Efficient vortex flow filter

By designing a high-efficiency vortex flow filter, the structure of the cyclone, collection chamber and return chamber is used to solve the problem of limited application of the filter in the prior art, and the efficient filtration and separation of various metal and non-metal particles is achieved. The overall structure is simple, low cost and wide applicability.

CN222641485UActive Publication Date: 2025-03-21JIANGSU JIJIA INTELLIGENT EQUIP TECH CO LTD
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Patent Information

Application Number
CN202421388395.2
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-06-17
Publication Date
2025-03-21
Estimated Expiration
2034-06-17

AI Technical Summary

Technical Problem

In the prior art, mechanical filters and magnetic filters are limited in their applications when filtering various metal and non-metallic particulate matter, and have complex structures and high costs.

Method used

A high-efficiency vortex flow filter is designed to use the structure of the cyclone, collection chamber and reflux chamber to separate particulate matter in the liquid by centrifugal force. It is suitable for the removal and filtration of various metal and non-metal particles, and can separate liquid mixtures of different densities and air containing particulate matter.

Benefits of technology

It realizes efficient filtration of various metal and non-metal particles. The overall structure is simple, low cost, and wide applicability. It can independently perform filtration and separation, water purification reflux and particulate matter discharge.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model discloses an efficient vortex flow filter and belongs to the field of filters. The outer wall of the rotational flow bin is provided with a nozzle along the tangential direction, a stock solution enters the nozzle, the bottom of the rotational flow bin is communicated with a collecting bin, a backflow bin is arranged in the collecting bin, the backflow bin is communicated with an inner cavity of the collecting bin, the backflow bin extends upwards from the bottom of the collecting bin, and the backflow bin is provided with a backflow pipe communicated to a discharge pipe at the top of the rotational flow bin; an emptying opening is formed in the bottom of the collecting bin. The device for separating the particulate matters in the liquid by utilizing the centrifugal force based on the fluid vortex flow principle is suitable for removing and filtering various metal and non-metal particles, is also suitable for separating liquid mixtures with different densities and separating and filtering air containing the particulate matters, and is wide in applicability.
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Description

Technical Field

[0001] The utility model relates to the technical field of filters, and more specifically to a high-efficiency vortex flow filter. Background Art

[0002] Fluids (oil, water, etc.) used in industrial cleaning, degreasing and machining processes are recycled. The recycled oil contains particulate matter generated during the production process, as well as other industrial and environmental waste liquid treatment systems, which all need to filter out the particulate matter. These particulate matter components are very complex, some are mainly metal particles, some are mainly non-metal particles, or a mixture of metal and non-metal particles.

[0003] The commonly used filtering methods in the industry are mechanical filter filtration or magnetic filter. The characteristic of the mechanical filter is that the mesh size of the filter needs to be designed according to the size of the particles, and often multiple layers of filters with different mesh sizes are required; magnetic filters are suitable for filtering metal particles that can be magnetized, but have almost no effect on filtering metal and non-metal particles that cannot be magnetized. It is obviously necessary to provide a high-efficiency filter with wide applicability.

[0004] The patent with publication number CN111204891A provides a centrifugal vortex ballast water filtration device, which is composed of a cascaded two-stage conical vertical filter cartridge. The inner surface of the conical vertical filter cartridge is provided with an internal spiral thread, and a water pump is provided at the front end of the inlet of the first-stage conical vertical filter cartridge. The sewage outlet of the two-stage conical vertical filter cartridge is connected to a sewage pipeline, a sewage valve, and a sewage suction pump and a sewage collector arranged on the sewage pipeline. The design adopts physical centrifugation, which can effectively separate large particles of impurities, and the overall structure is relatively complex, requires more components, and has a high production cost. Utility Model Content

[0005] 1. Technical problems to be solved by the utility model

[0006] The purpose of the utility model is to provide a high-efficiency vortex flow filter, which is based on the principle of fluid vortex flow and utilizes centrifugal force to separate particulate matter in liquid. It is suitable for removing and filtering various metal and non-metal particles to solve the problem that the application of mechanical filters and magnetic filters in the prior art is relatively limited. The separation device of the utility model is also suitable for separating liquid mixtures with different densities and separating and filtering air containing particulate matter. It has a wide applicability and a simple overall structure and is easy to use.

