CN110697837A - Overflow type oil-liquid separator - Google Patents
Overflow type oil-liquid separator Download PDFInfo
- Publication number
- CN110697837A CN110697837A CN201910903240.5A CN201910903240A CN110697837A CN 110697837 A CN110697837 A CN 110697837A CN 201910903240 A CN201910903240 A CN 201910903240A CN 110697837 A CN110697837 A CN 110697837A
- Authority
- CN
- China
- Prior art keywords
- oil
- overflow
- separation
- plate
- overflow plate
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 91
- 238000000926 separation method Methods 0.000 claims abstract description 101
- 238000005452 bending Methods 0.000 claims abstract description 16
- 238000000034 method Methods 0.000 claims description 9
- 238000005273 aeration Methods 0.000 claims description 7
- 238000001802 infusion Methods 0.000 claims description 4
- 238000005192 partition Methods 0.000 claims description 4
- 230000001154 acute effect Effects 0.000 claims description 2
- 239000003921 oil Substances 0.000 description 79
- 239000002699 waste material Substances 0.000 description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 239000003795 chemical substances by application Substances 0.000 description 7
- 239000002173 cutting fluid Substances 0.000 description 7
- 238000004519 manufacturing process Methods 0.000 description 7
- 238000013461 design Methods 0.000 description 6
- 238000005238 degreasing Methods 0.000 description 5
- 238000004512 die casting Methods 0.000 description 5
- 238000004581 coalescence Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 238000001914 filtration Methods 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000009825 accumulation Methods 0.000 description 2
- 230000004888 barrier function Effects 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000005188 flotation Methods 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 239000003973 paint Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 239000002199 base oil Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000013527 degreasing agent Substances 0.000 description 1
- 238000005237 degreasing agent Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001962 electrophoresis Methods 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 239000012510 hollow fiber Substances 0.000 description 1
- 239000010720 hydraulic oil Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 239000008206 lipophilic material Substances 0.000 description 1
- 230000001050 lubricating effect Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000005555 metalworking Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 238000000053 physical method Methods 0.000 description 1
- 230000003449 preventive effect Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/24—Treatment of water, waste water, or sewage by flotation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/16—Nature of the water, waste water, sewage or sludge to be treated from metallurgical processes, i.e. from the production, refining or treatment of metals, e.g. galvanic wastes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
- C02F2201/007—Modular design
Abstract
The invention provides an overflow oil-liquid separation device, which comprises a container, a first oil-liquid separator and a second oil-liquid separator, wherein the container is provided with an inlet, a first outlet and a second outlet; the separator divides the interior of the container into a separation area, a liquid discharge area and an oil discharge area; at least two oil separation plates are sequentially arranged in the separation area; the upper part of the oil baffle plate is provided with an inclined part facing the liquid discharge area; the first overflow plate is arranged in the separation area and is positioned between the oil separation plate and the liquid discharge area; the second overflow plate is arranged in an area enclosed by the first overflow plate and the side wall of the separation area; the third outlet is arranged on the side wall and is positioned between the first overflow plate and the second overflow plate; the fourth outlet is arranged on the side wall of an area enclosed by the second overflow plate and the side wall and is communicated with the area and the oil discharge area; one end of the first bending pipe is communicated with the third outlet, and the other end of the first bending pipe is positioned in the liquid discharge area and bends upwards. The invention has the advantages of high separation efficiency and the like.
Description
Technical Field
The invention relates to liquid separation, in particular to an overflow oil-liquid separation device.
Background
The cutting fluid is a metal working fluid used for cooling and lubricating metal in cutting, grinding and other processes. They are of various kinds and complicated in composition, and usually contain a base oil, an emulsifier, a rust preventive, and the like. Cutting fluids (mainly water-based cutting fluids) often have problems of miscellaneous oil, particles and the like in use. The miscellaneous oil is mainly brought by a workpiece or leaked from hydraulic oil and guide rail oil of a machine tool. The traditional machine tool is operated by self-carrying oil-water separation, a steel belt oil remover is used for separating oil from used cutting fluid, but the treatment speed is low and the effect is limited, so that a thick oil layer is suspended on the surface of the liquid, and the performance of the cutting fluid is influenced by breeding microorganisms for a long time.
