Cyclone centrifuge

Through the design of the cyclone centrifuge, the emulsion film is crushed by high-speed airflow and threaded columns, which solves the problem of oil-water emulsion separation, reduces costs and improves recovery, and is suitable for oil field wastewater treatment.

CN222174439UInactive Publication Date: 2024-12-17赵万古 +1
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Patent Information

Application Number
CN202420877061.5
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-04-25
Publication Date
2024-12-17
Estimated Expiration
Not applicable · inactive patent

AI Technical Summary

Technical Problem

The existing technology is difficult to effectively separate oil-water emulsions, resulting in high oil-water separation costs and difficult sewage treatment. The cost of oil production in the late stage of oil field development increases, and new technologies are needed to improve recovery rates and reduce costs.

Method used

A cyclone centrifuge is designed, using a high-power fan to match the air flow guidance of the air cylinder and the inner cavity cylinder, and the emulsion is rotated through the high-speed air flow in the centrifugal channel, and the emulsion film is crushed by the threaded column, so that the oil and water are different due to the specific gravity. The separation can be adjusted according to the material conditions and a small amount of chemical reagents can be added to accelerate separation.

Benefits of technology

The oil-water separation in the emulsion is achieved, the separation time is shortened, the production cost is reduced, and the output is increased. It is suitable for oil field wastewater treatment.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model discloses a cyclone centrifuge, which relates to the technical field of oilfield wastewater treatment and comprises a centrifugal cylinder, an inner cavity cylinder is arranged in the centrifugal cylinder, and a centrifugal channel is formed between the centrifugal cylinder and the inner cavity cylinder. According to the cyclone centrifugal machine, the arranged high-power draught fan is matched with airflow guiding of the air cylinder and the inner cavity cylinder, high-speed airflow in the centrifugal channel flows downwards, emulsion enters from a top side opening of the centrifugal channel, and under the action of the first guide piece and the second guide piece on the top side, the airflow containing the emulsion obtains large centrifugal force; an emulsion film can be broken by colliding with the threaded column, oil and water in the emulsion are separated due to different specific gravities, the wind power of the high-power fan can be adjusted according to different material conditions in the use process, polymers (part) are decomposed, oil-water separation is accelerated, the separation time is shortened, only a small amount of chemical reagents need to be added, and the production cost is reduced. The purposes of reducing the production cost and increasing the yield are achieved.
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Description

Technical Field

[0001] The utility model relates to the technical field of oilfield wastewater treatment, in particular to a cyclone centrifuge. Background Art

[0002] Oil is the basic raw material for the development of petrochemical industry and an important strategic material for the country. It is related to the overall national economy. At the same time, oil is a non-renewable resource. The oil recovery rate is the biggest concern not only for the oil industry but also for the entire society.

[0003] Although new oil fields are constantly being discovered in my country through technological improvements and a lot of energy invested by petroleum science and technology workers, most of my country's oil fields are in the late stages of development. This is mainly because after years of exploitation, the crude oil reserves of many oil fields have been greatly reduced and the difficulty of exploitation has gradually increased. In the late stages of development, the output of oil fields tends to gradually decline, and the cost of exploitation will also increase. Therefore, it is urgent to carry out secondary and tertiary oil recovery in an all-round way.

[0004] As an effective mining technology for improving oil recovery and increasing crude oil production, polymer crude oil has been recognized worldwide for its good effects, large recovery rate improvement, high economic efficiency and other characteristics under specific conditions. However, since the produced emulsion contains polymers, the strength of the oil-water surface film is increased, and the stability of the produced emulsion is greatly improved, it becomes very difficult to break the emulsion membrane water. The previous emulsion breaking water technology can no longer meet the production needs.

[0005] Oil and water are two immiscible substances, but with the rapid development of chemical technology, a variety of active chemical reagents have been widely used. These active chemical reagents make it very easy for incompatible oil and water to form a stable emulsion under specific conditions. For industrial fields that require oil-water separation, the oil-water separation technology and cost of the emulsion are very high. The emulsion will have a great negative impact on the field. For example, if the filtered water contains oil, the difficulty and cost of sewage treatment will increase. The presence of water in the oil will affect the quality of the oil. For this reason, the present application proposes a cyclone centrifuge to solve the above problems. Utility Model Content

[0006] 1. Technical issues to be resolved

[0007] In view of the deficiencies of the prior art, the utility model provides a cyclone centrifuge to solve the technical problems raised in the above background.

