A continuous layered oil separator

Abstract

The utility model discloses a continuous layered oil separator, the continuous layered oil separator includes the main part, the feed inlet of setting in the upper portion one side of main part and setting in the lower portion of main part another side water phase discharge gate, the main part is separated through a plurality of baffle in the inside and is separated a plurality of separating chambers, and the one side of separating chamber is provided with oil phase chamber and water phase chamber, and each separating chamber and water phase chamber are connected with oil phase chamber through pipeline, and one end of each baffle is contacted with the inner wall of main part, and is equipped with the liquid discharge port in the other end near the inner wall of main part, and the liquid discharge port on any two adjacent baffle is staggered setting, the utility model discloses a continuous layered oil separator, makes oil -water mixture slowly flow in each chamber, makes oil -water completely delaminates, and oil phase is gathered to oil phase chamber finally and is discharged through the oil outlet of each chamber, and water phase flows to water phase chamber, and is discharged through water phase discharge gate, and realizes the continuous separation of material light and heavy components under the closed environment.

Description

Technical Field

[0001] This utility model belongs to the field of fine chemical equipment technology, and relates to oil-water separation devices, and more particularly to a continuous stratified oil separator that realizes continuous separation of light and heavy components of materials in a closed environment. Background Technology

[0002] Oil-water separation is a common process in the production of petrochemicals, fine chemicals, and other industries. Oil-water separators, as a type of equipment used for oil-water separation, are widely used in chemical production and wastewater treatment. Their main function is to separate water-insoluble and relatively light oils or other organic substances from the water.

[0003] However, conventional oil-water separators use static separation, and then use an oil skimmer to scrape the oil layer floating on the water to other parts to complete the oil-water separation and then recover the material. This not only has poor separation effect, but also consumes too much time and reduces separation efficiency.

[0004] Therefore, existing oil-water separation devices suffer from drawbacks such as high equipment investment, low separation efficiency, and large space occupation, which greatly increases the production costs of enterprises. Utility Model Content

[0005] To address the aforementioned issues, this invention provides a continuous stratification oil separator, applicable to scenarios such as fragrance and flavor preparation and organic amine synthesis. It achieves continuous separation of light and heavy components in a closed environment. This invention features a large processing capacity, and the separation chambers can be enlarged or increased according to process requirements. It is energy-saving and consumption-reducing, requires no power equipment, has a simple structure, is easy to process, and can achieve continuous and efficient oil-water separation.

[0006] To achieve the above objectives, the present invention adopts the following technical solution: This utility model provides a continuous stratified oil separator, which includes a main body, an inlet located on one side of the upper part of the main body, and a water phase outlet located on the lower part of the other side of the main body. The main body is divided into multiple separation chambers by multiple partitions. One side of each separation chamber is provided with an oil phase chamber and a water phase chamber. Each separation chamber and the water phase chamber are connected to the oil phase chamber through pipes. One end of each partition is in contact with the inner wall of the main body, and the other end is provided with a drain port near the inner wall of the main body. The drain ports on any two adjacent partitions are staggered.

[0007] As a preferred embodiment of this utility model, both the upper part of the outer side of the individual separation chamber and the aqueous phase chamber are provided with oil drain ports, and the oil phase material is collected into the oil phase chamber through the oil drain ports and pipelines.

[0008] As a preferred embodiment of this utility model, a sight glass opening is also provided on the upper part of the outer side of the single separation chamber and the water phase chamber.

[0009] In a preferred embodiment of this utility model, the oil phase chamber is independently disposed within the water phase chamber via a second partition.

[0010] As a preferred embodiment of this utility model, the upper part of the outer side of the aqueous phase chamber is provided with a first liquid level gauge port, and the lower part is provided with a second liquid level gauge port.

[0011] As a preferred embodiment of this utility model, a third liquid level gauge port is provided on the upper part of the outer side of the oil phase chamber, and a fourth liquid level gauge port is provided on the lower part.

[0012] As a preferred embodiment of this utility model, the lower part of the outer side of the oil phase chamber is provided with an oil phase outlet and a sewage outlet.

[0013] In a preferred embodiment of this utility model, the number of separation chambers is ≥3.

[0014] As a preferred embodiment of this utility model, the main body is a cuboid structure.

[0015] Compared with the prior art, the present invention has the following beneficial effects: 1) The continuous stratification oil separator provided by this utility model realizes the continuous separation of light and heavy components of materials in a closed environment. The continuous stratification oil separator of this utility model has a large processing capacity.

[0016] 2) The continuous stratified oil separator provided by this utility model can be enlarged or increased in number according to process requirements, saving energy and reducing consumption, requiring no power equipment, with a simple structure and convenient processing.

[0017] 3) This utility model provides a continuous layered oil separator that can be applied to chemical fields such as fragrance and flavor preparation and organic amine synthesis.

