Water separator

By using inlet and outlet inclined plate assemblies to extend the flow path in the water separator and utilizing gravity differences to separate droplets, the problems of low separation efficiency and high cost in traditional devices are solved, achieving efficient and economical liquid separation.

CN224071236UActive Publication Date: 2026-04-03WUXI HONGDINGHUA CHEM EQUIP CO LTD
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Patent Information

Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2025-04-18
Publication Date
2026-04-03

AI Technical Summary

Technical Problem

In the existing technology, traditional gravity settling tanks and inclined plate or inclined tube separation devices have problems such as low separation efficiency, difficulty in handling emulsified oil or high viscosity fluids, complex structure and high cost in the oil-water separation process.

Method used

Design a water separator that uses an inlet inclined plate assembly and an outlet inclined plate assembly to form multiple diversion channels. Combined with a central baffle and an inclined grid plate, the flow path is extended, and the gravity difference is used to promote droplet sedimentation, thereby improving separation efficiency and reducing energy consumption and equipment wear.

Benefits of technology

It improves liquid separation efficiency, ensures pure liquid enters the next process, reduces energy consumption and equipment wear, and has a simple structure and low cost.

✦ Generated by Eureka AI based on patent content.

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    Figure CN224071236U_ABST
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Abstract

The utility model provides a water separator which comprises a shell, and a material inlet is formed in the upper end of the vertical side face of the shell; the feeding inclined plate assembly and the discharging inclined plate assembly are both installed at the end, close to the material inlet, in the shell, a plurality of flow dividing channels are formed in the feeding inclined plate assembly and the discharging inclined plate assembly, and liquid to be separated passes through the flow dividing channels. A center partition plate vertically arranged between the feeding inclined plate assembly and the discharging inclined plate assembly is further installed between the feeding inclined plate assembly and the discharging inclined plate assembly, and materials are limited to pass through the feeding inclined plate assembly and then enter the discharging inclined plate assembly. And the water phase outlet and the oil phase outlet are formed in the side surface of the shell. According to the utility model, the structure with the inclined plate component is arranged in the shell to disperse materials, the flow path can be effectively prolonged, liquid with high drop settling density is promoted to sink by utilizing gravity difference, the liquid separation efficiency is improved, the energy consumption and the equipment abrasion are reduced, and pure liquid is ensured to enter the next process.
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Description

Technical Field

[0001] This utility model relates to the field of extraction tanks, and in particular to the field of liquid separation technology, specifically a water separator. Background Technology

[0002] In the chemical, petroleum, and environmental protection fields, the efficient separation of oil-water mixtures is a core step in resource recovery and wastewater treatment. Traditional gravity settling tanks rely on density differences to achieve stratification, but their separation efficiency is low and they are difficult to handle emulsified oils or high-viscosity fluids.

[0003] Therefore, to improve separation efficiency, existing technologies mostly employ inclined plate or inclined tube separation devices, which promote oil-water separation by increasing the sedimentation area and extending the flow path. However, such structures still have significant drawbacks. The inclined plate coverage area is limited to the middle of the tank, and the edge separation efficiency is still not ideal. Some products are designed to adapt to fluids of different viscosities, but their structures are complex and their manufacturing costs are high, making it difficult to balance separation accuracy, stability, and cost. Summary of the Invention

[0004] In view of the shortcomings of the prior art described above, the purpose of this utility model is to provide a water separator to solve the difficulties of the prior art.

[0005] To achieve the above and other related objectives, this utility model provides a water separator, comprising:

[0006] Housing 1, with a material inlet N1 installed at the upper end of the vertical side of the housing 1;

[0007] The infeed inclined plate assembly and the discharge inclined plate assembly are both installed inside the housing 1 at one end near the material inlet N1, and multiple diversion channels 3 are formed inside the infeed inclined plate assembly and the discharge inclined plate assembly for the liquid to be separated to pass through.

[0008] A vertically arranged central partition 6 is also installed between the feed inclined plate assembly and the discharge inclined plate assembly to restrict the material from passing through the feed inclined plate assembly and then entering the discharge inclined plate assembly.

[0009] Aqueous phase outlet N2 and oil phase outlet N3 are installed on the side of housing 1.

[0010] According to the preferred embodiment, a drain port N4 is also provided at the bottom of the housing 1.

[0011] According to the preferred embodiment, the left and right sides of the housing 1 are integrally provided with a rectangular end 101 and an arc-shaped end 102. The rectangular end 101 is equipped with an inlet inclined plate assembly and an outlet inclined plate assembly, and the arc-shaped end 102 forms a buffer zone.