[0008] (II) Technical solution

[0009] In order to achieve the above purpose, the technical solution adopted by the utility model is: a cyclone centrifuge, including a centrifugal cylinder, an inner cavity cylinder is arranged in the centrifugal cylinder, and a centrifugal channel is formed between the centrifugal cylinder and the inner cavity cylinder, a plurality of inclined guide pieces 1 are arranged on the top side of the centrifugal channel, a plurality of inclined guide pieces 2 are arranged on the bottom side of the centrifugal channel, a plurality of threaded columns are installed in the centrifugal channel between the centrifugal cylinder and the inner cavity cylinder, a ring-shaped infusion pipeline is connected to the top side of the centrifugal channel, and the infusion pipeline is sleeved in the inner cavity cylinder. On the outside of the top side of the cavity cylinder, the bottom side of the centrifugal cylinder is connected to the inverted conical cylinder body, the bottom end of the inner cavity cylinder is connected to a conical cylinder, the top side of the inner cavity cylinder is connected to a high-power fan, the bottom end of the inverted conical cylinder body is connected to a discharge cylinder, the discharge cylinder is equipped with a first sealing plate and a second sealing plate, a liquid outlet pipe structure is installed in the middle of the inverted conical cylinder body, the top side opening of the conical cylinder is connected to a guide cylinder, a plurality of lower liquid pipes are installed at the lowest point of the upper inclined surface of the conical cylinder, and the bottom ends of the plurality of lower liquid pipes extend into the inverted conical cylinder body.

[0010] Preferably, the guide plates 1 and 2 are distributed in a ring shape, and both the guide plates 1 and 2 are installed on the inner wall of the centrifugal barrel, and the threaded columns are distributed between the guide plates 1 and 2.

[0011] Preferably, the liquid outlet pipe structure is arranged corresponding to the liquid storage tank, the liquid storage tank is provided with a pump outlet pipe connected to tank body one, and the top side of tank body one is connected to tank body two through an infusion pipe.

[0012] Preferably, the tank body 1 and the tank body 2 are adapted to be equipped with a storage pool, the top of the tank body 1 and the tank body 2 are both equipped with exhaust pipes, and the bottom of the tank body 1 and the tank body 2 are both equipped with discharge valves.

[0013] Preferably, the air duct at the air inlet end of the high-power fan is connected to the top side of the inner cavity tube, and the air outlet of the high-power fan is connected to the exhaust duct.

[0014] Preferably, the liquid outlet pipe structure includes a liquid outlet pipe and a sealing plate, and the liquid outlet pipe is installed on the side wall of the inverted cone-shaped cylinder, and the sealing plate is installed at the port of the liquid outlet pipe.

[0015] Preferably, the first blocking plate and the second blocking plate are respectively distributed on the top side and the bottom side of the discharge barrel, and counterweights are provided on the first blocking plate and the second blocking plate.

[0016] Preferably, a conical water blocking plate is provided on the top side of the discharge cylinder, and the bottom side of the conical water blocking plate is connected to the bottom side opening of the inverted conical cylinder body through a plurality of support rods.

[0017] Preferably, a filter plate is arranged on the top side of the inner cavity tube, and a plurality of S-shaped air ducts are vertically arranged in the filter plate.

[0018] (III) Beneficial effects

[0019] The beneficial effects of the utility model are:

[0020] The cyclone centrifuge realizes the downward flow of high-speed airflow in the centrifugal channel by means of the high-power fan arranged to cooperate with the airflow guide through the wind tube and the inner cavity tube. The emulsion enters from the top side opening of the centrifugal channel. Under the action of the top side guide piece 1 and the bottom side guide piece 2, the airflow containing the emulsion rotates and flows downward to obtain a large centrifugal force. The emulsion film can be broken by colliding with the threaded column in the rotating state, so that the oil and water in the emulsion are separated due to the difference in specific gravity. In use, the wind force of the high-power fan can be adjusted according to different material conditions to decompose the polymer (partially), accelerate the separation of oil and water, shorten the separation time, and only need to add a small amount of chemical reagents, so as to achieve the purpose of reducing production costs and increasing output. BRIEF DESCRIPTION OF THE DRAWINGS