[0018] 4) The continuous stratification oil separator provided by this utility model allows the oil-water mixture to flow slowly in each chamber, so that the oil and water are completely separated. The oil phase material is collected through the oil outlet of each chamber and finally discharged into the oil phase chamber; the water phase material flows to the water phase chamber and is discharged through the water phase outlet, realizing the continuous separation of light and heavy components of the material in a closed environment. Attached Figure Description

[0019] To more clearly illustrate the technical solutions in the embodiments of this application or the prior art, the drawings used in the description of the embodiments or the prior art will be briefly introduced below. Obviously, the drawings described below are only some embodiments of this application. For those skilled in the art, other drawings can be obtained based on these drawings without creative effort.

[0020] Figure 1 This is a top view of the present invention.

[0021] Figure 2 This is a front view of the present invention.

[0022] Figure 3 This is a diagram of the interface when this utility model is in operation.

[0023] In the diagram, 1. Main body; 1-1. Feed inlet; 2. Separation chamber; 3. Baffle; 3-1. Second baffle; 4. Drain outlet; 5. Oil outlet; 6. Sight glass; 7. Oil phase chamber; 7-1. Third level gauge outlet; 7-2. Fourth level gauge outlet; 7-3. Sewage outlet; 7-4. Oil phase inlet; 8. Aqueous phase chamber; 8-1. First level gauge outlet; 8-2. Second level gauge outlet; 9. Aqueous phase outlet; 10. Oil phase outlet. Detailed Implementation

[0024] To further understand the content of this utility model, a detailed description of this utility model will be provided in conjunction with the accompanying drawings and embodiments.

[0025] The present application will be further described in detail below with reference to the accompanying drawings and embodiments. It is understood that the specific embodiments described herein are merely illustrative of the relevant utility model and not intended to limit the utility model. Furthermore, it should be noted that, for ease of description, only the parts related to the utility model are shown in the accompanying drawings. The terms "first," "second," etc., used in this utility model are provided for the convenience of describing the technical solution of this utility model and have no specific limiting effect; they are all general terms and do not constitute a limitation on the technical solution of this utility model. It should be noted that, in the absence of conflict, the embodiments and features in the embodiments of this application can be combined with each other. In the description of this utility model, it should be noted that the terms "center," "upper," "lower," "left," "right," "vertical," "horizontal," "inner," and "outer," etc., indicate the orientation or positional relationship based on the orientation or positional relationship shown in the accompanying drawings, and 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 on this utility model. In addition, the terms "first," "second," and "third" are used for descriptive purposes only and should not be construed as indicating or implying relative importance. Unless otherwise explicitly specified and limited, the terms "installation," "connection," and "linking" should be interpreted broadly. For example, they can refer to fixed connections, detachable connections, or integral connections; they can refer to mechanical connections or electrical connections; they can refer to direct connections or indirect connections 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. Multiple technical solutions in the same embodiment, as well as multiple technical solutions in different embodiments, can be arranged and combined to form new technical solutions that do not contradict or conflict, all of which are within the scope of protection claimed by this utility model.

[0026] Example 1 See Figure 1 and Figure 2This embodiment provides a continuous stratified oil separator, which includes a rectangular parallelepiped body 1, an inlet 1-1 located on one side of the upper part of the body 1, and a water phase outlet 9 located on the lower part of the other side of the body 1. The body 1 is divided into multiple separation chambers 2 by multiple partitions 3 (the number of separation chambers 2 can be increased according to process requirements; in this embodiment, there are 4 separation chambers 2). An oil phase chamber 7 and a water phase chamber 8 are located on one side of each separation chamber 2. Each separation chamber 2 and the water phase chamber 8 are connected to the oil phase chamber 7 via pipes. One end of each partition 3 contacts the inner wall of the body 1 (in this embodiment, the partition is a thin rectangular parallelepiped, with its long side contacting the top and bottom plates of the body, and one end of its short side contacting the side plate of the body). A drain outlet 4 is located at the other end near the inner wall of the body 1. The drain outlets 4 on any two adjacent partitions 3 are staggered, allowing material in a single separation chamber to flow to an adjacent chamber through the drain outlet. Figure 1 The north and south are marked in the middle. The drain port 4 on the first separation chamber 2 is located at the south end, the drain port 4 on the second separation chamber 2 is located at the north end, the drain port 4 on the third separation chamber 2 is located at the south end, and the drain port 4 on the fourth separation chamber 2 is located at the north end. The fourth separation chamber 2 is adjacent to the aqueous phase chamber 8.

[0027] Both the upper part of the outer side of the individual separation chamber 2 and the aqueous phase chamber 8 are provided with oil drain ports 5. The oil phase material is collected in the oil phase chamber 7 through the oil drain ports 5 and the pipeline. The oil phase chamber 7 is provided with an oil phase inlet 7-4. A valve can also be provided on the oil drain port 5 (this is a conventional solution and is not shown in the figure) to facilitate observation of the start of oil discharge after oil-water separation.