[0007] 2. Technical solution

[0008] In order to achieve the above-mentioned purpose, the technical solution provided by the utility model is:

[0009] The utility model discloses a high-efficiency vortex flow filter, comprising a vortex chamber, an outer wall of the vortex chamber is provided with a nozzle for raw liquid to enter along a tangential direction, the bottom of the vortex chamber is connected with a collecting chamber, a reflux chamber is provided in the collecting chamber, the reflux chamber is connected with the inner cavity of the collecting chamber, and the reflux chamber extends upward from the bottom of the collecting chamber, a reflux pipe is provided on the reflux chamber and is connected to a discharge pipe at the top of the vortex chamber; an emptying port is provided at the bottom of the collecting chamber.

[0010] Furthermore, the bottom of the cyclone bin has a cyclone throat opening which opens downward and gradually contracts in the height direction, and the collecting bin is located below the cyclone throat opening and communicates with the inner cavity of the cyclone bin.

[0011] Furthermore, there is a conical cavity between the vortex throat and the collecting bin, the top opening of the conical cavity is consistent with the bottom opening of the vortex throat, and the conical cavity opening gradually expands downward in the height direction, and the inner cavity width of the collecting bin is greater than the bottom opening width of the conical cavity.

[0012] Furthermore, the reflux bin is arranged at the center of the collecting bin, and the reflux bin, the reflux pipe and the discharge pipe are coaxially arranged and coaxial with the axis of the swirl throat.

[0013] Furthermore, the cyclone chamber, the collection chamber and the reflux chamber all adopt a cylindrical structure with the same size of opening downward along the height direction.

[0014] Furthermore, a communication channel is provided on the circumferential side wall of the reflux bin to communicate with the collection bin, and a filter is provided on the communication channel.

[0015] Furthermore, the discharge pipe is located at the top center of the cyclone bin and is detachably mounted with the cyclone bin.

[0016] Furthermore, the reflux bin is arranged at the center of the collecting bin and is detachably mounted with the bottom of the collecting bin.

[0017] Furthermore, the reflux pipe is arranged at the top center position of the reflux bin and is detachably mounted with the reflux bin.

[0018] Furthermore, a drain flange and a drain valve are provided on the drain port at the bottom of the collecting bin.

[0019] 3. Beneficial effects

[0020] Compared with the prior art, the technical solution provided by the utility model has the following beneficial effects:

[0021] (1) The filter of the utility model has a reflux bin in the collection bin, the reflux bin is connected with the inner cavity of the collection bin, and the reflux bin extends upward from the bottom of the collection bin, and a reflux pipe is provided at the top of the reflux bin to connect to the discharge pipe at the top of the vortex bin; through the design of the reflux bin and the reflux pipe, not only can the liquid in the collection bin be prevented from flowing back into the vortex bin through the vortex throat at the bottom of the vortex bin to destroy the vortex in the vortex bin, but also a channel for the discharge of the clean liquid after separation is provided, so as to realize the independent operation of filtration separation, clean water reflux and particle discharge, and the overall structure is compact, simple and low in cost.

[0022] (2) The filter of the utility model has a conical vortex throat at the bottom of the vortex bin that opens downward and gradually contracts in the height direction, and a conical cavity that opens downward and gradually expands in the height direction is provided between the vortex throat and the collection bin. The conical design of the vortex throat increases the speed of the vortex and promotes the centrifugal separation effect, so that the particles collected on the cylinder wall flow through the vortex throat to the collection bin, and the conical cavity can guide the vortex liquid flowing out of the vortex throat into the collection bin and reduce the flow rate of the liquid so that the solid particles can be fully precipitated. BRIEF DESCRIPTION OF THE DRAWINGS

[0023] Figure 1 Schematic diagram of the filter structure in the embodiment.

[0024] Explanation of the symbols in the schematic diagram:

[0025] 1. Nozzle; 2. Swirl chamber; 3. Swirl throat; 4. Collection chamber; 5. Conical cavity; 6. Reflux chamber; 7. Reflux pipe; 8. Discharge pipe; 9. Drain flange; 10. Drain valve. DETAILED DESCRIPTION

[0026] In order to further understand the content of the utility model, the utility model is described in detail in conjunction with the accompanying drawings.