[0021] Figure 1 This is a schematic diagram of the cross-sectional structure of the centrifugal cylinder of the utility model;

[0022] Figure 2 It is a schematic diagram of the overall structure of the utility model;

[0023] Figure 3 This is an enlarged cross-sectional structural diagram of the centrifugal cylinder of the utility model;

[0024] Figure 4 This is a schematic diagram of the airflow guiding in the centrifugal cylinder of the utility model;

[0025] Figure 5 This is a three-dimensional cross-sectional schematic diagram of the inner cavity tube of the utility model;

[0026] Figure 6 It is a three-dimensional cross-sectional schematic diagram of the centrifugal cylinder of the utility model.

[0027] In the figure: 1 centrifugal cylinder, 2 inner cavity cylinder, 3 centrifugal channel, 4 guide plate 1, 5 guide plate 2, 6 threaded column, 7 inverted cone cylinder, 8 cone cylinder, 9 guide cylinder, 10 lower liquid pipe, 11 air cylinder, 12 high-power fan, 13 exhaust cylinder, 14 discharge cylinder, 15 cone water blocking plate, 16 first blocking plate, 17 second blocking plate, 18 counterweight, 19 liquid outlet pipe structure, 191 liquid outlet pipe, 192 blocking plate, 20 liquid storage tank, 21 pump outlet pipeline, 22 tank body 1, 23 infusion pipe, 24 tank body 2, 25 storage tank, 26 exhaust pipe, 27 discharge valve, 28 infusion pipeline, 29 filter plate. DETAILED DESCRIPTION

[0028] The following will be combined with the drawings in the embodiments of the utility model to clearly and completely describe the technical solutions in the embodiments of the utility model. Obviously, the described embodiments are only part of the embodiments of the utility model, not all of the embodiments. Based on the embodiments in the utility model, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the utility model.

[0029] like Figure 1-6As shown, the utility model provides a technical solution: a cyclone centrifuge, including a centrifugal cylinder 1, an inner cavity cylinder 2 is arranged in the centrifugal cylinder 1, and a centrifugal channel 3 is formed between the centrifugal cylinder 1 and the inner cavity cylinder 2, a plurality of inclined guide pieces 4 are arranged on the top side of the centrifugal channel 3, a plurality of inclined guide pieces 5 are arranged on the bottom side of the centrifugal channel 3, a plurality of threaded columns 6 are installed in the centrifugal channel 3 between the centrifugal cylinder 1 and the inner cavity cylinder 2, and the spiral pattern on the outer side of the threaded columns 6 can improve the effect of breaking the emulsion film, the top side of the centrifugal channel 3 is connected with an annular infusion pipeline 28, the infusion pipeline 28 is annularly sleeved on the outer wall of the top side of the inner cavity cylinder 2, and the bottom side of the annular part is connected to the top side of the centrifugal channel 3 to ensure that the emulsion can evenly enter the centrifugal channel 3, and the bottom side of the centrifugal cylinder 1 is connected to the inner cavity cylinder 2. The inverted conical cylinder 7 is connected to a conical cylinder 8 at the bottom end of the inner cavity cylinder 2, and a high-power fan 12 is connected to the top side of the inner cavity cylinder 2. The high-power fan 12 is operated to guide the air flow through the air cylinder 11 and the inner cavity cylinder 2, so that the high-speed airflow in the centrifugal channel 3 flows downward. The infusion pipeline 28 inputs the emulsion into the top side port of the centrifugal channel 3. Under the action of the top side guide piece 1 4 and the guide piece 2 5, the airflow containing the emulsion obtains a large centrifugal force, and the collision with the threaded column 6 can break the emulsion film, so that the oil and water in the emulsion are separated due to the difference in specific gravity. In use, the wind force of the high-power fan 12 can be adjusted according to different material conditions to decompose the polymer (partially), accelerate the separation of oil and water, shorten the separation time, and add a small amount of chemical reagents to To achieve the purpose of reducing production costs and increasing output, the bottom end of the inverted conical cylinder 7 is connected to the discharge cylinder 14, and the first sealing plate 16 and the second sealing plate 17 are installed on the discharge cylinder 14. A liquid outlet pipe structure 19 is installed in the middle of the inverted conical cylinder 7. A conical water blocking plate 15 is arranged on the top side of the discharge cylinder 14, and the bottom side of the conical water blocking plate 15 is connected to the bottom side opening of the inverted conical cylinder 7 through a plurality of support rods. The conical water blocking plate 15 can block the airflow or liquid ejected from the centrifugal channel 3 to avoid impacting the first sealing plate 16, and the heavier solids will pass through the gaps between the plurality of support rods and enter the first sealing plate 16 on the top side of the discharge cylinder 14, thereby realizing the diversion of solids, liquids and airflow. The initial emulsion can be provided with a self-heating device in the infusion pipeline 28, and the steam heating of the oil field can be used. Heat, the heated emulsion can greatly improve the activity of the emulsion. Under the action of the high-pressure pump, the initial emulsion has a heating system and automatic addition of chemical reagents in the straight pipe section of the infusion pipe 28. The infusion pipe 28 has a rotating component that can make the initial emulsion roll inside and outside during the flow, so as to achieve the temperature and chemical reagent mixing when the emulsion flows in the infusion pipe 28. The initial emulsion enters the centrifugal channel 3 through the infusion pipe 28 under the temperature and chemical test fluidization state. Under the action of the rotating blades of the high-power fan 12, a wind speed of 30m per second is generated to enter the centrifugal channel 3, and under the action of the guide blade 4, it rotates and descends, and hits the large number of threaded columns 6 in the centrifugal channel 3 to obtain a strong impact force. The emulsion not only generates a strong impact force during high-speed rotation, but alsoIt can also make solids with different densities obtain huge centrifugal force, move downward along the inner wall of the centrifugal cylinder 1 and the inner cavity cylinder 2, enter the bottom of the centrifugal cylinder 1 and then enter the inverted cone cylinder 7. A filter plate 29 is arranged on the top side of the inner cavity cylinder 2, and a plurality of S-shaped air ducts are arranged vertically in the filter plate 29 to further filter the moisture in the airflow discharged from the inner cavity cylinder 2. The S-shaped air duct increases the path of the airflow.

