CN210419359U - Water-oil-sand three-phase separation device - Google Patents

Water-oil-sand three-phase separation device Download PDF

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CN210419359U
CN210419359U CN201920892878.9U CN201920892878U CN210419359U CN 210419359 U CN210419359 U CN 210419359U CN 201920892878 U CN201920892878 U CN 201920892878U CN 210419359 U CN210419359 U CN 210419359U
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oil
sand
water
mixed liquid
separation device
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CN201920892878.9U
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Chinese (zh)
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程刚
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Shaanxi Tiann Environmental Protection Technology Co ltd
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Shaanxi Tiann Environmental Protection Technology Co ltd
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Abstract

The utility model provides a water oil sand triphase separator to the stoste separation that will mix water, oil, sand is the sand body, handles oil and processing water, and this water oil sand triphase separator includes the whirl subassembly, and is equipped with the constitution with this whirl subassembly intercommunication the stoste flows in whirl subassembly's inflow tube links to each other with this whirl subassembly drive and still is equipped with drive unit, and this drive unit can order about the whirl subassembly and rotate around whirl subassembly's axis, and constitute the mixed liquid separation of sand body and profit, and this water oil sand triphase separator still including setting firmly in whirl subassembly bottom, the sand body collecting element that supplies the sand body to flow in to and the mixed liquid outlet pipe, this mixed liquid outlet pipe can be with the leading-in mixed liquid separation subassembly of profit mixed liquid, again by mixed liquid separation subassembly will mix the liquid separation and become processing water and processing oil. Water oil sand three-phase separator can have higher separation efficiency.

