2；Trough is equipped with convex
The stepped fore-set 3 risen, double M types bottom centers of coalescing-plate body 1 distribute sedimentation hole 4 along the longitudinal (shown in Fig. 5)；Such as Fig. 7
Shown, the lower position that the back side of coalescing-plate body 1 is located at stepped fore-set 3 is equipped with stepped groove 5, and the side of stepped groove 5 is set
Fluted 6,3 front end of stepped fore-set of lower floor's coalescing-plate is inserted into the stepped groove 5 or groove 6 of upper strata coalescing-plate.
Oil slick hole 2 is uniformly arranged on the wave crest of coalescing-plate body 1, and stepped fore-set 3 is uniformly arranged on coalescing-plate body 1
Trough on, sedimentation hole 4 is uniformly distributed on double M types bottom center lines of coalescing-plate body 1.
A stepped fore-set 3 is equipped with coalescing-plate at spacing intervals, as the supporter between plate, on stepped top
The lower section of column 3 is equipped with stepped groove 5, and the side of stepped groove 5 is additionally provided with groove 6,3 front end of the stepped fore-set insertion of lower floor's coalescing-plate
In the stepped groove 5 or groove 6 of upper strata coalescing-plate, plate group can be held together.Into during assembling between andante, to coalescing-plate
Group is adjusted, to adapt to the requirement of conveying different viscosities grease.When conveying low viscosity grease, the rank of next laminate upper surface
Scalariform fore-set 3 is corresponded in the stepped groove 5 of insertion last layer plate lower surface, and as shown in Figure 8 and Figure 9, plate spacing is H at this time；When defeated
When sending high viscosity grease, after 180 ° of the direction horizontal rotation of next laminate, the stepped fore-set 3 of next laminate upper surface, which corresponds to, to be inserted
In the groove 6 for entering last layer plate lower surface, as shown in Figure 10 and Figure 11, plate spacing is H+A at this time；Completed with this to different viscosities
The conveying requirement of grease.
The board selection polypropylene of coalescing-plate, adds bone meal, to polypropylene board in polypropylene board manufacturing process
Tow sides are modified processing.Modified mechanism is hydroxyl in the positive and negative grafting of basic unit, makes it have strong oleophilic drainage
Characteristic, so as to realize emulsified oil droplet be demulsified after grease rapid coalescence.
Specific separation process is as follows：
Oil emulsion is inputted in the intake chamber 22 of cylinder 11 with suitable flow by inlet tube 19；Into the emulsification of cylinder 11
Oil is encountered every husky plate 17 during flowing downward, and under the action of husky plate 17, along every husky 17 direction of plate to the left
Top is flowed, so that avoiding oil emulsion from directly flowing to the particulate matters such as 11 bottom of cylinder, silt can sink under the action of husky plate
Product arrives cylinder body bottom, can periodically open silt discharge pipe 26 and discharge cylinder 11.
Passage 27 of the oil emulsion Jing Guo front baffle 12 into intake chamber 22 enters in separation chamber 23, oil emulsion lateral flow
Into M type coalescing-plates group 10, the surface of coalescing-plate is waveform, its tortuous passageway provided and very big coalescence surface, production
The current similar to sine wave have been given birth to, has made surface collision during tiny oil droplets bottom horizontal flow sheet in coalescing-plate, coalescence, works as oil droplet
When diameter coalescence is to certain particle diameter, oil droplet starts to float by the oil slick hole on 10 top of M type coalescing-plates group, and oil content is relatively low to be mixed
Liquid is closed to start to sink by the sedimentation hole 1 and sedimentation hole 26 of 10 bottom of M type coalescing-plates group.Oil droplet by coalescing-plate layer by layer by
The top of cylinder 11 is gradually floated up to, the relatively low mixed liquor of oil content sinks down into 11 bottom of cylinder by coalescing-plate layer by layer, from water outlet
18 discharges, floating up to the oil droplet at the top of cylinder 11 can enter grease chamber 24 by oil exit pipe 1 and oil exit pipe 2 16, then from
Flowline 20 is discharged outside cylinder 11, carries out the first time recycling of oil droplet.
The relatively low mixed liquor of 11 bottom oil content of cylinder is secondary into being formed by secondary separation plate 14 via overflow pipe 28
Separation chamber 25, under the effect of gravity, mixed liquor form layering, and the of a relatively high mixed liquor of oil content is located at top, and oil content
Relatively lower mixed liquor is located at lower part, periodically opens secondary outlet pipe 21, and the low water of oil content is discharged to outdoor, formation grease
Second separation.