[0030] The guide pieces 1 4 and the guide pieces 2 5 are distributed in a ring shape, and the guide pieces 1 4 and the guide pieces 2 5 are installed on the inner wall of the centrifugal cylinder 1 , and the threaded columns 6 are distributed between the guide pieces 1 4 and the guide pieces 2 5 .

[0031] The liquid outlet pipe structure 19 is arranged corresponding to the liquid storage tank 20. The liquid storage tank 20 is provided with a pump-out pipe 21 connected to the tank body 1 22. The top side of the tank body 1 22 is connected to the tank body 2 24 through the infusion pipe 23. The pump-out pipe 21 is adapted to be equipped with an extraction pump.

[0032] Tank body 1 22 and tank body 2 24 are equipped with a storage pool 25. Exhaust pipes 26 are installed on the top of tank body 1 22 and tank body 2 24. Discharge valves 27 are installed on the bottom of tank body 1 22 and tank body 2 24. The liquid storage tank 20 enters tank body 1 22 through the pump outlet pipe 21, so that oil and water enter and separate in layers, and a small amount of solid matter exists at the bottom of tank body 1 22. Solid matter is discharged to the storage pool 25 manually from time to time, and the storage pool 25 is post-processed.

[0033] The volume of tank 1 22 and tank 2 24 is 5m 3 The separation time of solid and liquid is observed by the oil mark at the bottom of tank body 1 22 and tank body 2 24. The solid matter is discharged into the solid matter discharge pool 25 according to the actual situation, and the water is discharged through the valve. As the water on the water surface becomes smaller, it can automatically flow into tank body 2 24 when it reaches a certain level. At this time, there is a certain level of water in the oil. Tank body 24 has a heating device. After the water evaporates, it is automatically discharged through the exhaust pipe 26 above the tank body. The above operations are all controlled by the console. Except for the solid emissions that need to be manually discharged regularly, the rest can be automatically controlled and no manual intervention is required.

[0034] The air duct 11 at the air inlet end of the high-power fan 12 has an anti-static device in the air duct 11 to prevent static electricity from generating open flames. The air duct 11 is connected to the top side of the inner cavity tube 2. The exhaust port of the high-power fan 12 is connected to the exhaust duct 13, and the exhaust duct 13 discharges the exhausted gas.