Description

Water-oil-sand three-phase separation device
Technical Field
The utility model relates to a solid-liquid separation sets up technical field, in particular to water oil sand three-phase separation device.
Background
At present, in the fields of petrochemical industry, metallurgy, mechanical processing and manufacturing and the like, waste stock solutions of mixed oil solid and liquid are generated, the liquid also comprises water, oil and the like, the direct discharge of the waste stock solution can cause great pollution to the environment, in order to separate the solid, water and oil in the waste stock solution, the existing separation equipment generally separates the waste stock solution by using the way of waiting for natural sedimentation of three substances with different densities, but the process of automatic sedimentation is usually slow, so that the treatment efficiency is not high, and the requirement of large-scale treatment is difficult to meet, the part is provided with a centrifugal force to separate solid and liquid, the higher the rotating speed of the centrifugal equipment is, the better the separation effect of the solid and the liquid is, however, when the centrifugal apparatus is rotated at a high speed, the separated solids may be partially rolled up and mixed again into the treated water.
SUMMERY OF THE UTILITY MODEL
In view of this, the utility model aims at providing a water oil sand three-phase separation device to can improve the separation efficiency of water, oil, solid, and have higher result of use.
In order to achieve the above purpose, the technical scheme of the utility model is realized like this:
a water-oil-sand three-phase separation device for separating a stock solution mixed with water, oil and sand into a sand body, treated oil and treated water, comprising:
the cyclone assembly is communicated with an inflow pipe which forms the raw liquid to flow into the cyclone assembly; the driving unit is connected with the rotational flow component in a driving way and can drive the rotational flow component to rotate around the axis of the rotational flow component so as to separate the mixed liquid of the sand body and the water and the oil;
the sand body collecting unit is connected with an outlet at the bottom of the cyclone assembly so as to allow separated sand bodies to enter;
the mixed liquid outflow pipe comprises a pipe head fixed at the outlet through a fixing unit and a pipe body connected with the pipe head and used for outflow of the mixed liquid;
mixed liquid separation subassembly, including being formed with the casing that holds the chamber, just hold the chamber with the body is linked together, in hold the intracavity and arrange at least a set of oil interceptor that will hold the chamber and separate into a plurality of cavities, each oil interceptor's top is higher than and holds the mixed liquid level of intracavity, and each cavity can be through oil interceptor's bottom intercommunication.
Preferably, the rotational flow component comprises a cylindrical part and a conical part which are connected in series from top to bottom, and the large end of the conical part is connected with the cylindrical part.
Preferably, a plurality of baffles which are obliquely arranged along the rotation direction of the rotational flow component are uniformly distributed on the inner wall of the conical part.
Preferably, the cyclone assembly further comprises a cylindrical connecting part connected with one end of the conical part far away from the cylindrical part in series, and the sand body collecting unit is connected with the connecting part in series.
Preferably, the tube head comprises an inner tube head and an outer tube head which are nested with each other, and the tube body comprises an outer tube communicated with the outer tube head and an inner tube nested in the outer tube and communicated with the inner tube head.
Preferably, the outer pipe is connected with the top of the accommodating cavity, and the inner pipe extends to the bottom of the accommodating cavity.
Preferably, the oil separation plates form a group, the accommodating cavity is divided into a first cavity and a second cavity which are communicated at the bottoms due to the oil separation plates, and the first cavity is communicated with the pipe body.
Preferably, exhaust ports are formed at the top of the first chamber and the top of the second chamber.
Preferably, the oil recovery port is provided at the top of the first chamber.
Preferably, the water recovery port is provided at the bottom of the second chamber.
Compared with the prior art, the utility model discloses following advantage has:
water oil sand triphase separator through setting up the whirl subassembly, because the density of water, oil, sand is different, and the density of the sand body is greater than the density of water and oil, consequently along with the rotation sand body of whirl subassembly can laminate on the inner wall of whirl subassembly because of density is great to along with the effect of gravity falls into in the sand body recovery unit, and in the mixed liquid of water and oil can flow into water oil separating subassembly through the outlet pipe, through passing through centrifugal force with the sand body and retrieving, can improve separation efficiency.
Drawings
The accompanying drawings, which form a part hereof, are included to provide a further understanding of the invention, and are incorporated in and constitute a part of this specification, illustrate embodiments of the invention and together with the description serve to explain the invention without undue limitation. In the drawings:
FIG. 1 is a cross-sectional view of a cyclone assembly according to an embodiment of the present invention;
fig. 2 is a schematic structural diagram of a baffle according to an embodiment of the present invention;
fig. 3 is a schematic view of a fixing structure of the tube head on the connecting portion according to the embodiment of the present invention;
FIG. 4 is a schematic diagram of a sand body stress according to an embodiment of the present invention;
fig. 5 is a schematic mechanism diagram of a mixed liquid separation assembly according to an embodiment of the present invention;
description of reference numerals:
1-cyclone assembly, 11-cylindrical part, 12-conical part, 121-baffle, 13-connecting part, 2-inflow pipe, 3-sand collecting unit, 4-mixed liquid outflow pipe, 41-outer pipe head, 42-inner pipe head, 43-outer pipe, 44-inner pipe, 5-mixed liquid separating assembly, 51-oil separation plate, 501-first chamber, 502-second chamber, 53-water recovering port, 54-oil recovering port and 55-exhaust port.
Detailed Description
It should be noted that, in the present invention, the embodiments and features of the embodiments may be combined with each other without conflict.
The present invention will be described in detail below with reference to the accompanying drawings in conjunction with embodiments.
The embodiment relates to a water-oil-sand three-phase separation device for separating a stock solution mixed with water, oil and sand into a sand body, treated oil and treated water, as shown in figures 1 and 5, the water-oil-sand three-phase separation device comprises a rotational flow component 1, an inflow pipe 2 which is communicated with the rotational flow component 1 and forms the raw liquid to flow into the rotational flow component 1, and a driving unit which is connected with the rotational flow component 1 in a driving way, the driving unit can drive the rotational flow component 1 to rotate around the axial line of the rotational flow component 1 so as to separate the sand body from the mixed liquid of oil and water, the water-oil-sand three-phase separation device also comprises a sand body collecting unit 3 which is fixedly arranged at the bottom of the rotational flow component 1 and is used for sand body to flow in, and a mixed liquid outlet pipe 4, the mixed liquid outflow pipe 4 can introduce the oil-water mixed liquid separated by the cyclone unit 1 into the mixed liquid separation unit 5, and the mixed liquid separation unit 5 separates the mixed liquid into treated water and treated oil.
