Solid-liquid-gas three-phase separator

Abstract

This utility model belongs to the technical field of separation equipment, and specifically relates to a solid-liquid-gas three-phase separator. It includes a cylindrical body with an internal separation chamber, and has an inlet, an outlet, and a drain connected thereto. A filter assembly with filter holes is installed inside the separation chamber. The filter assembly is used to filter and screen the gas. The inlet and outlet are located above the filter assembly. A baffle is installed in the separation chamber. A cyclone demister passes through the filter assembly and the baffle, with its outlet located between the baffle and the outlet. The gas to be separated into solid, liquid, and gas phases is discharged through the inlet. Because the baffle is installed above the inlet, the gas moves downwards through the filter assembly, which filters out the powder. The liquid is discharged through the drain. The gas then enters the cyclone demister to separate the liquid. Finally, the gas is discharged through the outlet, achieving high separation efficiency of the solid, liquid, and gas phases in the gas.

Description

Technical Field

[0001] This utility model belongs to the field of separation equipment technology, and specifically relates to a solid-liquid-gas three-phase separator. Background Technology

[0002] A three-phase separator is a device used to separate mixtures of solid, liquid, and gas phases. It has wide applications in many fields such as oil and gas, wastewater treatment, and biofuel production.

[0003] Gravity sedimentation separation: Separation is achieved by utilizing the density differences of the three phases under the action of gravity.

[0004] Centrifugal separation principle: High-speed rotation generates centrifugal force, causing solid particles and liquids to move towards the container wall under the action of centrifugal force, thereby separating them from the gas. Problems with gravity sedimentation separation technology: Separation efficiency is limited; gravity sedimentation separation efficiency is closely related to factors such as particle size and fluid velocity, resulting in poor separation effects; centrifugal separation principle has high requirements for feed materials and poor separation effect for certain materials. Utility Model Content

[0005] To address the aforementioned technical problems, embodiments of the present invention provide a solid-liquid-gas three-phase separator.

[0006] To achieve the above objectives, the embodiments of this application adopt the following technical solutions:

[0007] This application provides a solid-liquid-gas three-phase separator, which includes a cylinder, a filter assembly, a baffle plate, and a cyclone demister. The cylinder has a separation chamber inside, with an inlet, an outlet, and a drain connected thereto. The filter assembly, having filter holes, is installed within the separation chamber and is used for filtering and sieving the gas. The inlet and outlet are located above the filter assembly, and the drain is located below it. The baffle plate is installed in the separation chamber, between the inlet and outlet, with the inlet located below the baffle plate. The cyclone demister passes through the filter assembly and the baffle plate, with its outlet located between the baffle plate and the outlet, and its inlet located between the filter assembly and the drain.

[0008] In this embodiment, the gas to be separated into solid, liquid, and gas phases is discharged through the air inlet. Since the baffle is installed above the air inlet, the gas moves downwards and passes through the filter assembly. The filter assembly filters the gas to remove powder, and the liquid is discharged through the drain port. Then, the gas enters the cyclone demister to separate the liquid. Finally, the gas is discharged through the air outlet, thus achieving the separation of solid, liquid, and gas phases in the gas. The separation efficiency is high and meets practical needs.

[0009] In some embodiments, the solid-liquid-gas three-phase separator further includes a wire mesh demister installed in the separation chamber, located between the outlet of the cyclone demister and the gas outlet, and the wire mesh demister is used to remove liquid from the gas.

[0010] In some embodiments, the filter assembly includes a first filter plate sleeved on the outer side of the cyclone demister, the periphery of the first filter plate being connected to the separation chamber, the filter holes on the first filter plate having a diameter of 2 mm, and the air inlet being located on the side wall of the cylinder between the partition and the first filter plate.

[0011] In some embodiments, a first separation chamber is formed between the partition and the first filter plate, and a first drain outlet communicating with the first separation chamber is provided on the cylinder.

[0012] In some embodiments, the filter assembly further includes a second filter plate sleeved on the outside of the cyclone demister. The periphery of the second filter plate is connected to the separation chamber. The filter holes on the second filter plate have a diameter of 1 mm. The second filter plate has an included angle with the first filter plate and is located below the first filter plate.