[0035] The liquid outlet pipe structure 19 includes a liquid outlet pipe 191 and a sealing plate 192, and the liquid outlet pipe 191 is installed on the side wall of the inverted conical cylinder 7, and the sealing plate 192 is installed at the port of the liquid outlet pipe 191. The sealing plate 192 is made of deformable plastic material. When the water line in the inverted conical cylinder 7 is higher than the height covering the liquid outlet pipe 191, the sealing plate 192 is pushed outward by the pressure in the inverted conical cylinder 7, and the sealing plate 192 is deformed and bent outward. At this time, the port of the liquid outlet pipe 191 is in an open state to achieve liquid discharge.

[0036] Two solid discharge valves of different sizes are installed at the lower part of the inverted cone-shaped cylinder 7, namely the first sealing plate 16 and the second sealing plate 17. The first sealing plate 16 and the second sealing plate 17 are respectively distributed on the top side and the bottom side of the discharge barrel 14, and the first sealing plate 16 and the second sealing plate 17 are provided with a counterweight 18, and the counterweight 18 is connected to the adjusting rods of the first sealing plate 16 and the second sealing plate 17. The weight that the first sealing plate 16 and the second sealing plate 17 can bear can be adjusted by sliding the counterweight 18 on the adjusting rod. After a certain amount of solid matter accumulates on the upper side of the first sealing plate 16, the weight is greater than the counterweight 18, and the first sealing plate 16 will rotate with the positioning axis as the axis, so that the solid matter falls into the discharge barrel 14, and the second sealing plate 17 receives the solid matter falling from above. After a certain amount of solid matter accumulates on the upper side of the second sealing plate 17, the weight is greater than the counterweight 18, and the second sealing plate 17 will rotate with the positioning shaft as the axis. The positioning shaft is installed on the side wall of the discharge barrel 14, and the positioning shaft is set at the connection between the adjusting rod and the first sealing plate 16 and the second sealing plate 17, so that the solid matter falls to the outside of the discharge barrel 14 and is discharged. In this way, one of the first sealing plate 16 and the second sealing plate 17 is in a closed state, thereby ensuring the sealing of the inverted cone cylinder 7. The setting of the sealing plate 192 can make the sealing plate 192 push out the discharge liquid after a certain pressure is generated in the liquid outlet pipe 191, which is also used to ensure the sealing of the inverted cone cylinder 7, and the liquid is discharged through the liquid outlet pipe 191 into the external liquid storage tank 20, thereby realizing the closing or opening of the sealing plate 192 by utilizing the pressure difference.

[0037] The top side opening of the conical cylinder 8 is connected to the guide cylinder 9. The channel space of the guide cylinder 9 is smaller than that of the inverted conical cylinder 7, which plays a role in reducing the wind speed. It cooperates with the conical cylinder 8 to block water molecules. At the same time, a certain high-pressure space is guaranteed in the centrifugal channel 3 to ensure that the emulsion obtains a strong impact force when colliding with the threaded rod 6. The upper inclined surface of the conical cylinder 8 plays a flow-gathering role for the liquid, and the lower inclined surface of the conical cylinder 8 plays a blocking role for the liquid. A plurality of liquid down pipes 10 are installed at the lowest point of the upper inclined surface of the conical cylinder 8, and the bottom ends of the plurality of liquid down pipes 10 extend into the inverted conical cylinder 7. The liquid down pipes 10 are used for the liquid in the inner cavity cylinder 2 to flow down to the inverted conical cylinder 7.

[0038] The operating steps of the utility model are:

[0039] The high-power fan 17 operates to guide the air flow through the air cylinder 11 and the inner cavity tube 2, so that the high-speed air flow in the centrifugal channel 3 flows downward. The infusion pipeline 28 inputs the emulsion into the top side port of the centrifugal channel 3. Under the action of the top side guide piece 1 4 and the guide piece 2 5, the air flow containing the emulsion obtains a large centrifugal force, and the collision with the threaded column 6 can break the emulsion film, so that the oil and water in the emulsion are separated due to the difference in specific gravity. In use, the wind force of the high-power fan 12 can be adjusted according to different material conditions to decompose the polymer (partially), accelerate the separation of oil and water, shorten the separation time, and add a small amount of chemical reagents to achieve the purpose of reducing production costs and increasing output.