[0012] According to the preferred embodiment, the feed inclined plate assembly and the discharge inclined plate assembly respectively include:

[0013] Bottom channel steel frame 8, which is installed on the bottom inner side of the housing 1;

[0014] An angle steel limiting frame 9 is installed on the bottom channel steel frame 8;

[0015] Inclined grating 4, a plurality of the inclined grating 4 are inclined and equally spaced within the angle steel limiting frame 9;

[0016] A spacer tube 10 is installed perpendicular to the inclined grid plate 4 and passes through multiple inclined grid plates 4. Both ends of the spacer tube 10 are locked with nuts.

[0017] According to the preferred embodiment, the included angle between the inclined grating plate 4 and the bottom channel steel frame 8 is 43°.

[0018] According to the preferred embodiment, each of the inclined grid plates 4 is provided with mounting holes corresponding to the spacer tube 10.

[0019] According to the preferred embodiment, the inclined grid plates 4 in the feed inclined plate assembly and the discharge inclined plate assembly are arranged in opposite directions.

[0020] According to the preferred embodiment, the thickness of the inclined grating plate 4 is 2mm.

[0021] According to the preferred embodiment, the lengths of the adjacent inclined grid plates 4 on both sides are different, while the lengths of the inclined grid plates 4 on the middle diagonal are the same.

[0022] According to the preferred embodiment, the opening positions for installing the spacer tube 10 are different in the diagonal grid plate 4 with the same length on the middle diagonal.

[0023] According to the preferred embodiment, the aqueous phase outlet N2 and the oil phase outlet N3 are located on the same side of the housing 1 as the material inlet N1.

[0024] According to the preferred embodiment, a junction N6 for connecting a thermometer is also installed on the top of the housing 1 above the arc-shaped end 102.

[0025] According to the preferred embodiment, the top of the housing 1, located at the arc-shaped end 102 and the top of the side near the material inlet N1, is also equipped with a No. 1 handhole N8 and a No. 2 handhole N7, respectively.

[0026] This invention utilizes a structure with inclined plate components installed inside the housing to disperse materials and effectively extend the flow path. It also leverages gravity differences to promote the settling of liquids with high droplet density, thereby improving liquid separation efficiency, reducing energy consumption and equipment wear, and ensuring that pure liquid enters the next process.

[0027] The preferred embodiments of the present invention will be described in more detail below with reference to the accompanying drawings, so as to facilitate an understanding of the features and advantages of the present invention. Attached Figure Description

[0028] Figure 1 This is shown as the front view of the present invention;

[0029] Figure 2 This is a top view of the present invention;

[0030] Figure 3 The image shown is a left view of this utility model.

[0031] Figure 4 The diagram shown is a left-side internal structural diagram of this utility model;

[0032] Figure 5 The diagram shown is an enlarged view of the inclined plate assembly in this utility model.

[0033] Figure 6 This is an enlarged view of the inclined plate assembly from another perspective in this utility model.

[0034] Label Explanation

[0035] 1. Shell; 101. Rectangular end; 102. Arc-shaped end; 3. Multiple diversion channels; 4. Slanted grid plate; 6. Central partition plate;

[0036] 8. Bottom channel steel frame; 9. Angle steel limiting frame; 10. Spacer tube;

[0037] N1, Material Inlet; N2, Aqueous Phase Outlet; N3, Oil Phase Outlet; N4, Drain Port; N6, Connector; N7, Manhole No. 2; N8, Manhole No. 1. Detailed Implementation

[0038] To make the objectives, technical solutions, and advantages 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. The same reference numerals in the drawings represent the same components. It should be noted that the described embodiments are only some, not all, of the embodiments of this utility model. All other embodiments obtained by those skilled in the art based on the described embodiments of this utility model without creative effort are within the scope of protection of this utility model.

[0039] Compared to the embodiments shown in the accompanying drawings, feasible embodiments within the scope of protection of this utility model may have fewer components, have other components not shown in the drawings, different components, components arranged differently, or components with different connections, etc. Furthermore, two or more components shown in the drawings may be implemented in a single component, or a single component shown in the drawings may be implemented as multiple separate components.