[0013] In some embodiments, a second separation chamber is formed between the second filter plate and the first filter plate, and a second drain outlet communicating with the second separation chamber is provided on the cylinder.

[0014] In some embodiments, the filter assembly further includes a third filter plate sleeved on the outside of the cyclone demister. The periphery of the third filter plate is connected to the separation chamber. The filter pores on the third filter plate have a diameter of 0.5 mm. The third filter plate has an included angle with the second filter plate and is located below the second filter plate.

[0015] In some embodiments, a third separation chamber is formed between the third filter plate and the second filter plate, and a third drain outlet communicating with the third separation chamber is provided on the cylinder.

[0016] In some embodiments, the solid-liquid-gas three-phase separator further includes a viewing mirror mounted on the cylinder for observing the separation chamber.

[0017] In some embodiments, the solid-liquid-gas three-phase separator further includes support legs mounted on the cylinder body for supporting the cylinder body. Attached Figure Description

[0018] To more clearly illustrate the technical solutions in the embodiments of this utility model 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 utility model. For those skilled in the art, other drawings can be obtained based on these drawings without creative effort.

[0019] Figure 1 This is a schematic diagram of the solid-liquid-gas three-phase separator provided in an embodiment of the present invention;

[0020] Figure 2 A schematic diagram of the structure of the first filter plate provided in an embodiment of this utility model;

[0021] Figure 3 This is a schematic diagram of the structure of the second filter plate provided in an embodiment of the present utility model;

[0022] Figure 4 This is a schematic diagram of the structure of the third filter plate provided in an embodiment of the present invention. Detailed Implementation

[0023] The embodiments of this application will now be described in detail with reference to the accompanying drawings.

[0024] In the description of this application, it should be understood that the terms "center", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", etc., indicate the orientation or positional relationship based on the orientation or positional relationship shown in the accompanying drawings. They are only for the convenience of describing this application 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. Therefore, they should not be construed as limitations on this application.

[0025] The terms "first" and "second" are used for descriptive purposes only and should not be construed as indicating or implying relative importance or implicitly specifying the number of technical features indicated. Therefore, a feature defined as "first" or "second" may explicitly or implicitly include one or more of that feature. In the description of this application, unless otherwise stated, "a plurality of" means two or more.

[0026] In the description of this application, it should be noted that, unless otherwise expressly specified and limited, the terms "installation," "connection," and "linking" 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 between two components. Those skilled in the art can understand the specific meaning of the above terms in this application based on the specific circumstances.

[0027] like Figures 1 to 4 The embodiment of this application provides a solid-liquid-gas three-phase separator, which includes a cylinder 100, a filter assembly, a baffle plate 8, and a cyclone demister 6. The cylinder 100 has a separation chamber inside, with an air inlet 1, an air outlet 10, and a liquid outlet 5 connected thereto. The air inlet 1, air outlet 10, and liquid outlet 5 are respectively connected to the separation chamber. The filter assembly has filter holes and is installed inside the separation chamber. The filter assembly is used to filter and sieve the gas. The filter assembly can be installed inside the separation chamber by welding or screw connection. The filter holes on the filter assembly are used to sieve and filter powder in the gas. The air inlet 1 and air outlet 10 are located above the filter assembly, and the liquid outlet 5 is located below the filter assembly. The baffle plate 8 is installed in the separation chamber and located between the air inlet 1 and air outlet 10. The baffle plate 8 prevents untreated gas from being directly discharged through the air outlet 10. The air inlet 1 is located below the baffle plate 8. The cyclone demister 6 is installed on the filter assembly and the baffle 8. The outlet of the cyclone demister 6 is located between the baffle 8 and the air outlet 10, and the inlet of the cyclone demister 6 is located between the filter assembly and the drain outlet 5. In addition, the part of the cyclone demister 6 located on the upper side of the baffle 8 has an overflow port 7 to prevent liquid accumulation.

[0028] In this embodiment, the gas to be separated into solid, liquid, and gas phases is discharged through the air inlet 1. Since the baffle 8 is installed above the air inlet 1, the gas moves downwards and passes through the filter assembly. The filter assembly filters the gas to remove powder, and the liquid is discharged through the drain port 5. Then, the gas enters the cyclone demister 6 to separate the liquid. Finally, the gas is discharged through the air outlet 10, thus achieving the separation of solid, liquid, and gas phases in the gas. The separation efficiency is high and meets the actual needs.