[0028] A sight glass port 6 is also provided on the upper part of the outer side of the individual separation chamber 2 and the aqueous phase chamber 8.

[0029] The oil phase chamber 7 can be located at any position. In this embodiment, a separate chamber is created in the aqueous phase chamber 8 by means of the second partition 3-1 to serve as the oil phase chamber 7.

[0030] The upper part of the outer side of the aqueous phase chamber 8 is provided with a first liquid level gauge port 8-1, and the lower part is provided with a second liquid level gauge port 8-2.

[0031] The upper part of the outer side of the oil phase chamber 7 is provided with a third liquid level gauge port 7-1, and the lower part is provided with a fourth liquid level gauge port 7-2. The lower part of the outer side of the oil phase chamber 7 is provided with an oil phase outlet port 10 and a drain port 7-3.

[0032] See Figure 1 and Figure 3The oil-water mixture is injected from the feed inlet 1-1 and flows from north to south in the first separation chamber 2. It then enters the adjacent separation chamber 2 through the drain port 4 on the partition 3, flowing from south to north, and so on, until it enters the aqueous phase chamber 8.

[0033] The oil phase material in the upper part of the separation chamber 2 flows out from the oil outlet 5, collects through the corresponding pipes, enters the oil phase chamber 7 from the oil phase inlet 7-4, and is finally discharged from the oil phase outlet 10; the water phase material collects into the water phase chamber 8 and is finally discharged from the water phase outlet 9.

[0034] Each separation chamber 2 is also equipped with a sight glass 6 for observing the oil-water interface.

[0035] The outer side of the water phase chamber 8 is provided with a first liquid level gauge port 8-1 and a second liquid level gauge port 8-2, and the outer side of the oil phase chamber 7 is provided with a third liquid level gauge port 7-1 and a fourth liquid level gauge port 7-2, for observing the liquid level of the oil separator.

[0036] The oil phase chamber 7 is also equipped with a drain outlet 7-3.

[0037] As can be seen, the continuous stratification oil separator provided by this utility model allows the oil-water mixture to flow slowly in each chamber, resulting in complete stratification of oil and water. The oil phase is collected through the oil outlet of each chamber and finally discharged into the oil phase chamber; the water phase flows to the water phase chamber and is discharged through the water phase outlet, thus achieving continuous separation of light and heavy components of the material in a closed environment.

[0038] The present invention and its embodiments have been described above illustratively. This description is not restrictive, and the figures shown are only one embodiment of the present invention; the actual structure is not limited thereto. Therefore, if those skilled in the art are inspired by this description and design similar structures and embodiments without departing from the inventive spirit of the present invention, such designs should fall within the protection scope of the present invention.

Claims

1. A continuous stratified oil separator, characterized in that, The continuous stratified oil separator includes a main body, an inlet located on one side of the upper part of the main body, and a water phase outlet located on the lower part of the other side of the main body. The main body is divided into multiple separation chambers by multiple partitions. One side of each separation chamber is provided with an oil phase chamber and a water phase chamber. Each separation chamber and the water phase chamber are connected to the oil phase chamber through pipes. One end of each partition is in contact with the inner wall of the main body, and the other end is provided with a drain port near the inner wall of the main body. The drain ports on any two adjacent partitions are staggered.

2. The continuous stratified oil separator according to claim 1, characterized in that, Both the individual separation chamber and the upper part of the aqueous phase chamber are provided with oil drain ports, and the oil phase material is collected into the oil phase chamber through the oil drain ports and pipelines.

3. A continuous stratified oil separator according to claim 1, characterized in that, Each separate chamber and the upper part of the aqueous phase chamber are also provided with a sight glass opening.

4. A continuous stratification oil separator according to any one of claims 1-3, characterized in that, The oil phase chamber is independently located within the water phase chamber via a second partition.

5. A continuous stratified oil separator according to claim 1, characterized in that, The upper part of the outer side of the aqueous phase chamber is provided with a first liquid level gauge port, and the lower part is provided with a second liquid level gauge port.

6. A continuous stratified oil separator according to claim 1, characterized in that, The upper part of the outer side of the oil phase chamber is provided with a third liquid level gauge port, and the lower part is provided with a fourth liquid level gauge port.

7. A continuous stratified oil separator according to claim 1, characterized in that, The lower part of the outer side of the oil phase chamber is provided with an oil phase outlet and a sewage outlet.

8. A continuous stratified oil separator according to claim 1, characterized in that, The number of separation chambers is ≥3.

9. A continuous stratified oil separator according to claim 1, characterized in that, The main body is a cuboid structure.

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