A white oil refining tank

By setting up a combined mixing mechanism and multiple sets of anchor-type stirring paddles in front of the white oil refining tank, the problem of uneven mixing between clay and white oil was solved, and the high-efficiency mass transfer and refining effect of the white oil refining tank was achieved.

CN224377966UActive Publication Date: 2026-06-19HUBEI WEIJIA TECH CO LTD

Patent Information

Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
HUBEI WEIJIA TECH CO LTD
Filing Date
2025-05-26
Publication Date
2026-06-19

AI Technical Summary

Technical Problem

In existing white oil refining tanks, the mass transfer efficiency of mixing white clay and white oil is not high, resulting in low refining efficiency. The stirring device cannot achieve an ideal mixing state between white clay and white oil, thus affecting the refining effect.

Method used

A combined mixing mechanism is installed before the white oil refining tank, including a turbine dynamic pipeline mixer and an SK-type static mixer, combined with multiple sets of anchor-type agitators to ensure that the white oil and white clay are fully mixed, and then filtered through a bag filter.

Benefits of technology

It improves the mass transfer efficiency of white oil and white clay, enhances the refining effect, ensures that white clay fully plays its role in adsorbing impurities, and improves the overall efficiency of the refining tank.

✦ Generated by Eureka AI based on patent content.

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  • Figure CN224377966U_ABST
    Figure CN224377966U_ABST
Patent Text Reader

Abstract

The utility model relates to a white oil refining tank, it includes the refining tank body, still includes the combination mixing mechanism who sets up before the refining tank body and sets up the bag filter behind the refining tank body, the combination mixing mechanism includes setting up the top of the refining tank body and the turbine dynamic pipeline mixer and SK type static mixer who connect gradually, the two feed ends of turbine dynamic pipeline mixer are connected white oil delivery pipe and white clay feed pipe respectively, the discharge end of turbine dynamic pipeline mixer is connected with the import end of SK type static mixer, and the export end of SK type static mixer is connected with the feed port of the refining tank body through the elbow pipe. The utility model has the advantages that: the combination mixing mechanism is set up before the refining tank body, and the mass transfer efficiency of white oil and white clay is improved through the turbine dynamic pipeline mixer and SK type static mixer who connect gradually, and the subsequent refining efficiency is effectively improved.
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Description

Technical Field

[0001] This utility model relates to the field of white oil treatment technology, specifically to a white oil refining tank. Background Technology

[0002] Existing white oil refining tanks often add white oil and bleaching clay separately, which may result in insufficient mass transfer efficiency. During the white oil refining process, the mass transfer effect of the mixture of bleaching clay and white oil affects the refining efficiency. In some traditional white oil refining tanks, the stirring device may not be able to achieve an ideal mixing state between the bleaching clay and white oil, causing the bleaching clay to not fully perform its function of adsorbing impurities, and some white oil to fail to effectively contact the bleaching clay, thus reducing the refining effect. Utility Model Content

[0003] The purpose of this invention is to provide a white oil refining tank to address the aforementioned deficiencies.

[0004] A white oil refining tank includes a refining tank body, a combined mixing mechanism disposed in front of the refining tank body, and a bag filter disposed behind the refining tank body.

[0005] The combined mixing mechanism includes a turbine dynamic pipeline mixer and an SK-type static mixer, which are installed on the top of the refining tank and connected in sequence. The two inlet ends of the turbine dynamic pipeline mixer are respectively connected to the white oil conveying pipe and the white clay inlet pipe. The outlet end of the turbine dynamic pipeline mixer is connected to the inlet end of the SK-type static mixer. The outlet end of the SK-type static mixer is connected to the inlet of the refining tank through a right-angle bend.

[0006] A mixing motor is located at the top center of the refining tank. The output shaft of the mixing motor is connected to a mixing shaft that extends into the refining tank. Multiple sets of anchor-type stirring paddles are evenly arranged on the mixing shaft. The bottom of the refining tank has a conical structure. A white oil discharge port with a filter screen and a valve is located at the bottom of the refining tank. The white oil discharge port is connected to the inlet of the bag filter through a white oil discharge pipe.

[0007] Preferably, the top of the refined tank is also provided with a breather valve for balancing the pressure inside the tank.

[0008] Preferably, the number of multiple sets of anchor-type agitators is no less than four sets.