[0029] In some embodiments, the solid-liquid-gas three-phase separator further includes a wire mesh demister 9, which is installed in the separation chamber. The wire mesh demister 9 can be welded to the separation chamber. The wire mesh demister 9 is located between the outlet of the cyclone demister 6 and the gas outlet 10. The wire mesh demister 9 is used to remove liquid from the gas, and then the treated gas is discharged through the gas outlet 10.

[0030] In some embodiments, the filter assembly may include a first filter plate 2, which is sleeved on the outside of the cyclone demister 6. The periphery of the first filter plate 2 is connected to the separation chamber. The filter holes on the first filter plate 2 have a diameter of 2 mm. The air inlet 1 is located on the side wall of the cylinder 100 between the partition 8 and the first filter plate 2.

[0031] In some embodiments, a first separation chamber is formed between the partition plate 8 and the first filter plate 2, and a first drain port 11a connected to the first separation chamber is provided on the cylinder 100. The first drain port 11a is used to discharge the filtered and screened powder in the gas.

[0032] In some embodiments, the filter assembly may further include a second filter plate 3, which is sleeved on the outside of the cyclone demister 6. The periphery of the second filter plate 3 is connected to the separation chamber. The filter holes on the second filter plate 3 have a diameter of 1 mm. The second filter plate 3 has an included angle with the first filter plate 2 and is located below the first filter plate 2.

[0033] In some embodiments, a second separation chamber is formed between the second filter plate 3 and the first filter plate 2, and a second drain port 11b connected to the second separation chamber is provided on the cylinder 100. The second drain port 11b is used to discharge the filtered and screened powder in the gas.

[0034] In some embodiments, the filter assembly may further include a third filter plate 4, which is sleeved on the outside of the cyclone demister 6. The periphery of the third filter plate 4 is connected to the separation chamber. The filter holes on the third filter plate 4 have a diameter of 0.5 mm. The third filter plate 4 has an included angle with the second filter plate 3 and is located below the second filter plate 3.

[0035] In some embodiments, a third separation chamber is formed between the third filter plate 4 and the second filter plate 3, and a third drain port 11c connected to the third separation chamber is provided on the cylinder 100. The third drain port 11c is used to discharge the filtered and screened powder in the gas.

[0036] Based on the above, the first filter plate 2, the second filter plate 3, and the third filter plate 4 are arranged at an angle of 15° to each other. The maximum distance between the first filter plate 2 and the second filter plate 3 is 500 mm, and the maximum distance between the second filter plate 3 and the third filter plate 4 is 500 mm. Since the filter holes on the first filter plate 2 are larger than those on the second filter plate 3, and the filter holes on the second filter plate 3 are larger than those on the third filter plate 4, the filter holes on the first filter plate 2, the second filter plate 3, and the third filter plate 4 perform step-by-step filtration and sieving of the powder in the gas. The filtered and sieved gas then enters the cyclone demister 6 for gas-liquid separation.

[0037] Based on the above, the thickness of the first filter plate 2, the second filter plate 3, and the third filter plate 4 is 3mm. The outer and inner edges of the first filter plate 2, the second filter plate 3, and the third filter plate 4 are reserved with a 20mm diameter without openings. The inner edge of the cylinder 100 and the outer edge of the cyclone demister 6 are welded to the inner and outer edges, respectively. When the aperture is 2mm, the center distance between the two apertures is 3mm; when the aperture is 1mm, the center distance between the two apertures is 1.5mm; and when the aperture is 0.5mm, the center distance between the two apertures is 1mm.

[0038] In some embodiments, the solid-liquid-gas three-phase separator further includes a viewing mirror 12, which is installed on the cylinder 100 for observing the separation chamber, so as to observe the separation of gas and solid inside the separation chamber at any time.

[0039] In some embodiments, the solid-liquid-gas three-phase separator further includes a support leg 13, which is mounted on the cylinder 100 to support the cylinder 100.