[0027] In the description of the present invention, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", etc., indicating the orientation or positional relationship, are based on the orientation or positional relationship shown in the drawings, and are 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 limiting the present invention. In addition, the terms "first", "second", and "third" are used for descriptive purposes only, and cannot be understood as indicating or implying relative importance.

[0028] The utility model is further described below in conjunction with embodiments.

[0029] Example

[0030] Combination Figure 1As shown, a high-efficiency vortex flow filter of this embodiment includes a vortex chamber 2, and a nozzle 1 for raw liquid to enter is provided on the outer wall of the vortex chamber 2 along the tangential direction. The bottom of the vortex chamber 2 is connected to a collecting chamber 4, and a reflux chamber 6 is provided in the collecting chamber 4. The reflux chamber 6 is connected to the inner cavity of the collecting chamber 4, and the reflux chamber 6 extends upward from the bottom of the collecting chamber 4. A reflux pipe 7 is provided on the reflux chamber 6 and connected to a discharge pipe 8 at the top of the vortex chamber 2; an emptying port is provided at the bottom of the collecting chamber 4. The raw liquid enters in the tangential direction to generate a vortex so as to separate the solid particles from the liquid. The solid particles are concentrated in the collecting chamber 4 and can be discharged in a centralized manner, while the liquid can flow back to the outside of the vortex chamber 2 through the reflux chamber 6.

[0031] In practice, the cyclone bin 2, the collection bin 4 and the reflux bin 6 can all adopt a cylindrical structure with the same size of opening downward in the height direction. More preferably, in order to improve the separation effect, the bottom of the cyclone bin 2 has a tapered cyclone throat 3 with a gradually narrowing opening downward in the height direction, the top opening of the cyclone throat 3 is smaller than the inner cavity width of the cyclone bin 2, the collection bin 4 is located below the cyclone throat 3 and is connected to the inner cavity of the cyclone bin 2, and the inner cavity width of the collection bin 4 is significantly larger than the bottom opening of the cyclone throat 3. A better design is that there is also a tapered cavity 5 between the cyclone throat 3 and the collection bin 4, the top opening of the tapered cavity 5 is consistent with the bottom opening of the cyclone throat 3, and the opening of the tapered cavity 5 gradually expands downward in the height direction, and the inner cavity width of the collection bin 4 is larger than the bottom opening width of the tapered cavity 5.

[0032] When the above design is used, the raw liquid with a certain flow rate is input from the nozzle 1 at the upper part of the cyclone chamber 2 and in the tangential direction into the closed cyclone chamber 2. The liquid forms a cyclone along the inner wall of the cylinder and moves toward the lower part of the cylinder. The conical design of the cyclone throat 3 increases the speed of the vortex. Due to the action of centrifugal force, the solid particles in the liquid will be thrown to the cylinder wall, and the particles collected on the cylinder wall will flow through the cyclone throat 3 at the bottom of the cyclone chamber 2 to the collection chamber 4 at the bottom. The lower part of the cyclone throat 3 is a conical cavity 5. The function of the collection chamber 4 is to reduce the flow rate of the liquid so that the solid particles can settle. The conical cavity 5 can guide the vortex liquid flowing out of the cyclone throat 3. Since the circumferential side wall of the reflux chamber 6 is provided with a connecting channel to maintain communication with the collection chamber 4, the clean liquid separated in the collection chamber 4 will enter the reflux chamber 6 under the action of the vortex pressure and gradually move upward, and then be transported back to the middle part of the upper cyclone chamber 2 through the reflux pipe 7, and then flow out through the discharge pipe 8 at the top. In order to prevent the filtered particles from entering the reflux bin 6 along with the liquid, a filter is provided on the communication channel of the circumferential side wall of the reflux bin 6 to prevent the solid particles from entering and achieve efficient separation.

[0033] In order to optimize the spatial layout of each component, in this embodiment, the reflux bin 6 is arranged at the center of the collecting bin 4, and the reflux bin 6, the reflux pipe 7 and the discharge pipe 8 are coaxially arranged and coaxial with the axis of the swirl throat 3. In order to facilitate the connection and coordination of each component, the discharge pipe 8 is located at the top center of the swirl bin 2 and is detachably mounted with the swirl bin 2; the reflux bin 6 is arranged at the center of the collecting bin 4 and is detachably mounted with the bottom of the collecting bin 4; the reflux pipe 7 is arranged at the top center of the reflux bin 6 and is detachably mounted with the reflux bin 6, and can be specifically installed in the form of threaded mounting. And the emptying port at the bottom of the collecting bin 4 is provided with an emptying flange 9 and an emptying valve 10, which are used to control the uniform discharge of the separated particles.

