Distilled water oil-water separation structure of vacuum distillation system

By designing a distilled water, oil and water separation structure in a vacuum distillation system, using the combination of oil-suction pipe and buffer plate to achieve oil-water separation, solving the problem of distilled water oil-polluting the environment, and improving water quality and environmental protection effect.

CN223060765UActive Publication Date: 2025-07-04SHENZHEN IVP TECH CO LTD
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Patent Information

Application Number
CN202422011420.1
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-08-20
Publication Date
2025-07-04
Estimated Expiration
2034-08-20

AI Technical Summary

Technical Problem

The distilled water in the MVR vacuum distillation system contains oil when discharged, resulting in poor water quality and polluting the environment. It is difficult for the existing technology to effectively separate oil and water.

Method used

A distilled water, oil and water separation structure of a vacuum distillation system is designed, including a distilled water tank body, inlet and outlet pipelines, oil pumping pipes and buffer plates. The oil is returned to the evaporation box through the pumping pipe, and the oil is quickly cooled by cooling device to precipitate, and combined with the buffer plate to prevent oil and water mixing.

Benefits of technology

Effectively reduce the oil content in distilled water, improve water quality, prevent oil and water mixing, and reduce environmental pollution.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model relates to the technical field of industrial wastewater treatment, and discloses a distilled water oil-water separation structure of a vacuum distillation system, which comprises a distilled water tank body, an inlet pipeline and an outlet pipeline are arranged on the side wall of the distilled water tank body, and the inlet pipeline is communicated with an evaporation box. The oil pumping pipe is arranged at the top of the distilled water tank, one end of the oil pumping pipe is communicated with the inside of the distilled water tank, and the other end is communicated with the evaporation box through a pump. The outlet pipeline is communicated with the interior of the distilled water tank body, extends to the bottom of the distilled water tank body and is not in contact with the bottom surface of the distilled water tank body. Distilled water is discharged into the distilled water tank body through the inlet pipeline after being cooled, oil in the distilled water can be separated out and floats upwards after the distilled water is rapidly cooled, the distilled water is pumped back to the evaporation box through the oil pumping pipeline, backflow is formed for re-evaporation, and the oil content in the discharged distilled water is reduced; by arranging a buffer plate, distilled water just discharged into the distilled water tank is buffered, and oil-water mixing caused by the large flowing speed of distilled water in the distilled water tank is prevented.
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Description

Technical Field

[0001] The utility model relates to the technical field of industrial wastewater treatment, in particular to an oil-water separation structure for distilled water in an MVR vacuum distillation system. Background Art

[0002] An MVR vacuum distillation system is used to treat oily wastewater. An evaporation tank is provided in the MVR vacuum distillation system, and the distilled water generated by the evaporation tank needs to be discharged. After the industrial oily wastewater is evaporated, the distilled water contains oil, resulting in an oil-water mixing phenomenon, which leads to poor discharged water quality and environmental pollution. Therefore, it is necessary to re-filter the discharged distilled water. Summary of the Utility Model

[0003] Based on this, in view of the problem that the distilled water discharged from the evaporation tank contains oil, an oil-water separation structure for distilled water in an MVR vacuum distillation system is provided.

[0004] To achieve the above object, the utility model provides the following technical solution: an oil-water separation structure for distilled water in a vacuum distillation system, including a distilled water tank body, an inlet pipeline and an outlet pipeline are provided on the side wall of the distilled water tank body, and the inlet pipeline is communicated with the evaporation tank.

[0005] An oil suction pipe, the oil suction pipe is arranged on the top of the distilled water tank body, and one end is communicated with the inside of the distilled water tank body, and the other end is communicated with the evaporation tank through a pump.

[0006] A buffer plate, the buffer plate is placed at the port of the inlet pipeline inside the distilled water tank body, and covers the periphery and the top of the port of the inlet pipeline to form a buffer cavity.

[0007] The outlet pipeline is communicated with the inside of the distilled water tank body, extends to the bottom of the distilled water tank body, and does not contact the bottom surface of the distilled water tank body.

[0008] In a preferred example of the utility model, it can be further configured that: an air inlet pipe is further provided on the top of the distilled water tank body for the air above to communicate with the upper part of the tank body during liquid discharge.

[0009] By adopting the above technical solution, the oil suction pipe is communicated with the top of the evaporation tank through a pump, and the oil at the top of the distilled water tank body is pumped back to the evaporation tank for evaporation again.

[0010] In a preferred example of the utility model, it can be further configured that: a cooling device is provided between the inlet pipeline and the evaporation tank.

[0011] By adopting the above technical solution, the cooling device quickly cools the distilled water. The purpose is to precipitate and float the oil in the water after quickly cooling the water, which is convenient for subsequent oil pumping.