[0040] The above-mentioned solid-liquid-gas three-phase separator is used to separate the mixed gas. The process parameters for the mixed gas are: 400 m³ / s. 3 / h CO2, containing 0.001% solid (6 kg / h) and 1% liquid (4 m³ / h) 3 The test results are shown in Table 1 below ( / h).

[0041] Table 1

[0042] Phase Before processing After processing Separation efficiency Export location gas <![CDATA[400m 3 / h]]> <![CDATA[360m 3 / h]]> 90% Air outlet 10 solid <![CDATA[0.004m 3 / h]]> <![CDATA[0.0032m 3 / h(4.8kg / h)]]> 80% First sewage outlet 11a, second sewage outlet 11b, third sewage outlet 11c liquid <![CDATA[4m 3 / h]]> <![CDATA[3.4m 3 / h]]> 85% Drain port 5

[0043] It should be noted that, unless otherwise specified, the embodiments and features described in this application can be combined with each other.

[0044] The above embodiments are only used to illustrate the technical solutions of this application and are not intended to limit this application. For those skilled in the art, this application can have various modifications and variations. Any modifications, equivalent substitutions, improvements, etc., made within the spirit and principles of this application should be included within the protection scope of this application.

Claims

1. A solid-liquid-gas three-phase separator, characterized by, include: The cylinder has an internal separation chamber with an air inlet, an air outlet, and a liquid outlet connected to it. A filter assembly with filter holes is installed in the separation chamber. The filter assembly is used to filter and sieve the gas. The air inlet and the air outlet are located above the filter assembly, and the liquid outlet is located below the filter assembly. A partition is installed in the separation chamber and located between the air inlet and the air outlet, with the air inlet located below the partition; A cyclone demister is installed between the filter assembly and the partition plate. The outlet of the cyclone demister is located between the partition plate and the air outlet, and the inlet of the cyclone demister is located between the filter assembly and the drain port.

2. The solid-liquid-gas three-phase separator according to claim 1, characterized in that, Also includes: A wire mesh demister is installed inside the separation chamber. The wire mesh demister is located between the outlet of the cyclone demister and the gas outlet. The wire mesh demister is used to remove liquid from the gas.

3. The solid-liquid-gas three-phase separator according to claim 1, wherein, The filtering component includes: The first filter plate is sleeved on the outside of the cyclone demister. The periphery of the first filter plate is connected to the separation chamber. The filter holes on the first filter plate have a diameter of 2 mm. The air inlet is located on the side wall of the cylinder between the partition and the first filter plate.

4. The solid-liquid-gas three-phase separator according to claim 3, characterized in that, A first separation chamber is formed between the partition plate and the first filter plate, and a first drain outlet connected to the first separation chamber is provided on the cylinder.

5. The solid-liquid-gas three-phase separator according to claim 3, characterized in that, The filtering component also includes: The second filter plate is sleeved on the outside of the cyclone demister. The periphery of the second filter plate is connected to the separation chamber. The filter holes on the second filter plate have a diameter of 1 mm. The second filter plate has an angle with the first filter plate and is located below the first filter plate.

6. The solid-liquid-gas three-phase separator according to claim 5, wherein, A second separation chamber is formed between the second filter plate and the first filter plate, and a second drain outlet connected to the second separation chamber is provided on the cylinder.

7. The solid-liquid-gas three-phase separator according to claim 5, wherein, The filtering component also includes: The third filter plate is sleeved on the outside of the cyclone demister. The periphery of the third filter plate is connected to the separation chamber. The filter holes on the third filter plate have a diameter of 0.5 mm. The third filter plate has an included angle with the second filter plate and is located below the second filter plate.

8. The solid-liquid-gas three-phase separator according to claim 7, characterized in that, A third separation chamber is formed between the third filter plate and the second filter plate, and a third drain outlet connected to the third separation chamber is provided on the cylinder.

9. The solid-liquid-gas three-phase separator according to any one of claims 1 to 8, wherein, Also includes: A fluoroscopic lens, mounted on the cylinder, is used to observe the separation chamber.

10. The solid-liquid-gas three-phase separator according to any one of claims 1 to 8, characterized in that, Also includes: The outriggers are mounted on the cylinder body to support it.

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