Specifically, as shown in fig. 1, the cyclone assembly 1 specifically includes a cylindrical portion 11, a conical portion 12 and a connecting portion 13 which are sequentially connected from top to bottom, wherein the cylindrical portion 11 and the connecting portion 13 are both cylindrical, and the raw liquid flowing into the cyclone assembly 1 through the inflow pipe 2 rotates inside the cyclone assembly 1, and due to the difference in density of water, oil and sand in the raw liquid, the centrifugal force generated by the rotation of the raw liquid in the cyclone assembly 1 can cause sand with a large specific gravity to face outward and settle along the inner wall of the conical portion 12, and then the sand flows into the sand recovery unit through the connecting portion 13. The rotational flow component 1 can rotate by being driven by a driving unit, the driving unit is not shown in the figure, one mode of driving the rotational flow component 1 to rotate by the driving unit is as follows, the driving unit is a motor, a first synchronizing wheel is fixedly arranged on an output shaft of the motor, a second synchronizing wheel is fixedly arranged on the periphery of the connecting part 13, and a synchronous belt is connected between the first synchronizing wheel and the second synchronizing wheel so as to drive the rotational flow component 1 to rotate by the motor; of course, the drive unit can drive the rotational flow component 1 to rotate in other manners, such as a chain wheel transmission or a gear transmission between the motor and the rotational flow component 1.
In order to accelerate the settling velocity of the sand, as shown in fig. 1 and fig. 2, in the present embodiment, a plurality of baffles 121 are uniformly distributed on the inner wall of the conical portion 12 and are obliquely arranged along the rotation direction of the cyclone assembly 1; by arranging the baffle 121, as shown in fig. 4, since the direction of the centrifugal force is tangential to the rotation direction of the sand body, when the rotation speed is high, the settling velocity of the sand body is slow, and by arranging the baffle 121, the centrifugal force and the supporting force of the baffle 121 to the sand body can form a downward resultant force, so that the settling velocity of the sand body can be effectively increased, and the separation efficiency of the sand body and the oil-water mixed liquid can be improved.
As is known, the higher the rotation speed of the cyclone assembly 1 is, the better the separation effect of the sand and the oil-water mixture is, but the too high rotation speed can cause the separated sand to be partially involved in the oil-water mixture, and in order to reduce the sand from being re-involved in the mixture, in this embodiment, as shown in fig. 1, the mixture outlet pipe 4 includes a pipe head fixed inside the connection portion 13 and a pipe body connected to the pipe head and extending downward, and the pipe head is preferably in an inverted cone shape, and further preferably, the pipe head is arranged concentrically with the connection portion 13, and by providing the pipe head, not only the oil-water mixture can be discharged, but also the outer wall of the pipe head can effectively prevent the separated sand from being involved in the mixture again, and the separation effect of the sand and the mixture can be effectively improved.
An effective fixing of the pipe head to the inner wall of the connecting part 13 is that, as shown in fig. 3, a plurality of connecting plates are provided between the pipe head and the inner wall of the connecting part 13, sand can flow into the sand recovery unit through the gaps between the connecting plates,
foretell mixed liquid separation subassembly 5 is including being formed with the casing that holds the chamber, and holds the chamber and be linked together with the body, arranges at least a set of oil interceptor 51 that will hold the chamber and separate into a plurality of cavities in holding the intracavity, and the top of each oil interceptor 51 is higher than the liquid level that holds the mixed liquid of intracavity, and the bottom intercommunication of each cavity accessible oil interceptor 51.
In the present embodiment, the oil separation plate 51 is a single plate and divides the accommodating cavity into a first chamber 501 and a second chamber 502, wherein the first chamber 501 is communicated with the pipe, the density of the mixed liquid flowing into the first chamber 501 is different from that of the water and the oil, and the density of the oil is less than that of the water, so the oil floats upwards, the water sinks, and the first chamber 501 is communicated with the second chamber 502 at the bottom, so the separated water can enter the second chamber 502 and be discharged through the water recovery port 53 at the bottom 502 of the second chamber, and the oil at the top of the first chamber 501 can be recovered through the oil recovery port 54 arranged at the first chamber 501.
In order to improve the oil-water separation rate by making the mixed liquid rotate in the cyclone assembly 1 to separate the water and the oil into layers, in this embodiment, as shown in fig. 1 and 5, the pipe head specifically includes an inner pipe head 42 and an outer pipe head 41 which are nested with each other, and the pipe body includes an outer pipe 43 connected to the outer pipe head 41 and an inner pipe 44 connected to the inner pipe head 42, and through the centrifugal analysis, since the oil has a density lower than that of the water, the oil is concentrated in the center of the cyclone assembly 1 and mainly flows into the mixed liquid separation assembly 5 through the inner pipe 44, and the water is concentrated between the oil and the sand and mainly flows into the mixed liquid separation assembly 5 through the outer pipe 43. For this reason, in the present embodiment, the outer tube 43 is configured to communicate with the receiving cavity, specifically the bottom of the first chamber 501, and the inner tube 44 is configured to communicate with the receiving cavity, specifically the top of the first chamber 501, and since the inner tube 44 mainly contains oil and the outer tube 43 mainly contains water, the inner tube 44 and the outer tube 43 are configured as above, which can significantly improve the separation efficiency of oil and water.
In this embodiment, as shown in fig. 3, the top portions of the first chamber 501 and the second chamber 502 are respectively provided with an exhaust port 55 capable of exhausting gas outwards, and of course, the exhaust port 55 may be communicated with a gas collecting device to prevent the gas from polluting the environment, which is not described herein again.
The above description is only a preferred embodiment of the present invention, and should not be taken as limiting the invention, and any modifications, equivalent replacements, improvements, etc. made within the spirit and principle of the present invention should be included in the protection scope of the present invention.