[0009] Preferably, each set of anchor-type mixing paddles includes four upward-sloping mixing rods evenly arranged along the circumference of the mixing shaft, with the mixing rods forming an angle of 60° with the mixing shaft.

[0010] Preferably, the bottom of the refining tank and the side of the white oil discharge port are provided with a white clay intake port.

[0011] Preferably, the filter screen at the white oil discharge port is a high-strength stainless steel filter screen used to prevent white clay particles from flowing out.

[0012] Preferably, the side wall of the refined tank is also provided with a heating jacket and a heat insulation layer.

[0013] The advantages of this invention are: a combined mixing mechanism is set in front of the refining tank, which improves the mass transfer efficiency of white oil and white clay by connecting a turbine dynamic pipeline mixer and an SK-type static mixer in sequence, thereby effectively improving the subsequent refining efficiency. Attached Figure Description

[0014] Figure 1 This is a schematic diagram of the structure of this utility model.

[0015] Figure 2 This is a schematic diagram of the anchor-type agitator. Detailed Implementation

[0016] To make the objectives, technical solutions, and advantages of the embodiments of this utility model clearer, the technical solutions of the embodiments of this utility model will be clearly and completely described below with reference to the accompanying drawings. Obviously, the described embodiments are only some embodiments of this utility model, and not all embodiments. The components of the embodiments of this utility model described and shown in the accompanying drawings can generally be arranged and designed in various different configurations.

[0017] Therefore, the following detailed description of the embodiments of the present invention provided in the accompanying drawings is not intended to limit the scope of the claimed invention, but merely to illustrate selected embodiments of the invention. All other embodiments obtained by those skilled in the art based on the embodiments of the present invention without inventive effort are within the scope of protection of the present invention.

[0018] It should be noted that similar labels and letters in the following figures indicate similar items. Therefore, once an item is defined in one figure, it does not need to be further defined and explained in subsequent figures.

[0019] In the description of the embodiments of this utility model, it should be noted that if terms such as "upper," "lower," "inner," or "outer" indicate the orientation or positional relationship based on the orientation or positional relationship shown in the accompanying drawings, or the orientation or positional relationship commonly used when the utility model product is in use, they are only for the convenience of describing the utility model and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, or be constructed and operated in a specific orientation, and therefore should not be construed as a limitation of the utility model. Furthermore, if terms such as "first" or "second" appear in the description of this utility model, they are only used to distinguish descriptions and should not be construed as indicating or implying relative importance.

[0020] In the description of the embodiments of this utility model, it should also be noted that, unless otherwise explicitly specified and limited, the terms "set" and "connection" should be interpreted broadly. For example, they can refer to a fixed connection, a detachable connection, or an integral connection; they can refer to a mechanical connection or an electrical connection; they can refer to a direct connection or an indirect connection through an intermediate medium; and they can refer to the internal connection of two components. Those skilled in the art can understand the specific meaning of the above terms in this utility model based on the specific circumstances.

[0021] As shown in the attached figure, a white oil refining tank includes a refining tank body 1, a combined mixing mechanism disposed in front of the refining tank body 1, and a bag filter 2 disposed behind the refining tank body 1.

[0022] The combined mixing mechanism includes a turbine dynamic pipeline mixer 3 and an SK-type static mixer 4, which are installed on the top of the refining tank 1 and connected in sequence. The two inlet ends of the turbine dynamic pipeline mixer 3 are respectively connected to the white oil conveying pipe and the white clay inlet pipe. The outlet end of the turbine dynamic pipeline mixer 3 is connected to the inlet end of the SK-type static mixer 4. The outlet end of the SK-type static mixer 4 is connected to the inlet 5 of the refining tank 1 through a right-angle bend 6.

[0023] A mixing motor 8 is located at the top center of the refining tank 1. The output shaft of the mixing motor 8 is connected to a mixing shaft 9 extending into the refining tank 1. Multiple sets of anchor-type stirring paddles 10 are evenly arranged on the mixing shaft 9. The bottom of the refining tank 1 has a conical structure and a white oil discharge port 11 with a filter screen and valve. The white oil discharge port 11 is connected to the inlet of the bag filter 2 through a white oil discharge pipe 12. Regular monitoring, cleaning, or replacement of the filter bags is necessary to ensure filtration efficiency and flow rate.

[0024] In another technical solution, the top of the refined tank 1 is also provided with a breather valve 7 for balancing the pressure inside the tank to prevent the pressure from being too high or too low.