[0040] Unless otherwise defined, the technical or scientific terms used herein shall have the ordinary meaning understood by one of ordinary skill in the art to which this invention pertains. The terms “first,” “second,” and similar terms used in this patent application specification and claims do not indicate any order, quantity, or importance, but are merely used to distinguish different components. Similarly, “an” or “a” and similar terms do not necessarily indicate a quantity limitation. Terms such as “comprising” or “including” mean that the element or object preceding the word encompasses the element or object listed following the word and its equivalents, without excluding other elements or objects. Terms such as “connected” or “linked” are not limited to physical or mechanical connections, but can include electrical connections, whether direct or indirect. Terms such as “upper,” “lower,” “left,” and “right” are used only to indicate relative positional relationships; these relative positional relationships may change accordingly when the absolute position of the described object changes.

[0041] This invention proposes a water separator for use in liquid-liquid separation processes of different densities. This invention does not limit the type of liquid, but the structure of this water separator is particularly suitable for water-oil separation.

[0042] In general, the water separator proposed in this utility model mainly includes a shell 1, an inlet inclined plate assembly and an outlet inclined plate assembly, a water phase outlet N2 and an oil phase outlet N3. See also... Figure 1 It shows the arrangement of the housing 1, the feed sloping plate assembly and the discharge sloping plate assembly, the water phase outlet N2 and the oil phase outlet N3.

[0043] To achieve rapid and high-precision separation of water and oil in an extraction tank, this invention addresses the shortcomings of existing technologies that primarily employ inclined plate or inclined tube separation devices. These devices increase the sedimentation area and extend the flow path to promote oil-water separation. However, such structures have significant drawbacks: the inclined plate coverage area is limited to the middle of the tank, and the edge separation efficiency remains unsatisfactory. Furthermore, some products, designed to accommodate fluids of varying viscosities, suffer from complex structures and high manufacturing costs, making it difficult to balance separation accuracy, stability, and cost. Therefore, the technical solution provided in this embodiment utilizes a structure with inclined plate components installed within the shell 1 to disperse the material and effectively extend the flow path. This leverages gravity differences to promote the settling of liquids with higher droplet density, improving liquid separation efficiency, reducing energy consumption and equipment wear, and ensuring that pure liquid proceeds to the next process.

[0044] As mentioned above, Figure 1 As shown, the housing 1 consists of two parts, including a rectangular end 101 and an arc-shaped end 102 integrally formed on the left and right sides. The rectangular end 101 is used to install the feed ramp assembly and the discharge ramp assembly, while the arc-shaped end 102 forms a buffer zone. In addition, to facilitate the feeding and discharging of materials, a material inlet N1 is installed at the upper end of the vertical side of the housing 1. At the same time, the liquid separated by the feed ramp assembly and the discharge ramp assembly are respectively provided with corresponding water phase outlet N2 and oil phase outlet N3 on the side of the housing 1, and are located on the same side as the material inlet N1. This is conducive to the centralized input and output of liquids, which facilitates quick operation by operators and improves the feeding and discharging time.

[0045] like Figure 2 As shown, a junction N6 for connecting a thermometer is also installed on the top of the housing 1 above the arc-shaped end 102. A first hand hole N8 and a second hand hole N7 are also installed on the top of the housing 1 on the side of the arc-shaped end 102 and the side near the material inlet N1, respectively.

[0046] Preferably, a drain port N4 is also provided at the bottom of the shell 1. Since the water phase outlet N2 and the oil phase outlet N3 are both located above the middle of the shell 1, a drain port N4 located at the bottom is provided to facilitate the output of excess liquid in the shell 1 and avoid the liquid being concentrated at the bottom, which would cause the contaminant to accumulate in the shell 1.

[0047] It should be specifically noted that the feed inclined plate assembly and the discharge inclined plate assembly used to separate liquids of different densities are both installed inside the housing 1 at one end near the material inlet N1, and multiple diversion channels 3 are formed within the feed inclined plate assembly and the discharge inclined plate assembly. After the liquid to be separated passes through, a vertically arranged central baffle 6 is also installed between the feed inclined plate assembly and the discharge inclined plate assembly to restrict the material from passing through the feed inclined plate assembly and then entering the discharge inclined plate assembly. The "louvered" arrangement of the feed inclined plate assembly and the discharge inclined plate assembly helps to extend the fluid flow path, causing the droplets to coalesce and fall after impacting the plate surface due to inertia.