The release agent is an essential auxiliary material in the die-casting production, in the die-casting production process, in order to prolong the service life of a die cavity and enable the die-casting piece to be smoothly demoulded, the surface of the die-casting piece is smooth and clean, the outline is clear and complete, the release agent is required to be sprayed on the die, a large amount of release agent is sprayed on the die in the die-casting production, part of the release agent is evaporated at high temperature and is adsorbed on the die for consumption, and most of the release agent directly flows into the lower part of the die after being used once to become oil-containing waste liquid, and the oil-containing waste liquid is generally collected.
The degreasing process is a basic process of an automobile coating pretreatment process, and after a white automobile body is welded, a lot of dirty oil including cooling oil, stretch-proofing oil, antirust oil and the like exists on the inner surface, the outer surface and the inner cavity of the automobile body. Problems occur in the degreasing process, which can affect the quality of the electrophoretic paint and further affect the adhesive force and corrosion resistance of the paint film. Along with the increasing of the vehicle passing amount on a production line, the oil content of degreasing fluid is increased, an electrophoresis tank which is not cleaned by dirty oil treatment is polluted, and even a coating workshop stops production and stops working, so that the degreasing tank fluid needs to be taken out for oil-water separation operation.
The purification and reuse treatment of the cutting fluid, the release agent and the degreasing agent can save the production and processing cost on one hand, and can reduce the discharge amount of dangerous wastes on the other hand, thereby realizing green and clean production. The main purpose of the purification and reuse treatment is to separate the mixed oil mixed in the oil, and common oil-water separation methods include a physical separation method and a chemical separation method, wherein the physical method is to remove the oil mixed in the water by the density difference or adsorption and filtration of the oil and the water, and the main methods include a heating separation method, a filtration separation method, an air flotation separation method, an ultrafiltration membrane separation method, a reverse osmosis separation method, a coalescence separation method, a centrifugal separation method and the like; the chemical separation method is to realize demulsification through a demulsifier, and the chemical separation method is not generally adopted because the chemical can influence the components of the liquid to be treated and increase the separation difficulty.
The following are currently common separation methods:
the disadvantages of the above separation methods are:
1. the heating separation method adopts steam or a heating device for demulsification, has simple equipment and less investment, but has poor oil removal effect and large energy consumption;
2. the gravity or air flotation separation is based on different oil-water densities or buoyancy, the method is simple, the oil removal effect is stable, but the required time is long;
3. the coalescence separation increases the oil content dispersed in water through the coarse grained material until the buoyancy is larger than the adhesion force to float, the equipment is simple, the investment is low, the service cycle of the coalescence material is long, but the coalescence filler which is not used is selected according to different oil-containing waste liquid, so the adaptability of the method is greatly reduced;
4. by utilizing the selective permeability principle of the hollow fiber membrane, the oil-water separation effect is good, but part of effective components can be removed simultaneously, the cost is high, the investment is large, and the equipment is complex and difficult to operate;
5. the oil in the solution is absorbed by a lipophilic material for filtration and separation, the effluent has good quality, the equipment is miniaturized and is simple to operate, but the equipment investment is high, and the filter bag of the filter material is difficult to regenerate;
6. the centrifugal separation method utilizes centrifugal force generated by rapid rotation to enable water with high density to flow outwards along a circular path, and oil with low density is thrown to an inner ring and gathers into large oil droplets to float and separate, but the daily maintenance is difficult, and the effective components of the liquid to be treated can be damaged.
Disclosure of Invention
In order to overcome the defects in the prior art, the invention provides the overflow oil-liquid separation device which is high in separation efficiency and simple in structure.
The purpose of the invention is realized by the following technical scheme:
an overflow oil separator comprising a vessel having an inlet, a first outlet, and a second outlet; the overflow type oil-liquid separation device further comprises:
a partition dividing the interior of the vessel into a separation zone, a drain zone, and an oil drain zone; the first outlet is communicated with the liquid discharge area and the outside, and the second outlet is communicated with the oil discharge area and the outside;
the oil separation plates are sequentially arranged in the separation area and along the direction from the separation area to the liquid discharge area; the upper part of the oil separation plate is provided with an inclined part facing the liquid discharge area;
the first overflow plate is arranged in the separation area and is positioned between the oil separation plate and the liquid discharge area; the top end of the first overflow plate is higher than the top end of the inclined part;
the second overflow plate is arranged in an area enclosed by the first overflow plate and the side wall of the separation area; the top end of the first overflow plate is higher than the top end of the second overflow plate;
a third outlet disposed on the sidewall between the first overflow plate and the second overflow plate;
the fourth outlet is arranged on the side wall of a region enclosed by the second overflow plate and the side wall and is communicated with the region and the oil discharge region;
and one end of the first bent pipe is communicated with the third outlet, the other end of the first bent pipe is positioned in the liquid discharge area and is bent upwards, and the top end height of the first bent pipe is the same as that of the second overflow plate.