[0025] In another technical solution, the number of multiple sets of anchor-type stirring paddles 10 is no less than four sets to ensure the stirring effect and improve the mass transfer efficiency.

[0026] In another technical solution, each set of anchor-type mixing paddles 10 includes four inclined upward mixing rods 13 evenly arranged around the mixing shaft 9, with the mixing rods 13 having an angle of 60° with the mixing shaft 9.

[0027] In another technical solution, a clay intake port 14 is provided at the bottom of the refining tank 1 and on one side of the white oil discharge port 11. The height of the side intake port is generally about 0.5-1m from the bottom of the tank, and the angle is usually 30-60° with the tangent of the tank body, so that the clay can be easily extracted.

[0028] In another technical solution, the filter screen at the white oil discharge port 11 is a high-strength stainless steel filter screen to prevent the outflow of bleaching clay particles. This filters solid impurities in the white oil, such as bleaching clay particles and rust, preventing these impurities from flowing out with the white oil and affecting its quality and subsequent use. The filter screen also provides preliminary filtration assurance for subsequent fine filtration processes, helping to improve the efficiency and stability of the entire filtration system.

[0029] In another technical solution, the side wall of the refined tank 1 is also provided with a heating jacket 15 and a heat insulation layer 16. The heat insulation layer effectively reduces heat loss and lowers energy consumption.

[0030] Working principle: A combined mixing mechanism is set in front of the refining tank. White oil and white clay are first mixed by a turbine dynamic pipeline mixer and then enter the SK-type static mixer. The combined mixing mechanism can effectively improve the mass transfer efficiency of white oil and white clay. Then, they are mixed and stirred by multiple sets of anchor-type stirring paddles in the refining tank to ensure the refining effect of white oil.

[0031] The above-described embodiments are only intended to illustrate the technical solution and features of this utility model, and are intended to enable those skilled in the art to implement them. They should not be used to limit the scope of protection of this utility model. All equivalent changes or modifications made in accordance with the spirit and essence of this utility model are within the scope of protection of this utility model. Anything not described in detail is prior art.

Claims

1. A white oil refining tank, comprising a refining tank body (1), characterized in that, It also includes a combined mixing mechanism disposed in front of the refining tank (1) and a bag filter (2) disposed behind the refining tank (1); The combined mixing mechanism includes a turbine dynamic pipeline mixer (3) and an SK-type static mixer (4) arranged on the top of the refining tank (1) and connected in sequence. The two feed ends of the turbine dynamic pipeline mixer (3) are respectively connected to the white oil conveying pipe and the white clay feed pipe. The discharge end of the turbine dynamic pipeline mixer (3) is connected to the inlet end of the SK-type static mixer (4). The outlet end of the SK-type static mixer (4) is connected to the feed port (5) of the refining tank (1) through a right-angle bend (6). A mixing motor (8) is provided at the top center of the refining tank (1). The output shaft of the mixing motor (8) is connected to a mixing shaft (9) that extends into the refining tank (1). Multiple sets of anchor-type stirring paddles (10) are evenly provided on the mixing shaft (9). The bottom of the refining tank (1) is a conical structure. A white oil discharge port (11) with a filter screen and a valve is provided at the bottom of the refining tank (1). The white oil discharge port (11) is connected to the inlet of the bag filter (2) through a white oil discharge pipe (12).

2. The white oil refining tank according to claim 1, characterized in that, The top of the refined tank (1) is also provided with a breather valve (7) for balancing the pressure inside the tank.

3. The white oil refining tank according to claim 1, characterized in that, The number of multiple sets of anchor-type mixing blades (10) shall not be less than four sets.

4. A white oil refining tank according to claim 3, characterized in that, Each set of anchor-type mixing paddles (10) includes four inclined upward mixing rods (13) evenly arranged around the mixing shaft (9), with the mixing rods (13) and the mixing shaft (9) having an angle of 60°.

5. A white oil refining tank according to claim 1, characterized in that, The bottom of the refined tank (1) and on one side of the white oil discharge port (11) is provided with a white clay intake port (14).

6. A white oil refining tank according to claim 1, characterized in that, The filter screen at the white oil discharge port (11) is a high-strength stainless steel filter screen used to prevent white clay particles from flowing out.

7. A white oil refining tank according to claim 1, characterized in that, The side wall of the refined tank (1) is also provided with a heating jacket (15) and a heat insulation layer (16).