[0012] In summary, the utility model includes at least one of the following beneficial technical effects:

[0013] After being cooled, the distilled water is discharged into the distilled water tank through the inlet pipeline. After the distilled water is rapidly cooled, the oil in the water will precipitate and float, and is pumped back to the evaporation box through the oil pumping pipeline to form a reflux and re-evaporation, reducing the oil content in the discharged distilled water;

[0014] By setting a buffer plate, the just-discharged distilled water is buffered to prevent the large flow rate of the distilled water inside the distilled water tank from causing oil-water mixing. Brief Description of the Drawings

[0015] The drawings are used to provide a further understanding of the present invention and constitute a part of the specification. Together with the embodiments of the present invention, they are used to explain the present invention and do not constitute a limitation to the present invention. In the drawings:

[0016] Figure 1 is a schematic structural diagram of the outside of the present invention;

[0017] Figure 2 is a schematic structural diagram of the inside of the present invention.

[0018] In the drawings:

[0019] 1. Distilled water tank; 11. Oil suction pipe; 12. Air inlet pipe; 13. Inlet pipeline; 14. Outlet pipeline; 2. Buffer plate. Detailed Embodiments

[0020] The following will clearly and completely describe the technical solutions in the embodiments of the present invention with reference to the drawings in the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, rather than all the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.

[0021] In Figure 1-2 the shown embodiment, the present invention provides a technical solution: a vacuum distillation system distilled water oil-water separation structure, including a distilled water tank 1, an inlet pipeline 13 and an outlet pipeline 14 are provided on the side wall of the distilled water tank 1, and the inlet pipeline 13 communicates with the distilled water outlet of the evaporation box.

[0022] A cooling device is provided between the inlet pipeline 13 and the evaporation box. The cooling device includes a cold water coil for cooling the distilled water, and the distilled water is cooled after passing through the coil. The outlet pipeline 14 communicates with the inside of the distilled water tank 1, extends to the bottom of the distilled water tank 1, and does not contact the bottom surface of the distilled water tank 1.

[0023] At the top of the distilled water tank body 1, there are an oil extraction pipe 11 and an air inlet pipe 12. The air inlet pipe 12 is connected to the top of the buffer cavity, and the oil extraction pipe 11 is connected to the cavity outside the buffer cavity. One end of the oil extraction pipe 11 is connected to the inside of the distilled water tank body 1, and the other end of the oil extraction pipe is connected to the evaporation tank through a pump. The air inlet pipe 12 is used to make the air above communicate with the upper part of the tank when discharging liquid, which is convenient for discharging distilled water.

[0024] The buffer plate 2 is placed at the port of the inlet pipeline 13 inside the distilled water tank body 1 and covers the periphery and top of the port of the inlet pipeline 13 to form a buffer cavity. The bottom of the buffer plate 2 only needs to be placed below the port of the inlet pipeline 13 and should not be too low.

[0025] The specific working principle of the present invention will be elaborated in detail below: The distilled water flows out from the evaporation tank, is cooled by the cooling device, and then enters the inside of the distilled water tank body 1 through the inlet pipeline 13. The distilled water first enters the buffer plate 2 for rectification. After entering the distilled water tank body 1, the oil floats up, and the oil is pumped into the evaporation tank through the oil extraction pipe 11 and the pump for evaporation again. The water at the bottom of the distilled water tank body 1 is discharged through the outlet pipeline 14 by the pump, reducing the oil content in the discharged distilled water.

[0026] Although the embodiments of the present invention have been shown and described, for those of ordinary skill in the art, it can be understood that various changes, modifications, substitutions, and variations can be made to these embodiments without departing from the principle and spirit of the present invention. The scope of the present invention is defined by the appended claims and their equivalents.

Claims

1. Vacuum distillation system for separating distilled water from oil and water, comprising a distilled water tank body (1), wherein an inlet pipeline (13) and an outlet pipeline (14) are provided on the side wall of the distilled water tank body (1), and the inlet pipeline (13) is communicated with an evaporation tank, and it is characterized in that: A cooling device is provided between the inlet pipeline (13) and the evaporation tank; An oil suction pipe (11), which is arranged at the top of the distilled water tank body (1), and one end is communicated with the inside of the distilled water tank body (1), and the other end is communicated with the evaporation tank through a pump and an oil suction pipe; A buffer plate (2), which is placed at the port of the inlet pipeline (13) inside the distilled water tank body (1), and covers the periphery and the top of the port of the inlet pipeline (13) to form a buffer cavity.

2. The distilled water and oil separation structure of the vacuum distillation system according to claim 1, characterized in that: An air inlet pipe (12) is further provided at the top of the distilled water tank body (1).

3. The oil-water separation structure of distilled water in the vacuum distillation system according to claim 1, wherein: The outlet pipeline (14) is communicated with the inside of the distilled water tank body (1), extends to the bottom of the distilled water tank body (1), and does not contact the bottom surface of the distilled water tank body (1).