Compared with the prior art, the invention has the beneficial effects that:
1. the separation efficiency is high;
the air flotation-oil separation plate gathering-overflow-grading treatment technology is comprehensively utilized, so that the oil-liquid separation efficiency is remarkably improved;
firstly, generating 0.5-2mm bubbles in a separation zone by using an aeration unit, and floating the miscellaneous oil in the waste liquid to the liquid surface by virtue of the bubbles to form an miscellaneous oil layer;
the separation area is divided into blocks by at least two oil separation plates, and the oil and liquid of the waste liquid are separated and divided into blocks; the design of the inclined part accelerates the accumulation of the miscellaneous oil;
in addition, the first overflow plate and the second overflow plate are designed to realize the overflow of the impurity oil layer on the surface of the waste liquid; due to the design of the bulges, the miscellaneous oil has an upward oblique speed, so that the miscellaneous oil enters the area surrounded by the second overflow plate in a parabola shape and enters the oil discharge area; the sawtooth-shaped design at the top end of the second overflow plate further improves the proportion of miscellaneous oil in the liquid entering the area surrounded by the second overflow plate;
furthermore, part of the liquid entering the oil discharge area is gathered at the lower part and enters the liquid discharge area through the second bent pipe, and the second bent pipe and the second outlet are designed in height, so that the second outlet is ensured to discharge the miscellaneous oil basically; the liquid between the first overflow plate and the second overflow plate enters the liquid discharge area through the first bending pipe, and the height design of the first bending pipe and the second overflow plate ensures that the liquid entering the liquid discharge area is basically liquid instead of miscellaneous oil
In addition, the design of the inner diameter of the bent pipe, the inner diameter of the inlet and the inner diameter of the first outlet ensures the separation and timely discharge of waste liquid in the container, thereby ensuring the oil-liquid separation efficiency;
2. the structure is simple and the cost is low;
the container, the oil separation plate, the overflow plate and the bent pipe are all conventional parts, and the oil separator has a simple structure and low cost.
Drawings
The disclosure of the present invention will become more readily understood with reference to the accompanying drawings. As is readily understood by those skilled in the art: these drawings are only for illustrating the technical solutions of the present invention and are not intended to limit the scope of the present invention. In the figure:
FIG. 1 is a schematic view of a flooded oil separator according to an embodiment of the present invention;
FIG. 2 is a schematic cross-sectional view of a flooded oil separator in accordance with an embodiment of the present invention;
fig. 3 is a schematic top view of a flooded oil separator according to an embodiment of the present invention.
Detailed Description
Fig. 1-3 and the following description depict alternative embodiments of the invention to teach those skilled in the art how to make and use the invention. Some conventional aspects have been simplified or omitted for the purpose of teaching the present invention. Those skilled in the art will appreciate that variations or substitutions from these embodiments will be within the scope of the invention. Those skilled in the art will appreciate that the features described below can be combined in various ways to form multiple variations of the invention. Thus, the present invention is not limited to the following alternative embodiments, but is only limited by the claims and their equivalents.
Example 1:
fig. 1 to 3 are schematic diagrams showing the configuration of a flooded oil-liquid separator according to an embodiment of the present invention, and as shown in fig. 1 to 3, the flooded oil-liquid separator includes:
a vessel 11 having an inlet 31, a first outlet 61 and a second outlet 62;
a partition 15, the partition 15 dividing the inside of the vessel 11 into a separation zone 12, a liquid discharge zone 13, and an oil discharge zone 14; the first outlet 61 is communicated with the liquid discharge area 13 and the outside, and the second outlet 62 is communicated with the oil discharge area 14 and the outside;
a first overflow plate 51, the first overflow plate 51 being disposed in the separation zone 12 and between the oil baffle 41 and the liquid discharge zone 13; the top end of the first overflow plate 51 is higher than the top end of the inclined part;
a second overflow plate 52, the second overflow plate 52 is arranged in the area enclosed by the first overflow plate 51 and the side wall of the separation area; the top end of the first overflow plate 51 is higher than the top end of the second overflow plate 52;
a third outlet 63, the third outlet 63 being provided in the side wall between the first overflow plate 51 and the second overflow plate 52;
a fourth outlet 64, wherein the fourth outlet 64 is arranged on the side wall of the area enclosed by the second overflow plate 52 and the side wall, and is communicated with the oil drainage area;
and one end of the first bent pipe 71 is communicated with the third outlet 63, the other end of the first bent pipe 71 is positioned in the liquid discharge area 13 and is bent upwards, and the top end height of the first bent pipe 71 is the same as that of the second overflow plate 52.