Claims (10)

1. A water-oil-sand three-phase separation device for separating a stock solution mixed with water, oil and sand into a sand body, treated oil and treated water, is characterized by comprising:
the cyclone assembly (1) is communicated with the cyclone assembly (1) and is provided with an inflow pipe (2) which enables the stock solution to flow into the cyclone assembly (1); the driving unit is connected with the rotational flow component (1) in a driving way and can drive the rotational flow component (1) to rotate around the axis of the rotational flow component (1) so as to separate the mixed liquid of the sand body and the water and the oil;
the sand body collecting unit (3) is connected with an outlet at the bottom of the cyclone assembly (1) so as to allow separated sand bodies to enter;
a mixed liquid outflow pipe (4) which comprises a pipe head fixed at the outlet through a fixing unit and a pipe body connected with the pipe head and used for outflow of the mixed liquid;
mixed liquid separation subassembly (5), including being formed with the casing that holds the chamber, just hold the chamber with the body is linked together, in hold the intracavity and arrange at least a set of oil interceptor (51) that will hold the chamber and separate into a plurality of cavities, each oil interceptor (51) top is higher than and holds the mixed liquid level of intracavity, and each cavity can be through the bottom intercommunication of oil interceptor (51).
2. The water-oil-sand three-phase separation device of claim 1, wherein: the cyclone assembly (1) comprises a cylindrical part (11) and a conical part (12) which are connected in series from top to bottom, and the large end of the conical part (12) is connected with the cylindrical part (11).
3. The water-oil-sand three-phase separation device of claim 2, wherein: a plurality of baffles (121) which are obliquely arranged along the rotation direction of the rotational flow component (1) are uniformly distributed on the inner wall of the conical part (12).
4. The water-oil-sand three-phase separation device of claim 2, wherein: the cyclone assembly (1) further comprises a connecting part (13) which is connected with one end, far away from the cylindrical part (11), of the conical part (12) in series and is cylindrical, and the sand body collecting unit (3) is connected with the connecting part (13) in series.
5. The water-oil-sand three-phase separation device of claim 1, wherein: the tube head comprises an inner tube head (42) and an outer tube head (41) which are nested with each other, the tube body comprises an outer tube (43) communicated with the outer tube head (41), and an inner tube (44) which is nested in the outer tube (43) and communicated with the inner tube head (42).
6. The water-oil-sand three-phase separation device of claim 5, wherein: the outer tube (43) is connected with the top of the containing cavity, and the inner tube (44) extends to the bottom of the containing cavity.
7. The water-oil-sand three-phase separation device of any one of claims 1 to 6, wherein: the oil separating plates (51) are in a group, the accommodating cavity is divided into a first cavity (501) and a second cavity (502) which are communicated at the bottoms due to the oil separating plates (51), and the first cavity (501) is communicated with the pipe body.
8. The water-oil-sand three-phase separation device of claim 7, wherein: exhaust ports (55) are formed at the top of the first chamber (501) and the top of the second chamber (502).
9. The water-oil-sand three-phase separation device of claim 7, wherein: an oil recovery port (54) is provided at the top of the first chamber (501).
10. The water-oil-sand three-phase separation device of claim 7, wherein: the water recovery port (53) is provided at the bottom of the second chamber (502).
CN201920892878.9U 2019-06-13 2019-06-13 Water-oil-sand three-phase separation device Active CN210419359U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201920892878.9U CN210419359U (en) 2019-06-13 2019-06-13 Water-oil-sand three-phase separation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201920892878.9U CN210419359U (en) 2019-06-13 2019-06-13 Water-oil-sand three-phase separation device

Publications (1)

Publication Number Publication Date
CN210419359U true CN210419359U (en) 2020-04-28

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201920892878.9U Active CN210419359U (en) 2019-06-13 2019-06-13 Water-oil-sand three-phase separation device

Country Status (1)

Country Link
CN (1) CN210419359U (en)

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