[0048] Specifically, the feed inclined plate assembly and the discharge inclined plate assembly respectively include a bottom channel steel frame 8, an angle steel limiting frame 9, an inclined grating plate 4, and a spacer tube 10. The bottom channel steel frame 8 is installed on the bottom inner side of the housing 1 to support the inclined grating plate 4 on the inner upper side of the housing 1. Then, the angle steel limiting frame 9 is installed on the bottom channel steel frame 8 to limit the installation position of the inclined grating plate 4 and limit the position of its four corners to facilitate the quick alignment and installation of the internal inclined grating plate 4.

[0049] Based on this, multiple inclined grating plates 4 are set at equal intervals within the angle steel limiting frame 9. Multiple spacer tubes 10 are inserted between the multiple inclined grating plates 4 to achieve positioning and installation. Correspondingly, each inclined grating plate 4 has a corresponding spacer tube 10 with an installation hole. Preferably, the angle between the inclined grating plate 4 and the bottom channel steel frame 8 is 43°, and the spacer tube 10 is set perpendicular to the inclined grating plate 4. After alignment and installation, the two ends of the spacer tube 10 are locked with nuts to prevent the inclined grating plate 4 from loosening due to the entry of a large amount of material after installation. At the same time, the thickness of the inclined grating plate 4 is 2mm, which can also effectively ensure the stability of the liquid during the separation process.

[0050] In addition, the feed sloping plate assembly and the discharge sloping plate assembly form a liquid buffer through the arc end 102. In order to achieve the continuity of the path, the flow direction is changed to reduce the fluid velocity and the gravity difference is used to promote the sinking of liquid with high droplet settling density. The inclined grid plates 4 in the feed sloping plate assembly and the discharge sloping plate assembly are set in opposite directions to ensure that pure gas or liquid enters the next process, reducing energy consumption and equipment wear.

[0051] Preferably, the lengths of the adjacent inclined grid plates 4 on both sides are different, while the lengths of the inclined grid plates 4 on the middle diagonal are the same. In order to ensure that the inclined grid plates 4 of the same length in the middle position can also be aligned, the opening positions for installing the spacer tube 10 in the inclined grid plates 4 of the same length on the middle diagonal are different.

[0052] The above embodiments are merely illustrative of the principles and effects of this utility model and are not intended to limit the scope of this utility model. Any person skilled in the art can modify or alter the above embodiments without departing from the spirit and scope of this utility model. Therefore, all equivalent modifications or alterations made by those skilled in the art without departing from the spirit and technical concept disclosed in this utility model should still be covered by the claims of this utility model.

Claims

1. A water separator characterized by, It comprises: A housing (1), the upper end of the vertical side of which is provided with a material inlet (N1); A material inlet chute assembly and a material outlet chute assembly, both of which are installed on one end of the housing (1) close to the material inlet (N1) and form a plurality of shunt channels (3) in the material inlet chute assembly and the material outlet chute assembly for the liquid to be separated to pass through; A center partition (6) is also installed vertically between the material inlet chute assembly and the material outlet chute assembly to restrict the material from entering the material outlet chute assembly after passing through the material inlet chute assembly; A water phase outlet (N2) and an oil phase outlet (N3) are both installed on the side of the housing (1).

2. The water separator of claim 1, wherein The left and right sides of the housing (1) are integrally provided with a rectangular end (101) and an arc-shaped end (102), the material inlet chute assembly and the material outlet chute assembly are installed in the rectangular end (101), and a buffer zone is formed in the arc-shaped end (102).

3. The water separator of claim 2, wherein, The material inlet chute assembly and the material outlet chute assembly each comprise: A bottom channel steel frame (8) installed on the inner side of the bottom of the housing (1); An angle steel limiting frame (9) installed on the bottom channel steel frame (8); A plurality of inclined grid plates (4) are inclined and equally spaced in the angle steel limiting frame (9); A distance pipe (10) is perpendicular to the inclined grid plate (4) and is installed through a plurality of inclined grid plates (4), and the two ends of the distance pipe (10) are locked by nuts.

4. The water separator of claim 3, wherein The inclined grid plates (4) in the material inlet chute assembly and the material outlet chute assembly are oppositely arranged.

5. The water separator of claim 4, wherein, The lengths of the adjacent inclined grid plates (4) located on both sides are different, and the lengths of the inclined grid plates (4) located on the middle diagonal line are consistent.

6. The water separator of claim 5, wherein, The water phase outlet (N2) and the oil phase outlet (N3) are arranged on the same side of the housing (1) as the material inlet (N1).

7. The water separator of claim 6, wherein A bundle joint (N6) connected to a thermometer is also installed on the top of the arc-shaped end (102) of the housing (1).