In order to discharge the liquid collected at the lower part of the oil discharge area, the overflow type oil-liquid separation device further comprises:
and the second bent pipe 72 is communicated with the liquid discharge area 13 and the oil discharge area 14, one end of the second bent pipe 72, which is positioned in the liquid discharge area 13, is bent upwards, and the top end position of the second bent pipe is the same as the bottom of the second outlet 62.
In order to improve the oil-liquid separation efficiency, the side of the first overflow plate 51 facing the second overflow plate 52 is provided with a strip-shaped protrusion 53, so that the miscellaneous oil flowing obliquely downwards along the first overflow plate 51 is blocked by the protrusion 53 to obtain an obliquely upward velocity, and flies into the area enclosed by the second overflow plate 52 along the parabola.
In order to improve the oil-liquid separation efficiency, further, the overflow type oil-liquid separation device further comprises:
the infusion tube 81 is arranged at the inlet and is provided with an input end, a first output end and a second output end, wherein the interior of the input end, the first output end and the second output end are mutually communicated; the first and second outputs are disposed within the separation zone; the central axis of first output and second output with the contained angle between the part of the non-slope portion of oil removal board is zero or acute angle for the waste liquid that gets into the separation zone is not direct impact oil removal board.
In order to improve the oil-liquid separation efficiency, further, the overflow type oil-liquid separation device further comprises:
the aeration unit 21 is arranged in the separation area and is positioned at the lower part of the oil separation plate; the air inlet 22 communicates with the aeration unit 21.
In order to maintain the oil-liquid separation continuously, the inner diameter R of the first bending pipe 71 is further increased1＞R0The inner diameter R of the second bending tube 722＜R0Inner diameter R of the first outlet 613＝R0，R0Is the inner diameter of the inlet 31.
Example 2:
the overflow oil-liquid separation device according to the embodiment of the invention is applied to oil-water separation in the treatment of cutting fluid, release agent and degreasing tank liquor.
In the present application example, as shown in fig. 1 to 3, the included angle between the inclined part of the oil baffle plate 41 and the horizontal plane is 45 to 60 degrees; the first overflow plate 51 and the second overflow plate 52 are inclined from top to bottom towards the side wall of the separation area 12, the included angle between the first overflow plate 51 and the second overflow plate 52 and the horizontal plane is 45-60 degrees, and the first overflow plate 51 and the second overflow plate 52 are arranged in parallel; the side of the first overflow plate 51 facing the second overflow plate 52 is provided with a strip-shaped projection 53 extending along the horizontal direction; the top end of the second overflow plate 52 is in a sawtooth shape; the infusion tube 81 is T-shaped, two output ends are arranged in the separation area, and the central axis is parallel to the oil separation plate 41; the two aeration pipes are arranged at the bottom of the separation area, and the projections of the liquid conveying pipe in the separation area on the horizontal plane are positioned between the projections of the two aeration pipes on the horizontal plane and are not overlapped; the second bending pipe 72 is communicated with the liquid discharge area 13 and the oil discharge area 14, one end of the second bending pipe in the liquid discharge area 13 is bent upwards, and the top end position of the second bending pipe is the same as the bottom of the second outlet 62; inner diameter R of the first bending pipe 711＞R0The inner diameter R of the second bending tube 722＜R0Inner diameter R of the first outlet 613＝R0，R0Is the inner diameter of the inlet 31.