[0040] The initial emulsion can be provided with a self-heating device in the infusion pipeline 28, and can be heated by steam from the oil field. The heated emulsion can greatly improve the activity of the emulsion. Under the action of the high-pressure pump, the initial emulsion has a heating system and a small amount of chemical reagents are automatically added to the infusion pipeline 28. The infusion pipeline 28 has a rotating component that can make the initial emulsion roll inside and outside during the flow, so as to achieve the temperature and chemical reagent mixing when the emulsion flows in the infusion pipeline 28. The initial emulsion enters the centrifugal channel 3 through the annular section of the infusion pipeline 28 under the temperature and chemical test fluidization state, and in the high-power Under the action of the rotating blades of the high-speed fan 12, a wind speed of 30m / s is generated to enter the centrifugal channel 3, and under the action of the guide blade 4, it rotates and descends, hitting the large number of threaded columns 6 in the centrifugal channel 3 to obtain a strong impact force. The emulsion not only generates a strong impact force during high-speed rotation, but also enables solids with different densities to obtain huge centrifugal force, move downward along the inner wall of the centrifugal cylinder 1 and the inner cavity cylinder 2, and enter the bottom of the centrifugal cylinder 1 and then enter the inverted cone cylinder 7. The lower part of the inverted cone cylinder 7 is equipped with two solid discharge valves of different sizes, that is, the first sealing The blocking plate 16 and the second blocking plate 17, after a certain amount of solid matter accumulates on the upper side of the first blocking plate 16, the weight is greater than the counterweight 18, the first blocking plate 16 will rotate with the positioning axis as the axis, so that the solid matter falls to the discharge barrel 14, the second blocking plate 17 receives the solid matter falling from above, after a certain amount of solid matter accumulates on the upper side of the second blocking plate 17, the weight is greater than the counterweight 18, the second blocking plate 17 will rotate with the positioning axis as the axis, so that the solid matter falls to the outside of the discharge barrel 14 for discharge, the two counterweights 18 are not located on the outer sides of the first blocking plate 16 and the second blocking plate 17 The same is achieved in this way, that the weight of solid matter accumulated when the first sealing plate 16 and the second sealing plate 17 are opened is different. After the device is adjusted, the weight of solid matter required for the second sealing plate 17 is greater, so that the first sealing plate 16 and the second sealing plate 17 are not opened at the same time, so that one of the first sealing plate 16 and the second sealing plate 17 is in a closed state, thereby ensuring the sealing of the inverted cone cylinder 7. The setting of the sealing plate 192 can push the sealing plate 192 out to discharge liquid after a certain pressure is generated in the liquid outlet pipe 191, which is also used to ensure the sealing of the inverted cone cylinder 7.

[0041] The liquid storage tank 20 enters the tank body 22 through the pump outlet pipe 21, so that the oil and water enter and separate in layers, and a small amount of solid matter exists at the bottom of the tank body 22. The solid matter is discharged to the storage tank 25 manually at irregular intervals for post-processing of the storage tank 22.

[0042] The volume of tank 1 22 and tank 2 24 is 5m 3 The separation time of solid and liquid is determined by observing the oil marks at the bottom of tank body 1 22 and tank body 2 24. The solids are discharged into the solid discharge pool 25 according to the actual separation situation of the solids and liquids, and the water is discharged through the valve. As the oil ratio becomes smaller, when it reaches a certain level on the water surface, it can automatically flow into tank body 2 24. At this time, there is a certain level of water in the oil. Tank body 24 has a heating device. After the water evaporates, it is automatically discharged through the exhaust pipe 26 above tank body 24. The above operations are all controlled by the console. Except for the solid emissions that need to be manually discharged regularly, the rest can be automatically controlled and no manual intervention is required.

[0043] In the description of the present invention, it is necessary to understand that the indicated orientation or positional relationship is based on the orientation or positional relationship shown in the accompanying drawings, and is only for the convenience of describing the present invention and simplifying the description, rather than indicating or implying that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and therefore cannot be understood as a limitation on the present invention.

[0044] In the present invention, unless otherwise clearly stipulated and limited, for example, it can be a fixed connection, a detachable connection, or an integrated connection; it can be a mechanical connection or an electrical connection; it can be directly connected or indirectly connected through an intermediate medium, it can be the internal connection of two elements or the interaction relationship between two elements. Unless otherwise clearly defined, for ordinary technicians in this field, the specific meanings of the above terms in the present invention can be understood according to the specific circumstances.