The foregoing description of the disclosed embodiments, enables professional and technical personnel in the field to realize or new using this practicality
Type.A variety of modifications to these embodiments will be apparent for those skilled in the art, determine herein
The General Principle of justice can be realized in other embodiments without departing from the spirit or scope of the present utility model.Cause
This, the utility model is not intended to be limited to the embodiments shown herein, and is to fit to and principles disclosed herein
The most wide scope consistent with features of novelty.
Claims (7)
1. a kind of equipment for water-oil separating, it is characterised in that including cylinder, by front baffle and rear bulkhead point in the cylinder
Into intake chamber, separation chamber and go out grease chamber, double M types coalescing-plate groups adjustable in pitch, double M types coalescences are equipped with the separation chamber
It is fixed on above plate group by fixed press strip on barrel wall, the fixed press strip is equipped with handle, is set below double M types coalescing-plate groups
There is bottom plate, string column is equipped between the fixed press strip and bottom plate, the string column passes through double M types coalescing-plate groups；The feed liquor
The barrel top of room is equipped with inlet tube, and the position away from inlet tube, which is equipped with, in the front baffle can make intake chamber and separation chamber's phase
Logical passage；The position away from passage is equipped with the secondary separation room being made of secondary separation plate and barrel in the separation chamber,
The secondary separation plate bottom is equipped with overflow pipe, and the cylinder of secondary separation room lower part is equipped with the secondary water outlet that can be periodically turned on
Pipe, the cylinder lower part of the separation chamber is equipped with water outlet；Positioned at the front and rear sides difference of double M type coalescing-plate groups in the separation chamber
Equipped with opening up oil exit pipe one and oil exit pipe two, the oil exit pipe one and oil exit pipe two are L-type, and the outlet of L-type is welded
In on rear bulkhead；It is described go out grease chamber cylinder be equipped with flowline.
A kind of 2. equipment for water-oil separating according to claim 1, it is characterised in that double M types coalescing-plate groups
Including the coalescing-plate several stacked on top together, the coalescing-plate includes the coalescing-plate body that cross section is double M types, described poly-
Knot tying body is in wavy along longitudinal direction, is equipped with double M types tops of the coalescing-plate body along longitudinal direction on wavy wave crest
Oil slick hole, trough are equipped with raised stepped fore-set, and it is heavy that double M types bottom centers of the coalescing-plate body distribute along the longitudinal
Hole drops；The lower position that the back side of the coalescing-plate body is located at stepped fore-set is equipped with stepped groove, and the one of the stepped groove
Side is equipped with groove, and the stepped fore-set front end of lower floor's coalescing-plate is inserted into the stepped groove or groove of upper strata coalescing-plate.
3. a kind of equipment for water-oil separating according to claim 1, it is characterised in that intake chamber bottom is equipped with
The silt discharge pipe that can be periodically turned on, tilts upward equipped with every sand on the inner wall below silt discharge pipe in the intake chamber
Plate.
4. a kind of equipment for water-oil separating according to claim 1, it is characterised in that the oil exit pipe one and oil extraction
The spout tops position of pipe two is less than the apical position of double M type coalescing-plate groups.
5. a kind of equipment for water-oil separating according to claim 3, it is characterised in that described to be welded in cylinder every husky plate
On body, and horizontal by 45° angle.
6. a kind of equipment for water-oil separating according to claim 1, it is characterised in that the inlet tube is L-type.
7. a kind of equipment for water-oil separating according to claim 1, it is characterised in that the cylinder body bottom is equipped with solid
Determine groove body, the backplane card is in fixing groove body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720751209.0U CN207227068U (en) | 2017-06-27 | 2017-06-27 | Equipment for water-oil separating |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720751209.0U CN207227068U (en) | 2017-06-27 | 2017-06-27 | Equipment for water-oil separating |
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| Publication Number | Publication Date |
|---|---|
| CN207227068U true CN207227068U (en) | 2018-04-13 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720751209.0U Active CN207227068U (en) | 2017-06-27 | 2017-06-27 | Equipment for water-oil separating |
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| CN (1) | CN207227068U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111069245A (en) * | 2019-12-26 | 2020-04-28 | 浙江华力环境科技有限公司 | Kitchen waste treatment process |
-
2017
- 2017-06-27 CN CN201720751209.0U patent/CN207227068U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111069245A (en) * | 2019-12-26 | 2020-04-28 | 浙江华力环境科技有限公司 | Kitchen waste treatment process |
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Address after: No.28, Zhejiang Road, Shinan District, Qingdao City, Shandong Province Patentee after: Shandong Ocean Instrument Technology Center Co.,Ltd. Address before: No. 28, Zhejiang Road, Southern District, Shandong, Qingdao, Shandong Patentee before: SHANDONG PROVINCE OCEANOGRAPHIC INSTRUMENTATION TECHNOLOGY CENTER |