The working mode of the overflow oil-liquid separation device of the embodiment is as follows:
generating 0.5-2mm bubbles in the separation zone 12 by using the aeration unit 21;
the waste liquid enters the separation zone 12 through the liquid conveying pipe 81, and the miscellaneous oil in the waste liquid floats to the liquid surface by virtue of the bubbles, so that an miscellaneous oil layer is formed;
at least two oil separation plates 41 divide the separation area into blocks, and the oil and liquid of the waste liquid are separated and divided into blocks; the design of the inclined part accelerates the accumulation of the miscellaneous oil;
the liquid level in the separation zone 12 rises, the miscellaneous oil layer passes through the first overflow plate 51, accelerates downwards along the inclined first overflow plate 51, obtains an initial upward inclined speed after encountering the strip-shaped bulge 53, and flies into the area enclosed by the second overflow plate 52 along the parabola;
the liquid level in the area enclosed by the first overflow plate 51 and the second overflow plate 52 rises, and the upper layer of the miscellaneous oil layer crosses the second zigzag overflow plate 52, enters the area enclosed by the second overflow plate 52 and then enters the oil discharge area 14 through the fourth outlet 64;
the liquid at the lower part in the area enclosed by the first overflow plate 51 and the second overflow plate 52 enters a liquid discharge area through the third outlet 63 and the first bent pipe 71;
miscellaneous oil and a small amount of waste liquid are accumulated in the oil discharge area 14, the miscellaneous oil on the upper layer is discharged through the second outlet 62, the liquid on the lower layer enters the liquid discharge area 13 through the second bent pipe 72, and the waste liquid in the liquid discharge area 13 is discharged from the first outlet 61, so that oil-liquid separation is realized.
The benefits achieved according to the application example of the invention are: the air flotation-oil separation plate gathering-overflow-grading treatment technology is comprehensively utilized, the oil-liquid separation efficiency is obviously improved, and the whole device is simple in component and low in cost.
Claims (10)
1. An overflow oil separator comprising a vessel having an inlet, a first outlet, and a second outlet; the method is characterized in that: the overflow type oil-liquid separation device further comprises:
a partition dividing the interior of the vessel into a separation zone, a drain zone, and an oil drain zone; the first outlet is communicated with the liquid discharge area and the outside, and the second outlet is communicated with the oil discharge area and the outside;
the oil separation plates are sequentially arranged in the separation area and along the direction from the separation area to the liquid discharge area; the upper part of the oil separation plate is provided with an inclined part facing the liquid discharge area;
the first overflow plate is arranged in the separation area and is positioned between the oil separation plate and the liquid discharge area; the top end of the first overflow plate is higher than the top end of the inclined part;
the second overflow plate is arranged in an area enclosed by the first overflow plate and the side wall of the separation area; the top end of the first overflow plate is higher than the top end of the second overflow plate;
a third outlet disposed on the sidewall between the first overflow plate and the second overflow plate;
the fourth outlet is arranged on the side wall of a region enclosed by the second overflow plate and the side wall and is communicated with the region and the oil discharge region;
and one end of the first bent pipe is communicated with the third outlet, the other end of the first bent pipe is positioned in the liquid discharge area and is bent upwards, and the top end height of the first bent pipe is the same as that of the second overflow plate.
2. The overflow oil separator as claimed in claim 1, wherein: the overflow type oil-liquid separation device further comprises:
and the second bending pipe is communicated with the liquid discharge area and the oil discharge area, one end of the second bending pipe in the liquid discharge area is bent upwards, and the top end of the second bending pipe is positioned at the same position as the bottom of the second outlet.
3. The overflow oil separator as claimed in claim 1, wherein: the side of the first overflow plate facing the second overflow plate is provided with a strip-shaped bulge.
4. The overflow oil separator as claimed in claim 1, wherein: the first overflow plate and/or the second overflow plate are arranged obliquely.
5. The overflow oil separator as claimed in claim 4, wherein: the first overflow plate and the second overflow plate are arranged in parallel.
6. The overflow oil separator as claimed in claim 4, wherein: the top end of the second overflow plate is serrated.
7. The overflow oil separator as claimed in claim 1, wherein: the overflow type oil-liquid separation device further comprises:
the infusion tube is arranged at the inlet and is provided with an input end, a first output end and a second output end, and the interior of the infusion tube is communicated with the input end, the first output end and the second output end; the first and second outputs are disposed within the separation region.
8. The flooded oil separator as claimed in claim 7, wherein: and the included angle between the central axes of the first output end and the second output end and the part of the oil separation plate, which is not the inclined part, is zero or an acute angle.
9. The overflow oil separator as claimed in claim 1, wherein: the overflow type oil-liquid separation device further comprises:
and the aeration unit is arranged in the separation area and is positioned at the lower part of the oil separation plate.
