CN221720559U - Fixed cyclone separator - Google Patents
Fixed cyclone separator Download PDFInfo
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- CN221720559U CN221720559U CN202323266456.6U CN202323266456U CN221720559U CN 221720559 U CN221720559 U CN 221720559U CN 202323266456 U CN202323266456 U CN 202323266456U CN 221720559 U CN221720559 U CN 221720559U
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 170
- 239000010865 sewage Substances 0.000 claims abstract description 45
- 238000000926 separation method Methods 0.000 claims abstract description 32
- 239000008213 purified water Substances 0.000 claims abstract description 19
- 230000000087 stabilizing effect Effects 0.000 claims description 13
- 238000000034 method Methods 0.000 claims description 8
- 230000008569 process Effects 0.000 claims description 5
- 230000003139 buffering effect Effects 0.000 claims description 3
- 238000003825 pressing Methods 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 10
- 239000003921 oil Substances 0.000 description 110
- 239000002245 particle Substances 0.000 description 28
- 239000007788 liquid Substances 0.000 description 11
- 238000005457 optimization Methods 0.000 description 6
- 239000012071 phase Substances 0.000 description 5
- 230000001133 acceleration Effects 0.000 description 4
- 239000010779 crude oil Substances 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 239000007791 liquid phase Substances 0.000 description 3
- 238000010008 shearing Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 230000007423 decrease Effects 0.000 description 2
- 239000000839 emulsion Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 238000010926 purge Methods 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- MBMLMWLHJBBADN-UHFFFAOYSA-N Ferrous sulfide Chemical compound [Fe]=S MBMLMWLHJBBADN-UHFFFAOYSA-N 0.000 description 1
- 230000000712 assembly Effects 0.000 description 1
- 238000000429 assembly Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000033558 biomineral tissue development Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000013043 chemical agent Substances 0.000 description 1
- 238000004581 coalescence Methods 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000005238 degreasing Methods 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000007764 o/w emulsion Substances 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
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Abstract
The utility model provides a fixed cyclone separator, comprising: the two saddles, the water inlet cavity, the water outlet cavity, the oil outlet cavity and the swirl tube assembly; the water inlet cavity is arranged on the two saddles, both ends of the water inlet cavity are provided with fixing plates, and the water inlet cavity is also provided with a sewage inlet; the water outlet cavity is arranged at the first end of the water inlet cavity, and a purified water outlet is arranged on the water outlet cavity; the oil outlet cavity is arranged at the second end of the water inlet cavity, and an oil outlet is arranged at the bottom of the oil outlet cavity; the swirl tube assembly is arranged in the water inlet cavity, and two ends of the swirl tube assembly respectively penetrate through the fixed plate and are respectively communicated with the water outlet cavity and the oil outlet cavity; the oil-containing sewage enters the water inlet cavity through the sewage inlet, the cyclone pipe assembly carries out oil-water separation on the oil-containing sewage, the separated clean water enters the water outlet cavity and then is discharged through the clean water outlet, and the separated oil enters the oil outlet cavity and then is discharged through the oil outlet. The utility model solves the problems of large volume, heavy weight and poor oil-water separation effect of the hydrocyclone in the prior art.
Description
Technical Field
The utility model relates to the technical field of cyclone separation devices, in particular to a fixed cyclone separation device.
Background
The oilfield produced water is oily sewage which is produced in oil extraction operation and is subjected to crude oil dehydration and separation, and is a complex mixture containing solid impurities, liquid impurities, dissolved gas, dissolved salt and the like after crude oil collection and primary processing. Because of the differences of crude oil characteristics, oil extraction methods, geological conditions and the like, the quality of produced water of each oil field has larger difference, but has commonality, and the main characteristics are as follows: high oil content, high mineralization, bacteria content, high content of complex organic matters and suspended matters, high COD and high water temperature, improper treatment easily causes stratum blockage, and brings difficulty to biochemical treatment of sewage.
The hydrocyclone is a common device for treating oilfield produced water, has good treatment effect when separating mixtures with large density differences, and still has the problems of large volume, large weight and poor oil-water separation effect.
Disclosure of utility model
The utility model mainly aims to provide a fixed cyclone separation device which at least solves the problems of large volume, large weight and poor oil-water separation effect of a hydrocyclone in the prior art.
In order to achieve the above object, the present utility model provides a stationary cyclonic separating apparatus comprising: the two saddles, the water inlet cavity, the water outlet cavity, the oil outlet cavity and the swirl tube assembly; the water inlet cavity is arranged on the two saddles, both ends of the water inlet cavity are provided with fixing plates, and the water inlet cavity is also provided with a sewage inlet; the water outlet cavity is arranged at the first end of the water inlet cavity, and a purified water outlet is arranged on the water outlet cavity; the oil outlet cavity is arranged at the second end of the water inlet cavity, and an oil outlet is arranged at the bottom of the oil outlet cavity; the swirl tube assembly is arranged in the water inlet cavity, and two ends of the swirl tube assembly respectively penetrate through the fixed plate and are respectively communicated with the water outlet cavity and the oil outlet cavity; the oil-containing sewage enters the water inlet cavity through the sewage inlet, the cyclone pipe assembly carries out oil-water separation on the oil-containing sewage, the separated clean water enters the water outlet cavity and then is discharged through the clean water outlet, and the separated oil enters the oil outlet cavity and then is discharged through the oil outlet.
Further, the swirl tube assembly comprises a plurality of swirl tubes, the swirl tubes are arranged in a honeycomb shape, and two ends of each swirl tube respectively penetrate through the two fixing plates and are respectively communicated with the water outlet cavity and the oil outlet cavity.
Further, the cyclone tube comprises a cylindrical cyclone section, a concentric necking section, a conical section and a parallel tail section which are connected in sequence; the cylindrical cyclone section is a cylindrical cavity and is used for forming vortex for oily sewage; the concentric necking section is a conical body cavity and is used for accelerating oily sewage and flowing in a spiral track; the conical section is a conical cavity and is used for continuously accelerating oily sewage; the parallel tail section is a cylinder chamber and is used for back-pressing other sections so as to fully separate oil from water of the oily sewage; the cylindrical cyclone section is respectively communicated with the sewage inlet and the oil outlet, and the parallel tail section is communicated with the purified water outlet.
Further, the swirl tube assembly further comprises a stabilizing plate, the stabilizing plate is vertically arranged on the parallel tail sections of the swirl tubes, the parallel tail sections of the swirl tubes penetrate through the stabilizing plate, and the stabilizing plate is used for supporting and righting the swirl tubes and eliminating vibration of the swirl tubes in the working process.
Further, a diversion cone is arranged in the water inlet cavity and used for diversion and buffering of the oily sewage and uniformly distributing the oily sewage to each cyclone tube.
Further, the top of the water inlet cavity, the water outlet cavity and the oil outlet cavity are respectively provided with an exhaust port and a pressure gauge, and the water inlet cavity is also provided with a safety valve.
Further, drain outlets are arranged at the bottoms of the water inlet cavity and the water outlet cavity.
The fixed cyclone separator of the present utility model includes: the two saddles, the water inlet cavity, the water outlet cavity, the oil outlet cavity and the swirl tube assembly; the water inlet cavity is arranged on the two saddles, both ends of the water inlet cavity are provided with fixing plates, and the water inlet cavity is also provided with a sewage inlet; the water outlet cavity is arranged at the first end of the water inlet cavity, and a purified water outlet is arranged on the water outlet cavity; the oil outlet cavity is arranged at the second end of the water inlet cavity, and an oil outlet is arranged at the bottom of the oil outlet cavity; the swirl tube assembly is arranged in the water inlet cavity, and two ends of the swirl tube assembly respectively penetrate through the fixed plate and are respectively communicated with the water outlet cavity and the oil outlet cavity; the oil-containing sewage enters the water inlet cavity through the sewage inlet, the cyclone pipe assembly carries out oil-water separation on the oil-containing sewage, the separated clean water enters the water outlet cavity and then is discharged through the clean water outlet, and the separated oil enters the oil outlet cavity and then is discharged through the oil outlet. The utility model solves the problems of large volume, heavy weight and poor oil-water separation effect of the hydrocyclone in the prior art.
Drawings
The accompanying drawings, which are included to provide a further understanding of the utility model and are incorporated in and constitute a part of this specification, illustrate embodiments of the utility model and together with the description serve to explain the utility model. In the drawings:
FIG. 1 is a schematic illustration of a stationary cyclonic separating apparatus according to an alternative embodiment of the utility model;
FIG. 2 is a schematic illustration of an assembly of cyclone tube assemblies of an alternative stationary cyclone separator device according to an embodiment of the utility model;
FIG. 3 is a schematic view of a cyclone tube structure of an alternative stationary cyclone separator according to an embodiment of the utility model.
Wherein the above figures include the following reference numerals:
10. A saddle; 20. a water inlet cavity; 21. a fixing plate; 22. a sewage inlet; 30. a water outlet cavity; 31. a purified water outlet; 40. an oil outlet cavity; 41. an oil outlet; 50. a swirl tube assembly; 51. swirl tube; 511. a cylindrical swirl section; 512. concentric necking sections; 513. a conical section; 514. parallel tail sections; 52. a stabilizing plate; 60. and a sewage outlet.
Detailed Description
It should be noted that, without conflict, the embodiments of the present utility model and features of the embodiments may be combined with each other. The utility model will be described in detail below with reference to the drawings in connection with embodiments.
As shown in fig. 1 to 3, a stationary cyclonic separating apparatus comprising: two saddles 10, a water inlet chamber 20, a water outlet chamber 30, an oil outlet chamber 40 and a swirl tube assembly 50; the water inlet cavity 20 is arranged on the two saddles 10, both ends of the water inlet cavity 20 are provided with fixing plates 21, and the water inlet cavity 20 is also provided with a sewage inlet 22; the water outlet cavity 30 is arranged at the first end of the water inlet cavity 20, and a purified water outlet 31 is arranged on the water outlet cavity 30; the oil outlet cavity 40 is arranged at the second end of the water inlet cavity 20, and an oil outlet 41 is arranged at the bottom of the oil outlet cavity 40; the swirl tube assembly 50 is arranged in the water inlet cavity 20, and two ends of the swirl tube assembly 50 respectively pass through the fixed plate 21 and are respectively communicated with the water outlet cavity 30 and the oil outlet cavity 40; the oily sewage enters the water inlet cavity 20 through the sewage inlet 22, the cyclone tube assembly 50 performs oil-water separation on the oily sewage, the separated clean water enters the water outlet cavity 30 and is discharged through the clean water outlet 31, and the separated oil enters the oil outlet cavity 40 and is discharged through the oil outlet 41.
As an optimization scheme of the present utility model, as shown in fig. 2, the swirl tube assembly 50 includes a plurality of swirl tubes 51, the plurality of swirl tubes 51 are arranged in a honeycomb shape, and two ends of each swirl tube 51 respectively pass through two fixing plates 21 and respectively communicate with the water outlet chamber 30 and the oil outlet chamber 40.
As an optimization scheme of the utility model, as shown in FIG. 3, a cyclone tube 51 comprises a cylindrical cyclone section 511, a concentric necking section 512, a conical section 513 and a parallel tail section 514 which are connected in sequence; the cylindrical cyclone section 511 is a cylindrical cavity, and the cylindrical cyclone section 511 is used for forming vortex for oily sewage; the concentric necking segment 512 is a conical body cavity, and the concentric necking segment 512 is used for accelerating oily sewage and flowing in a spiral track; the conical section 513 is a conical chamber, and the conical section 513 is used for continuously accelerating oily sewage; the parallel tail section 514 is a cylindrical cavity, and the parallel tail section 514 is used for back-pressing other sections to fully separate oil from water of the oily sewage; the cylindrical swirl section 511 is respectively communicated with the sewage inlet 22 and the oil outlet 41, and the parallel tail section 514 is communicated with the purified water outlet 31.
As an optimization scheme of the present utility model, as shown in fig. 2, the swirl tube assembly 50 further includes a stabilizing plate 52, the stabilizing plate 52 is vertically disposed on parallel tail sections 514 of the swirl tubes 51, the parallel tail sections 514 of the swirl tubes 51 all pass through the stabilizing plate 52, and the stabilizing plate 52 is used for supporting and centralizing the swirl tubes 51, so as to eliminate vibration of the swirl tubes 51 during operation.
As an optimization scheme of the present utility model, a diversion cone is further disposed in the water inlet cavity 20, and the diversion cone is used for diversion and buffering of the oily sewage and uniformly distributing the oily sewage to each cyclone tube 51.
As an optimization scheme of the utility model, as shown in FIG. 1, the top parts of the water inlet cavity 20, the water outlet cavity 30 and the oil outlet cavity 40 are respectively provided with an air outlet and a pressure gauge, and the water inlet cavity 20 is also provided with a safety valve. The exhaust port and the pressure gauge ensure that the air pressure in the water inlet chamber 20, the water outlet chamber 30 and the oil outlet chamber 40 is in a normal range, and when the equipment fails, the safety valve is automatically opened to discharge the liquid in the water inlet chamber 20.
As an optimization scheme of the present utility model, as shown in fig. 1, drain openings 60 are provided at the bottoms of the water inlet chamber 20 and the water outlet chamber 30. The drain 60 is periodically opened to drain the contaminants from the inlet and outlet chambers 20 and 30.
The working principle of the utility model is as follows:
The liquid swirl in a stationary hydrocyclone is produced by the high-velocity flow of liquid at a certain pressure. The produced water of the oil field enters the cylindrical vortex section along the tangential direction and flows spirally along the axial direction of the cyclone tube to enter the concentric necking section, and due to the change of the section, the narrow cross section area accelerates the liquid to 30000r/min, so that a strong centrifugal force for separating oil and water is formed, and the liquid is accelerated and kept in the conical section in order to compensate the loss of the centrifugal force and the friction force. Due to the density difference of water and oil, the centrifugal force acting on the water phase with higher density makes the water swirl along the conical pipe wall; the oil phase with lighter density is collected in the center to form a low-pressure oil core, the outer water ring passes through the parallel tail section and is discharged from the purified water outlet, and the separation process of the oil water in the cyclone tube is not more than 2 seconds.
The separation performance of the cyclone is mainly influenced by the particle size of the oil phase, the liquid temperature and the density difference of the oil-water liquid phase to be separated. The mechanism of hydrocyclone separation can be expressed in terms of stokes law. This law is expressed in terms of net separation force (F N) in the cyclonic separation of spherical oil particles, as the difference between the centrifugal force (F) produced by the swirling flow and the shear force (F S) on the moving oil particles: f N＝F-FS
Wherein F- -centrifugal force, # W - -density of water, ρ u - -density of oil, a- -angular acceleration, d- -particle size.
FS＝3π·μW·v·d----------(2)
Wherein F S - -shear force, mu W - -kinematic viscosity of water, v- -radial velocity of oil particles.
Thus, the net separation force F N is expressed as:
Formula (3) shows that F N may be affected by four factors, namely particle size, angular acceleration, density difference between liquid phases, and viscosity of the water continuous phase. Among the four factors, angular acceleration is easier to control. Theoretically, the greater the angular acceleration, the higher the separation effect. In practice, however, excessive speeds can result in shearing or crushing of the oil particles and unstable flow, which can reduce separation performance.
The separation performance of a hydrocyclone is related to the following factors:
Particle diameter of oil particles: the larger the oil particles, the better the separation effect. If the particle size of the oil particles is less than 5. Mu.m, separation is difficult; when the particle diameter of the oil particles is more than 20. Mu.m, separation is easy. Therefore, if the process is reasonably designed (e.g., a positive displacement pump or a low-speed lift pump is selected), the throttling, pressure drop and other shearing forces of the cyclone inlet on the produced water can be eliminated, thereby maximizing the oil particle size.
Temperature: the viscosity of water can be reduced by increasing the temperature, and the separation performance of the cyclone can be improved by easily passing oil particles through the water phase.
Density difference: deoiling depends on the relative density difference between the oil and water, and in general, the density difference should be greater than 50kg/m 3, the greater the density difference, the higher the separation effect.
Inlet oil content: with the increase of the inlet oil content, the particle size of the oil particles is correspondingly increased, which is beneficial to improving the separation performance. Therefore, the relative increase of the oil content of the inlet has little influence on the quality of the effluent. But the inlet oil content should be below 2000mg/L.
Surface tension: surface tension exists in the interface of two incompatible liquids. Lower surface tension can reduce the shearing resistance of the oil particles, so that the oil particles are easier to break. The higher surface tension becomes "sticky" oil particles, making them less prone to breakage or coalescence with other oil particles into larger oil particles.
Gas: since the residence time of the gas/liquid in the hydrocyclone is extremely short, equilibrium cannot be reached and therefore no significant effect is produced in the cyclone separation process. Hydrocyclones can treat liquids with a gas content of 20%.
Chemical agents and solid particles: surfactants can affect the interfacial properties of the oil-in-water oil particles and the stability of the emulsion. The detergent molecules and organic salts are concentrated on the interfaces of oil particles after being mixed with the oil-in-water emulsion because of carrying electrostatic charges, so that the same polarity discharge is carried out on all dispersed oil particles, and the oil particles are mutually repelled and can not be coalesced. Solids such as scale and iron sulfide can strengthen the interfacial film and stabilize the emulsion.
The process of the utility model is calculated as follows:
The fixed hydrocyclone effectively separates oil from water by means of centrifugal force. As shown in fig. 3, its inlet pressure and inlet shape is the rotation of the liquid, the flow rate of which is controlled by the pressure drop across the cyclone. The differential pressure determines the maximum throughput of the hydrocyclone and is calculated as follows:
The pressure drop Δp 0 (oil drain) between the inlet and the oil drain is:
ΔP0＝P-P0-------------(4)
Wherein P is the raw water inlet pressure, MPa, P 0 is the oil discharge outlet pressure and MPa.
The pressure drop Δp w (drain) between inlet and outlet is:
ΔPw＝P-Pw------------(5)
P w - -purified water outlet pressure, MPa.
At a constant flow and drain ratio of 1.5%, Δp 0 is about 2 times Δp w. Thus, given a pressure drop, the maximum throughput of the cyclone is dependent on the pressure drop Δp 0. The following describes two concepts of oil drainage ratio and oil removal efficiency.
The ratio of the oil discharge amount to the total water inlet amount is the oil discharge ratio eta 0：Q0
Wherein Q-total produced water inlet flow, m 3/h,Q0 -total oil discharge, m 3/h.
Although the oil extraction ratio refers to the oil content, the oil content is generally less than 10% by volume, and the balance is water. Under the condition that the oil content in water is less than 1 percent by volume. In order to achieve the best operating condition, the oil discharge ratio of the deoiling type hydrocyclone should be kept in the range of 1% -2%. If the oil content of the inlet water is more than 1%, the oil discharge ratio should be increased in order to maintain the separation efficiency.
The pressure difference ratio is the ratio of the pressure drop of the inlet and the oil drain port members to the pressure drop of the purified water outlet, and can be expressed as:
Only maintaining a constant ratio of Δp 0 and Δp w ensures an optimal constant oil drain ratio.
The oil removal efficiency determines the quality of the purified water, expressed as:
Wherein C- - -inlet oil content, mg/L, C W - - -purified water outlet oil content, mg/L.
At a certain inlet pressure, the hydrocyclone operational flow rate should be maintained within a range in which the degreasing efficiency is maintained at an optimum constant condition.
The maximum flow rate of the hydrocyclone is controlled by the pressure drop between the inlet and the oil drain. If the inlet flow of the cyclone exceeds this maximum flow range, the flow rate becomes too high, resulting in a lower core pressure that cannot be discharged from the drain. Thus, the oil removal efficiency is lowered due to insufficient amount of the oil drain.
If the inlet flow rate of the cyclone is lower than the minimum flow range, the flow rate becomes too small, and as a result, the cyclone centrifugal force cannot be achieved, and thus the oil-water separation effect cannot be achieved.
The process control of the utility model is as follows:
There are various control methods of the system according to the system constitution of the hydrocyclone. The method specifically comprises the following steps:
(1) Maximum purge water flow control
The maximum purified water flow rate of the hydrocyclone is generally determined by the pressure of the incoming buffer tank lift pump and the difference between the raw water inlet pressure and the outlet purified water pressure of the hydrocyclone. The maximum flow of the cyclone is limited by the minimum back pressure acting on the water outlet. The maximum flow can be limited by installing a restrictor at the hydrocyclone inlet or by bypass.
(2) Minimum purge water flow control
① Indirect control of
If the pressure difference between the inlet and the outlet of the hydrocyclone is lower than the preset pressure difference, the flow control valve is closed; and opening the flow control valve when the water level of the buffer tank rises or the pressure difference between the inlet and the outlet of the cyclone reaches a preset value.
② Direct control of
And closing the flow control valve if the flow of the cyclone falls below a preset limit.
(3) Control of oil discharge flow
① If the ratio of Δp 0 to Δp w remains constant, the drain flow rate decreases proportionally if the water flow rate decreases.
② Flow control valve control
The oil discharge control valve and the flow control valve at the inlet of the cyclone are controlled by parallel signals in the same way as the flow control valve at the outlet of the purified water.
③ On-off or flash control
The purified water outlet flow control valve and the oil discharge control valve are both in on/off positions, and the back pressure of the oil discharge port is set by the downstream throttle. In practical application, the flow rate of the oil drain port tends to be relatively stable, and is about 2% of the rated purified water outlet flow rate. The method is simple and effective, can be adjusted on site, and is suitable for stable flow conditions or low-pressure and low-flow working conditions.
(4) Throttle control
Typically, the turndown ratio between the maximum and minimum flow rates of the hydrocyclone is 7:1. As long as the water outlet of the hydrocyclone is not lower than the minimum flow of the hydrocyclone, the hydrocyclone can still work stably.
The structural design of the utility model is as follows:
(1) Design input
The treatment amount (m 3/h), the oil content (mg/L) of the incoming water and the oil content of the incoming water are lower than 2000mg/L. The oil content (mg/L) of effluent, the design pressure (MPa), the design temperature (DEG C), the external dimension, the material of a cyclone tube and others.
(2) Process calculation
And calculating and determining the diameters of the water inlet, the water outlet and the oil drain opening according to the treatment capacity, then determining the diameters and the number of the swirl tubes, determining the diameter of the tank body according to the swirl tubes, and comprehensively calculating the volume of each cavity.
Principle:
① Since the difference in density between the two liquid phases of oil and water is small, a strong rotational centrifugal force needs to be generated to ensure radial movement.
② To obtain a strong centrifugal force and avoid excessive pressure drop, a small diameter of the cyclone is required, but a large aspect ratio is required to ensure a sufficient residence time.
The above description is only of the preferred embodiments of the present utility model and is not intended to limit the present utility model, but various modifications and variations can be made to the present utility model by those skilled in the art. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present utility model should be included in the protection scope of the present utility model.
Claims (4)
1. A stationary cyclonic separating apparatus, comprising:
Two saddles (10);
The water inlet cavity (20), the water inlet cavity (20) is arranged on the two saddles (10), the two ends of the water inlet cavity (20) are provided with fixing plates (21), and the water inlet cavity (20) is also provided with a sewage inlet (22);
The water outlet cavity (30), the water outlet cavity (30) is arranged at the first end of the water inlet cavity (20), and a purified water outlet (31) is arranged on the water outlet cavity (30);
An oil outlet cavity (40), wherein the oil outlet cavity (40) is arranged at the second end of the water inlet cavity (20), and an oil outlet (41) is arranged at the bottom of the oil outlet cavity (40);
The swirl tube assembly (50) is arranged in the water inlet cavity (20), and two ends of the swirl tube assembly (50) respectively penetrate through the fixing plate (21) and are respectively communicated with the water outlet cavity (30) and the oil outlet cavity (40); the cyclone tube assembly (50) comprises a plurality of cyclone tubes (51) and a stabilizing plate (52), the cyclone tubes (51) are arranged in a honeycomb shape, and two ends of each cyclone tube (51) respectively penetrate through two fixing plates (21) and are respectively communicated with the water outlet cavity (30) and the oil outlet cavity (40); the cyclone tube (51) comprises a cylindrical cyclone section (511), a concentric necking section (512), a conical section (513) and a parallel tail section (514) which are connected in sequence; the cylindrical cyclone section (511) is respectively communicated with the sewage inlet (22) and the oil outlet (41), and the parallel tail section (514) is communicated with the purified water outlet (31); the cylindrical cyclone section (511) is a cylindrical cavity, and the cylindrical cyclone section (511) is used for forming vortex for oily sewage; the concentric necking section (512) is a conical body cavity, and the concentric necking section (512) is used for accelerating the oily sewage and flowing in a spiral track; the conical section (513) is a conical chamber, and the conical section (513) is used for continuously accelerating the oily sewage; the parallel tail section (514) is a cylinder chamber, and the parallel tail section (514) is used for back-pressing other sections so as to fully separate oil from water of the oily sewage; the stabilizing plates (52) are vertically arranged on parallel tail sections (514) of the cyclone tubes (51), the parallel tail sections (514) of the cyclone tubes (51) penetrate through the stabilizing plates (52), and the stabilizing plates (52) are used for supporting and righting the cyclone tubes (51) and eliminating vibration of the cyclone tubes (51) in the working process;
The oil-containing sewage enters the water inlet cavity (20) through the sewage inlet (22), the cyclone tube assembly (50) performs oil-water separation on the oil-containing sewage, separated clean water enters the water outlet cavity (30) and then is discharged through the clean water outlet (31), and separated oil enters the oil outlet cavity (40) and then is discharged through the oil outlet (41).
2. A stationary cyclonic separating apparatus as claimed in claim 1,
And a diversion cone is further arranged in the water inlet cavity (20) and is used for diversion and buffering of the oily sewage and uniformly distributing the oily sewage to each cyclone tube (51).
3. The fixed cyclone separation device according to claim 1, wherein the top of the water inlet chamber (20), the top of the water outlet chamber (30) and the top of the oil outlet chamber (40) are respectively provided with an air outlet and a pressure gauge, and a safety valve is further arranged on the water inlet chamber (20).
4. The stationary cyclone separator as claimed in claim 1, wherein the bottoms of the water inlet chamber (20) and the water outlet chamber (30) are provided with a drain outlet (60).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202323266456.6U CN221720559U (en) | 2023-12-01 | 2023-12-01 | Fixed cyclone separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202323266456.6U CN221720559U (en) | 2023-12-01 | 2023-12-01 | Fixed cyclone separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN221720559U true CN221720559U (en) | 2024-09-17 |
Family
ID=92686080
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202323266456.6U Active CN221720559U (en) | 2023-12-01 | 2023-12-01 | Fixed cyclone separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN221720559U (en) |
-
2023
- 2023-12-01 CN CN202323266456.6U patent/CN221720559U/en active Active
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