[0034] In this embodiment, the design of the reflux bin 6 and the reflux pipe 7 can not only prevent the liquid in the collection bin 4 from flowing back into the vortex bin 2 through the vortex throat 3 at the bottom of the vortex bin 2 to destroy the vortex in the vortex bin 2, but also provide a channel for the clean liquid to be discharged after separation, thereby realizing the independent filtration separation, clean water reflux and particle discharge. In addition, the overall structure is compact, simple, and low in cost, and is very suitable for promotion and application.

[0035] The above is a schematic description of the present invention and its implementation methods, which is not restrictive and is only one of the implementation methods of the present invention, and is not actually limited to this. Therefore, if ordinary technicians in this field are inspired by it and design structural methods and embodiments similar to the technical solution without creativity without departing from the purpose of the present invention, they should all fall within the protection scope of the present invention.

Claims

1. A high efficiency vortex flow filter, characterized in that: The invention comprises a swirl chamber (2), wherein a nozzle (1) for raw liquid to enter is provided on the outer wall of the swirl chamber (2) along a tangential direction, the bottom of the swirl chamber (2) is connected to a collecting chamber (4), a reflux chamber (6) is provided in the collecting chamber (4), the reflux chamber (6) is connected to the inner cavity of the collecting chamber (4), and the reflux chamber (6) extends upward from the bottom of the collecting chamber (4), a reflux pipe (7) is provided on the reflux chamber (6) and is connected to a discharge pipe (8) at the top of the swirl chamber (2); and an emptying port is provided at the bottom of the collecting chamber (4).

2. A high efficiency vortex flow filter according to claim 1, characterized in that: The bottom of the cyclone bin (2) has a cyclone throat (3) which opens downward and gradually contracts in the height direction. The collection bin (4) is located below the cyclone throat (3) and is in communication with the inner cavity of the cyclone bin (2).

3. A high efficiency vortex flow filter according to claim 2, characterized in that: A conical cavity (5) is also provided between the cyclone throat (3) and the collection bin (4); the top opening of the conical cavity (5) is consistent with the bottom opening of the cyclone throat (3), and the opening of the conical cavity (5) gradually expands downward in the height direction; the inner cavity width of the collection bin (4) is greater than the bottom opening width of the conical cavity (5).

4. A high efficiency vortex flow filter according to claim 2, characterized in that: The reflux bin (6) is arranged at the center of the collection bin (4), and the reflux bin (6), the reflux pipe (7) and the discharge pipe (8) are coaxially arranged and coaxial with the axis of the swirl throat (3).

5. A high efficiency vortex flow filter according to claim 2, characterized in that: The cyclone bin (2), the collection bin (4) and the reflux bin (6) all adopt a cylindrical structure with openings of the same size downward in the height direction.

6. A high efficiency vortex flow filter according to any one of claims 1 to 5, characterized in that: A communication channel is provided on the circumferential side wall of the reflux bin (6) to maintain communication with the collection bin (4), and a filter screen is provided on the communication channel.

7. A high efficiency vortex flow filter according to any one of claims 1 to 5, characterized in that: The discharge pipe (8) is located at the top center of the cyclone bin (2) and is detachably mounted with the cyclone bin (2).

8. A high efficiency vortex flow filter according to any one of claims 1 to 5, characterized in that: The reflux bin (6) is arranged at the center of the collection bin (4) and is detachably mounted with the bottom of the collection bin (4).

9. A high efficiency vortex flow filter according to any one of claims 1 to 5, characterized in that: The reflux pipe (7) is arranged at the top center position of the reflux bin (6) and is detachably mounted with the reflux bin (6).

10. A high efficiency vortex flow filter according to any one of claims 1 to 5, characterized in that: A drain flange (9) and a drain valve (10) are provided on the drain port at the bottom of the collecting bin (4).

Citation Information

Patent Citations

  • Centrifugal vortex type ballast water filtering device with self-adaptive cleaning function

    CN111204891A