[0045] Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that various changes, modifications, substitutions and variations may be made to the embodiments without departing from the principles and spirit of the present invention, and that the scope of the present invention is defined by the appended claims and their equivalents.

Claims

1. A cyclone centrifuge, comprising a centrifugal drum (1), characterized in that: The centrifugal cylinder (1) is provided with an inner cavity cylinder (2), and a centrifugal channel (3) is formed between the centrifugal cylinder (1) and the inner cavity cylinder (2), a plurality of inclined guide pieces (1) (4) are provided on the top side of the centrifugal channel (3), a plurality of inclined guide pieces (2) (5) are provided on the bottom side of the centrifugal channel (3), a plurality of threaded columns (6) are installed in the centrifugal channel (3), the top side of the centrifugal channel (3) is connected to an annular infusion pipeline (28), the bottom side of the centrifugal cylinder (1) is connected to an inverted conical cylinder body (7), and the bottom end of the inner cavity cylinder (2) is connected to a conical cylinder body (8). The inverted conical cylinder (8) is connected to a high-power fan (12) at the top side of the inner cavity cylinder (2), the bottom end of the inverted conical cylinder (7) is connected to a discharge cylinder (14), a first sealing plate (16) and a second sealing plate (17) are installed on the discharge cylinder (14), a liquid outlet pipe structure (19) is installed in the middle of the inverted conical cylinder (7), the top side opening of the conical cylinder (8) is connected to a guide cylinder (9), a plurality of lower liquid pipes (10) are installed at the lowest point of the upper side inclined surface of the conical cylinder (8), and the bottom ends of the plurality of lower liquid pipes (10) extend into the inverted conical cylinder (7).

2. A cyclone centrifuge according to claim 1, characterized in that: The plurality of guide pieces 1 (4) and the plurality of guide pieces 2 (5) are distributed in a ring shape, and the guide pieces 1 (4) and the guide pieces 2 (5) are both installed on the inner wall of the centrifugal cylinder (1), and the plurality of threaded columns (6) are distributed between the plurality of guide pieces 1 (4) and the plurality of guide pieces 2 (5).

3. A cyclone centrifuge according to claim 1, characterized in that: The liquid outlet pipe structure (19) is arranged corresponding to the liquid storage tank (20), and the liquid storage tank (20) is provided with a pump outlet pipe (21) connected to the tank body 1 (22), and the top side of the tank body 1 (22) is connected to the tank body 2 (24) through the infusion pipe (23).

4. A cyclone centrifuge according to claim 3, characterized in that: The tank body 1 (22) and the tank body 2 (24) are adapted to be equipped with a storage pool (25), the top of the tank body 1 (22) and the top of the tank body 2 (24) are both equipped with an exhaust pipe (26), and the bottom of the tank body 1 (22) and the bottom of the tank body 2 (24) are both equipped with a discharge valve (27).

5. A cyclone centrifuge according to claim 1, characterized in that: The air cylinder (11) at the air inlet end of the high-power fan (12) is connected to the top side of the inner cavity cylinder (2), and the air outlet of the high-power fan (12) is connected to the air cylinder (13).

6. A cyclone centrifuge according to claim 1, characterized in that: The liquid outlet pipe structure (19) comprises a liquid outlet pipe (191) and a sealing plate (192), wherein the liquid outlet pipe (191) is installed on the side wall of the inverted cone-shaped cylinder (7), and the sealing plate (192) is installed at the port of the liquid outlet pipe (191).

7. A cyclone centrifuge according to claim 1, characterized in that: The first blocking plate (16) and the second blocking plate (17) are respectively distributed on the top side and the bottom side of the discharge barrel (14), and a counterweight (18) is provided on both the first blocking plate (16) and the second blocking plate (17).

8. A cyclone centrifuge according to claim 1, characterized in that: A conical water blocking plate (15) is arranged on the top side of the discharge cylinder (14), and the bottom side of the conical water blocking plate (15) is connected to the bottom side opening of the inverted conical cylinder (7) through a plurality of support rods.

9. A cyclone centrifuge according to claim 1, characterized in that: A filter plate (29) is arranged on the top side of the inner cavity tube (2), and a plurality of S-shaped air ducts are vertically arranged inside the filter plate (29).