10. The overflow oil separator as claimed in claim 1, wherein: the inner diameter R of the first bending pipe1＞R0The inner diameter R of the second bending pipe2＜R0Inner diameter R of said first outlet3＝R0，R0Is the inner diameter of the inlet。
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910903240.5A CN110697837A (en) | 2019-09-24 | 2019-09-24 | Overflow type oil-liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910903240.5A CN110697837A (en) | 2019-09-24 | 2019-09-24 | Overflow type oil-liquid separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110697837A true CN110697837A (en) | 2020-01-17 |
Family
ID=69196017
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910903240.5A Pending CN110697837A (en) | 2019-09-24 | 2019-09-24 | Overflow type oil-liquid separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110697837A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112588013A (en) * | 2020-11-24 | 2021-04-02 | 湖南祥柏生态环保科技有限公司 | Multi-stage oil-residue separation device |
| CN112587984A (en) * | 2020-11-24 | 2021-04-02 | 湖南祥柏生态环保科技有限公司 | Circulating filtering type oil residue separating device |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001321765A (en) * | 2000-05-17 | 2001-11-20 | Dowa Mining Co Ltd | Oil separating device |
| CN202358977U (en) * | 2011-09-06 | 2012-08-01 | 中国石油化工股份有限公司 | Device for demulsifying and un-oiling produced water by binary compound flooding |
| CN202688038U (en) * | 2012-07-03 | 2013-01-23 | 杨志江 | Air floatation type automatic oil scraping and separating device |
| KR101795002B1 (en) * | 2017-08-29 | 2017-12-01 | 주식회사 성지엔지니어링 | Oil-water separating and remediating apparatus |
| CN210944934U (en) * | 2019-09-24 | 2020-07-07 | 杭州路弘科技有限公司 | Overflow type oil-liquid separator |
-
2019
- 2019-09-24 CN CN201910903240.5A patent/CN110697837A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001321765A (en) * | 2000-05-17 | 2001-11-20 | Dowa Mining Co Ltd | Oil separating device |
| CN202358977U (en) * | 2011-09-06 | 2012-08-01 | 中国石油化工股份有限公司 | Device for demulsifying and un-oiling produced water by binary compound flooding |
| CN202688038U (en) * | 2012-07-03 | 2013-01-23 | 杨志江 | Air floatation type automatic oil scraping and separating device |
| KR101795002B1 (en) * | 2017-08-29 | 2017-12-01 | 주식회사 성지엔지니어링 | Oil-water separating and remediating apparatus |
| CN210944934U (en) * | 2019-09-24 | 2020-07-07 | 杭州路弘科技有限公司 | Overflow type oil-liquid separator |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112588013A (en) * | 2020-11-24 | 2021-04-02 | 湖南祥柏生态环保科技有限公司 | Multi-stage oil-residue separation device |
| CN112587984A (en) * | 2020-11-24 | 2021-04-02 | 湖南祥柏生态环保科技有限公司 | Circulating filtering type oil residue separating device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206457275U (en) | A kind of fiberglass integrally improves grid type oil interceptor | |
| CN101182080B (en) | Water treatment separator device | |
| CN110697837A (en) | Overflow type oil-liquid separator | |
| CN205803146U (en) | Oily waste water efficient cyclone | |
| CN111018193A (en) | Sewage treatment system based on swirler | |
| CN210944934U (en) | Overflow type oil-liquid separator | |
| CN204400653U (en) | A kind of integration air-float oil eliminator | |
| GB2275210A (en) | Regenerating of degreasing liquid | |
| CN202246207U (en) | High-efficiency float and sediment solid-liquid separation device | |
| CN207468243U (en) | Vehicular air supporting settles grease solid separation device | |
| CN110759424A (en) | Overflow type oil-liquid separation method | |
| CN211141745U (en) | Integrated liquid treatment device | |
| CN212347805U (en) | Oil-water separation device based on air floatation technology | |
| CN112777768B (en) | Multifunctional impurity-removing oil-removing filtering water tank | |
| CN212894180U (en) | Oily wastewater treatment oil interceptor | |
| CN210286942U (en) | Oil-water separation device | |
| CN209128193U (en) | A kind of high speed degreasing unit and rapidly and efficiently oil removing Airfloat filtering pond | |
| CN213049501U (en) | Oil-water separating device | |
| RU124672U1 (en) | SEWAGE TREATMENT PLANT AND TECHNOLOGICAL LIQUIDS | |
| CN113117383A (en) | Demulsification oil-water separation system and method | |
| CN201470154U (en) | On-line automatic backwash oil-water separation device | |
| CN106495366B (en) | Device and method for treating coal gasification wastewater | |
| CN110723838A (en) | Centralized liquid treatment method | |
| CN202237385U (en) | Double-stage oil-water separator | |
| CN212347803U (en) | Automatic collecting device and oil-water separating device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination |