Gas-liquid separation system

Abstract

The present application relates to gas-liquid separation system, including separation tank, the inside of separation tank is provided with processing cavity, the middle part of processing cavity inside is provided with suspension refrigeration assembly, one side of the top of separation tank is provided with connecting pipe one, the other side of the top of separation tank is provided with connecting pipe two. Through the use of center rod and oscillating piece, the center rod moves with oscillating piece in flow-through cavity one and flow-through cavity two, the relative position changes, the position change of flow-through cavity one and flow-through cavity two is extruded and tightened by oscillating piece, the position change of oscillating piece makes flow-through cavity one and elastic heat exchange film two oscillate, so that water and small ice crystals on flow-through cavity one and elastic heat exchange film two gather, mix until fall, avoid water and liquid large area sustained coverage heat exchange wall and lead to heat exchange efficiency reduction, more avoid water and liquid large area condensation coverage in flow-through cavity one and elastic heat exchange film two heat exchange wall, thereby greatly improve the heat exchange capacity of heat exchange wall.

Description

Technical Field

[0001] This invention belongs to the field of refrigeration separation, specifically a gas-liquid separation system. Background Technology

[0002] As a core unit in chemical, oil and gas extraction, and environmental protection engineering, the technological evolution of gas-liquid separation systems has long been constrained by the contradiction between separation efficiency, anti-clogging ability, and material durability. When using refrigeration to separate liquid from gas, the liquid in the gas is prone to accumulate or even condense on the heat exchange wall during the refrigeration process, forming a barrier that reduces the heat exchange capacity of the heat exchange wall, thus greatly limiting the separation efficiency. Moreover, mechanical de-icing can easily damage the heat exchange wall. Therefore, the gas-liquid separation system was proposed. Summary of the Invention

[0003] The purpose of this section is to outline some aspects of embodiments of the present invention and to briefly describe some preferred embodiments. Simplifications or omissions may be made in this section, as well as in the abstract and title of this application, to avoid obscuring the purpose of these documents; however, such simplifications or omissions should not be construed as limiting the scope of the invention.

[0004] Given the following technical problems in the existing technology: when using refrigeration to separate liquid from gas, the liquid in the gas is prone to accumulate or even condense on the heat exchange wall during the refrigeration process, forming a barrier that reduces the heat exchange capacity of the heat exchange wall, thus greatly limiting the separation efficiency. Moreover, mechanical de-icing is very likely to damage the heat exchange wall.

[0005] To solve the above technical problems, the present invention provides the following technical solution: a gas-liquid separation system, including a separation tank, a processing chamber is opened on the inner side of the separation tank, a suspended cooling component is arranged in the middle of the inner side of the processing chamber, a connecting pipe one is arranged on one side of the top of the separation tank, and a connecting pipe two is arranged on the other side of the top of the separation tank. The connecting pipe one is connected to the processing chamber, and the connecting pipe two is connected to the processing chamber.

[0006] Both connecting pipe 2 and connecting pipe 1 extend into the processing chamber. An elastic heat exchange membrane 1 is provided on the inner wall of the processing chamber. A flow chamber 2 is provided between the elastic heat exchange membrane 1 and the inner wall of the processing chamber. Connecting pipe 2 and connecting pipe 1 pass through the elastic heat exchange membrane 1 from both sides of the separation tank. The elastic heat exchange membrane 1 is connected to both connecting pipe 2 and connecting pipe 1.

[0007] As a preferred technical solution for the gas-liquid separation system, a number of elastic connecting ropes are provided on the inner side of the flow cavity two, and the elastic connecting ropes are made of elastic material.

[0008] As a preferred technical solution for the gas-liquid separation system, a rotating chamber 1 is recessed on the inner side of the top of the separation tank, and a flow chamber 2 is connected to the rotating chamber 1. A sealing ring 1 is rotatably connected inside the rotating chamber 1, and several central rods are provided on the sealing ring 1. The central rods extend into the flow chamber 2, and several oscillating elements are provided on the central rods. The oscillating elements are in contact with the inner sides of both the elastic heat exchange membrane 1 and the elastic heat exchange membrane 2.

[0009] The central rod rotates at a small angle around the center of the processing chamber. During this rotation, the central rod, along with the oscillating element, moves and changes its relative position within the first and second flow chambers. The positions of the first and second flow chambers, which are compressed and tightened by the oscillating element, change. This change in the position of the oscillating element causes the first and second elastic heat exchange membranes to oscillate, resulting in the accumulation, mixing, and eventual fall of water and small ice crystals on the first and second elastic heat exchange membranes. This prevents water from continuously covering a large area of ​​the heat exchange wall, which would reduce heat exchange efficiency. Furthermore, it prevents water from condensing and covering a large area of ​​the heat exchange wall of the first and second elastic heat exchange membranes, thereby greatly improving the heat exchange capacity of the heat exchange wall. The side wall of the first and second elastic heat exchange membranes facing the inner cavity of the processing chamber is the heat exchange wall.

[0010] As a preferred technical solution for the gas-liquid separation system, the oscillating component includes an elastic connecting plate, an outer ring, and an extrusion block. Several outer rings are sleeved on the central rod. Three extrusion blocks are evenly arranged around the outer ring. Three elastic connecting plates are connected between the inner side of the outer ring and the central rod. The elastic connecting plate is made of a spring plate. Several connecting blocks are evenly arranged inside the rotating cavity. The material of the extrusion block is rubber.

[0011] The elastic connecting plate allows the outer ring and the extrusion block to rotate within a small range, and allows the outer ring to undergo micro-movements and vibrations during its movement, thereby enhancing the adaptability of the oscillating element to the first and second flow chambers and enhancing the oscillating element's ability to act on the first and second elastic heat exchange membranes.

[0012] As a preferred technical solution for the gas-liquid separation system, the separation tank has two symmetrically arranged fan-shaped movable cavities recessed inside. The fan-shaped movable cavities are connected to a rotating cavity. A rotating platform is rotatably connected to the inner side of the separation tank. A swing rod is connected between the rotating platform and a sealing ring. The swing rod is movably connected to the fan-shaped movable cavities.

[0013] The swing arm can swing back and forth within the fan-shaped movable cavity.

[0014] As a preferred technical solution for the gas-liquid separation system, the suspended refrigeration component includes a central column and an elastic heat exchange membrane II. The central column is provided on the inner top wall of the processing chamber, and the elastic heat exchange membrane II is provided on the outer side of the top of the central column. A flow chamber I is provided between the outer side of the central column and the elastic heat exchange membrane II. Several central rods are provided in the flow chamber I, and an oscillating element is provided on the central rod.

[0015] The central rod rotates at a certain angle within the second and first flow chambers.

[0016] As a preferred technical solution for the gas-liquid separation system, a second rotating chamber is recessed inside the top of the separation tank. The second rotating chamber is connected to the first flow chamber. A second sealing ring is rotatably connected inside the second rotating chamber. A connecting block is provided inside the second rotating chamber. The swing rod is connected to the second sealing ring through a connecting rod. A motor is provided inside the separation tank. The power output end of the motor is connected to the rotating table.

[0017] The motor controls the swing arm to rotate back and forth, causing the swing arm and the structure connected to the swing arm to rotate at a certain angle, with a maximum rotation angle of 8 to 16 degrees.

[0018] As a preferred technical solution for the gas-liquid separation system, a flow divider is provided in the middle of the bottom wall of the processing chamber, and a drain pipe is provided at the bottom of the separation tank, with the drain pipe connected to the edge of the bottom wall of the processing chamber.

[0019] The diversion seat causes the water to collect at the bottom edge of the treatment chamber. The drain pipe is a T-shaped pipe with a one-way valve inside, which only allows water to be discharged.

[0020] As a preferred technical solution for the gas-liquid separation system, a spiral blade is provided on the outer ring at the bottom of the central column, and the diameter of the spiral blade is three-quarters of the inner diameter of the processing chamber.

[0021] As a preferred technical solution for the gas-liquid separation system, the bottom of the separation tank is provided with an inlet pipe and an outlet pipe. The outlet pipe is connected to the bottom of the second elastic heat exchange membrane. The first flow chamber is connected to the outlet pipe, and the second flow chamber is connected to the inlet pipe.

[0022] The gas first moves downward through the processing chamber near the connecting pipe. When it passes the spiral blades, due to the guiding effect of the spiral blades, some of the gas rotates, causing water droplets in the gas to be thrown onto the inner wall of the processing chamber.

[0023] The beneficial effects of the gas-liquid separation system of the present invention are as follows: By using a central rod and an oscillating element, the central rod moves and changes the relative position of the oscillating element within the first and second flow chambers. The position of the first and second flow chambers, which are compressed and tightened by the oscillating element, changes. This change in the position of the oscillating element causes the first and second elastic heat exchange membranes to oscillate, resulting in the accumulation, mixing, and eventual fall of water and small ice crystals on the first and second elastic heat exchange membranes. This avoids the continuous large-area coverage of the heat exchange wall by water, which would reduce the heat exchange efficiency. Furthermore, it avoids the large-area condensation of water on the heat exchange walls of the first and second elastic heat exchange membranes, thereby greatly improving the heat exchange capacity of the heat exchange wall.

[0024] A vertical plate is provided in the middle of the second elastic heat exchange membrane, which divides the inner cavity of the processing chamber into two. The spiral blades are eccentrically arranged with respect to the central column. The circumferential surface of the spiral blades is closer to the side where the first connecting pipe is located in the processing chamber, so that the gas is minimally guided by the spiral blades when it flows near the second connecting pipe. Attached Figure Description

[0025] To more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings used in the description of the embodiments will be briefly introduced below. Obviously, the drawings described below are only some embodiments of the present invention. For those skilled in the art, other drawings can be obtained based on these drawings without creative effort. Wherein:

[0026] Figure 1 This is a schematic diagram of the overall structure of the present invention;

[0027] Figure 2 This is a schematic diagram of the cross-sectional structure of the present invention viewed from below;

[0028] Figure 3 This is a schematic diagram of the structure of the oscillating element of the present invention;

[0029] Figure 4 This is a schematic cross-sectional view of the separation tank of the present invention;

[0030] Figure 5 For the present invention Figure 1 A partially enlarged structural diagram of part A in the middle;

[0031] Figure 6 For the present invention Figure 1 A partially enlarged structural diagram of section B;

[0032] Figure 7 For the present invention Figure 1 A magnified schematic diagram of part C in the middle.

[0033] Reference numerals: 1. Separator; 2. Processing chamber; 3. Central column; 4. Spiral blade; 5. Connecting pipe one; 6. Connecting pipe two; 7. Sealing ring one; 8. Swing rod; 9. Flow chamber one; 10. Central rod; 11. Flow chamber two; 12. Connecting rod; 13. Rotary table; 14. Fan-shaped movable chamber; 15. Elastic connecting plate; 16. Outer ring; 17. Squeezing block; 18. Connecting block; 19. Rotating chamber one; 20. Rotating chamber two; 21. Sealing ring two; 22. Elastic heat exchange membrane one; 23. Motor; 24. Inlet pipe; 25. Outlet pipe; 26. Drain pipe; 27. Diverter seat; 28. Elastic heat exchange membrane two; 29. ​​Elastic connecting rope. Detailed Implementation

[0034] To make the above-mentioned objects, features and advantages of the present invention more apparent and understandable, the specific embodiments of the present invention will be described in detail below with reference to the accompanying drawings.

[0035] Many specific details are set forth in the following description in order to provide a full understanding of the invention. However, the invention may also be practiced in other ways different from those described herein, and those skilled in the art can make similar extensions without departing from the spirit of the invention. Therefore, the invention is not limited to the specific embodiments disclosed below.

[0036] Secondly, the term "one embodiment" or "embodiment" as used herein refers to a specific feature, structure, or characteristic that may be included in at least one implementation of the present invention. The phrase "in one embodiment" appearing in different places in this specification does not necessarily refer to the same embodiment, nor is it a single or selective embodiment that is mutually exclusive with other embodiments.

[0037] Secondly, the present invention is described in detail with reference to the schematic diagrams. When detailing the embodiments of the present invention, for ease of explanation, the cross-sectional views illustrating the device structure may be partially enlarged, not according to the usual scale. Furthermore, the schematic diagrams are merely examples and should not limit the scope of protection of the present invention. In addition, actual fabrication should include three-dimensional spatial dimensions of length, width, and depth.

[0038] like Figures 1-7 As shown, the present invention proposes a gas-liquid separation system, including a separation tank 1, a processing chamber 2 is provided on the inner side of the separation tank 1, a suspended cooling component is provided in the middle of the inner side of the processing chamber 2, a connecting pipe 5 is provided on one side of the top of the separation tank 1, and a connecting pipe 6 is provided on the other side of the top of the separation tank 1. The connecting pipe 5 is connected to the processing chamber 2, and the connecting pipe 6 is connected to the processing chamber 2.

[0039] Both connecting pipe 6 and connecting pipe 5 extend into the processing chamber 2. An elastic heat exchange membrane 22 is provided on the inner wall of the processing chamber 2. A flow chamber 11 is provided between the elastic heat exchange membrane 22 and the inner wall of the processing chamber 2. The connecting pipe 6 and connecting pipe 5 pass through the elastic heat exchange membrane 22 from both sides of the separation tank 1. The elastic heat exchange membrane 22 is connected to both connecting pipe 6 and connecting pipe 5.

[0040] The inner side of the flow cavity 21 is provided with a plurality of elastic connecting ropes 29, which are made of elastic material.

[0041] A rotating cavity 19 is recessed on the inner side of the top of the separation tank 1. The flow cavity 11 is connected to the rotating cavity 19. A sealing ring 7 is rotatably connected inside the rotating cavity 19. Several central rods 10 are provided on the sealing ring 7. The central rods 10 extend into the flow cavity 11. Several oscillating elements are provided on the central rods 10. The oscillating elements are in contact with the inner sides of the elastic heat exchange membrane 22 and the elastic heat exchange membrane 28.

[0042] The central rod 10 rotates at a small angle around the center of the processing chamber 2. During this time, the central rod 10, along with the oscillating element, moves and changes its relative position within the first flow chamber 9 and the second flow chamber 11. The positions of the first flow chamber 9 and the second flow chamber 11, which are compressed and tightened by the oscillating element, change. This change in the position of the oscillating element causes the first elastic heat exchange membrane 22 and the second elastic heat exchange membrane 28 to oscillate, causing the water and small ice crystals on the first elastic heat exchange membrane 22 and the second elastic heat exchange membrane 28 to accumulate, mix, and eventually fall off. This prevents the water from continuously covering the heat exchange wall over a large area, which would reduce the heat exchange efficiency. It also prevents the water from condensing and covering the heat exchange wall of the first elastic heat exchange membrane 22 and the second elastic heat exchange membrane 28 over a large area, thereby greatly improving the heat exchange capacity of the heat exchange wall. The side wall of the first elastic heat exchange membrane 22 and the second elastic heat exchange membrane 28 facing the inner cavity of the processing chamber 2 is the heat exchange wall.

[0043] The vibrating component includes an elastic connecting plate 15, an outer ring 16, and a compression block 17. Several outer rings 16 are sleeved on the central rod 10. Three compression blocks 17 are evenly arranged around the outer rings 16. Three elastic connecting plates 15 are connected between the inner side of the outer rings 16 and the central rod 10. The elastic connecting plates 15 are made of spring plates. Several connecting blocks 18 are evenly arranged in the rotating cavity 19. The material of the compression block 17 is rubber.

[0044] The elastic connecting plate 15 allows the outer ring 16 and the extrusion block 17 to rotate within a small range, and allows the outer ring 16 to undergo micro-movements and vibrations during its movement, thereby enhancing the adaptability of the oscillating element to the first flow cavity 9 and the second flow cavity 11, and enhancing the oscillating element's ability to act on the first elastic heat exchange membrane 22 and the second elastic heat exchange membrane 28.

[0045] The separation tank 1 has two symmetrically arranged fan-shaped movable cavities 14 recessed inside. The fan-shaped movable cavities 14 are connected to the rotating cavity 19. The inner side of the separation tank 1 is rotatably connected to a rotating platform 13. A swing rod 8 is connected between the rotating platform 13 and the sealing ring 7. The swing rod 8 is movably connected to the fan-shaped movable cavities 14.

[0046] The swing arm 8 can swing back and forth within the fan-shaped movable cavity 14.

[0047] The suspended cooling assembly includes a central column 3 and an elastic heat exchange membrane 28. The central column 3 is provided on the inner top wall of the processing chamber 2. The elastic heat exchange membrane 28 is provided on the outer side of the top of the central column 3. A flow chamber 9 is provided between the outer side of the central column 3 and the elastic heat exchange membrane 28. Several central rods 10 are provided in the flow chamber 9. An oscillating element is provided on the central rod 10.

[0048] The central rod 10 rotates at a certain angle within the second flow cavity 11 and the first flow cavity 9.

[0049] The top of the separation tank 1 has a recessed rotating cavity 20, which is connected to the flow cavity 9. A sealing ring 21 is rotatably connected inside the rotating cavity 20. A connecting block 18 is provided inside the rotating cavity 20. The swing rod 8 is connected to the sealing ring 21 through the connecting rod 12. A motor 23 is provided inside the separation tank 1. The power output end of the motor 23 is connected to the rotating table 13.

[0050] The motor 23 controls the swing arm 8 to rotate back and forth, causing the swing arm 8 and the structure connected to the swing arm 8 to rotate at a certain angle, with a maximum rotation angle of 8 to 16 degrees.

[0051] A diversion seat 27 is provided in the middle of the bottom wall of the processing chamber 2, and a drain pipe 26 is provided at the bottom of the separation tank 1. The drain pipe 26 is connected to the edge of the bottom wall of the processing chamber 2.

[0052] The diversion seat 27 causes the water to gather at the bottom edge of the treatment chamber 2. The drain pipe 26 is a T-shaped pipe with a one-way valve inside, which only allows water to be discharged.

[0053] The outer ring at the bottom of the central column 3 is provided with a spiral blade 4, the diameter of which is three-quarters of the inner diameter of the processing cavity 2.

[0054] The bottom of the separation tank 1 is provided with an inlet pipe 24 and an outlet pipe 25. The outlet pipe 25 is connected to the bottom of the second elastic heat exchange membrane 28. The first flow chamber 9 is connected to the outlet pipe 25, and the second flow chamber 11 is connected to the inlet pipe 24.

[0055] The gas first moves downward through the processing chamber 2 near the connecting pipe 5. When it passes the spiral blade 4, due to the guiding effect of the spiral blade 4, some of the gas rotates, causing water droplets in the gas to be thrown onto the inner wall of the processing chamber 2.

[0056] The beneficial effects of the gas-liquid separation system of the present invention are as follows: By using the central rod 10 and the oscillating element, the central rod 10 moves and changes the relative position of the oscillating element within the first flow chamber 9 and the second flow chamber 11. The position of the first flow chamber 9 and the second flow chamber 11, which are squeezed and tightened by the oscillating element, changes. The change in the position of the oscillating element causes the first elastic heat exchange membrane 22 and the second elastic heat exchange membrane 28 to oscillate, causing the water and small ice crystals on the first elastic heat exchange membrane 22 and the second elastic heat exchange membrane 28 to accumulate, mix, and eventually fall off. This avoids the continuous large-area coverage of the heat exchange wall by water, which would reduce the heat exchange efficiency. It also avoids the large-area condensation of water on the heat exchange wall of the first elastic heat exchange membrane 22 and the second elastic heat exchange membrane 28, thereby greatly improving the heat exchange capacity of the heat exchange wall.

[0057] A vertical plate is provided in the middle of the elastic heat exchange membrane 28, which divides the inner cavity of the processing chamber 2 into two. The spiral blade 4 is eccentrically positioned with respect to the central column 3. The circumferential surface of the spiral blade 4 is closer to the side where the connecting pipe 5 is located on the processing chamber 2, so that the gas is minimally guided by the spiral blade 4 when it flows near the connecting pipe 6.

[0058] The vertical plate is connected to the inner wall of the processing chamber 2.

[0059] The diameter of the oscillating element is greater than the inner cavity width of flow cavity 9 and flow cavity 11.

[0060] The materials of the elastic heat exchange membrane 1 22 and the elastic heat exchange membrane 28 are existing technologies, including liquid metal-silicone composite material. This is an advanced functional material that combines the ultra-high thermal conductivity of liquid metal with the flexibility of silicone, and has important application potential in the fields of medical heat therapy, flexible electronics, and soft robots.

[0061] The specific implementation method is as follows: the gas containing water vapor passes through the inner cavity of the processing chamber 2 through the connecting pipe 5, passes through the space between the elastic heat exchange membrane 28 and the elastic heat exchange membrane 22, and reaches the connecting pipe 6 for discharge. The liquid inlet pipe 24 introduces a low-temperature heat-absorbing medium and the liquid outlet pipe 25 discharges the heat-absorbing medium. The heat-absorbing medium circulates in the flow chamber 11 and the flow chamber 9, so that the gas is cooled, the water vapor in the gas is liquefied, and small water droplets are gathered into large water droplets. The water droplets flow to the bottom of the processing chamber 2 under the action of gravity and are discharged through the liquid outlet pipe 26.

[0062] The gas first moves downward through the side of the processing chamber 2 near the connecting pipe 5. When it passes the spiral blade 4, due to the guiding effect of the spiral blade 4, some of the gas rotates, causing water droplets to be thrown onto the inner wall of the processing chamber 2, which further separates the water and gas. Then, the gas passes through the side of the processing chamber 2 near the connecting pipe 6 and is again subjected to heat absorption by the elastic heat exchange membrane 28 and the elastic heat exchange membrane 22, which further cools the gas, liquefies the remaining water vapor again, and causes small water droplets to gather into large water droplets and detach from the gas. The gas that continues to rise is discharged through the connecting pipe 6.

[0063] It should be understood that numerous specific implementation decisions can be made during the development of any practical implementation, such as in any engineering or design project. Such development efforts may be complex and time-consuming, but for those skilled in the art who benefit from this disclosure, the development effort will be a routine work of design, manufacturing, and production without requiring much experimentation.

[0064] It should be noted that the above embodiments are only used to illustrate the technical solutions of the present invention and are not intended to limit it. Although the present invention has been described in detail with reference to preferred embodiments, those skilled in the art should understand that modifications or equivalent substitutions can be made to the technical solutions of the present invention without departing from the spirit and scope of the technical solutions of the present invention, and all such modifications or substitutions should be covered within the scope of the claims of the present invention.

Claims

1. A gas-liquid separation system, characterized in that: The system includes a separation tank (1), a processing chamber (2) is provided on the inner side of the separation tank (1), a suspended refrigeration component is provided in the middle of the inner side of the processing chamber (2), a connecting pipe (5) is provided on one side of the top of the separation tank (1), and a connecting pipe (6) is provided on the other side of the top of the separation tank (1). The connecting pipe (5) is connected to the processing chamber (2), and the connecting pipe (6) is connected to the processing chamber (2). Both connecting pipe 2 (6) and connecting pipe 1 (5) extend into the processing chamber (2). The inner wall of the processing chamber (2) is provided with an elastic heat exchange membrane 1 (22). A flow chamber 2 (11) is provided between the elastic heat exchange membrane 1 (22) and the inner wall of the processing chamber (2). The connecting pipe 2 (6) and connecting pipe 1 (5) pass through the elastic heat exchange membrane 1 (22) from both sides of the separation tank (1). The elastic heat exchange membrane 1 (22) is connected to both connecting pipe 2 (6) and connecting pipe 1 (5). The inner side of the top of the separation tank (1) is recessed with a rotating cavity one (19). The flow cavity two (11) is connected to the rotating cavity one (19). A sealing ring one (7) is rotatably connected in the rotating cavity one (19). Several central rods (10) are provided on the sealing ring one (7). The central rods (10) extend into the flow cavity two (11). Several oscillating elements are provided on the central rods (10). The oscillating elements are in contact with the inner sides of the elastic heat exchange membrane one (22) and the elastic heat exchange membrane two (28). The vibrating component includes an elastic connecting plate (15), an outer ring (16), and an extrusion block (17). Several outer rings (16) are sleeved on the central rod (10). Three extrusion blocks (17) are evenly arranged around the outer rings (16). Three elastic connecting plates (15) are connected between the inner side of the outer rings (16) and the central rod (10). The elastic connecting plates (15) are made of spring plates. Several connecting blocks (18) are evenly arranged in the first rotating cavity (19). The material of the extrusion block (17) is rubber. The separation tank (1) has two symmetrically arranged fan-shaped movable cavities (14) recessed inside. The fan-shaped movable cavities (14) are connected to the first rotating cavity (19). The inner side of the separation tank (1) is rotatably connected to a rotating platform (13). A swing rod (8) is connected between the rotating platform (13) and the first sealing ring (7). The swing rod (8) is movably connected to the fan-shaped movable cavity (14). The suspended cooling assembly includes a central column (3) and an elastic heat exchange membrane II (28). The central column (3) is provided on the inner top wall of the processing chamber (2). An elastic heat exchange membrane II (28) is provided on the outer side of the top of the central column (3). A flow chamber I (9) is provided between the outer side of the central column (3) and the elastic heat exchange membrane II (28). Several central rods (10) are provided in the flow chamber I (9). An oscillating element is provided on the central rods (10). The top of the separation tank (1) has a recessed rotating cavity (20), which is connected to the flow cavity (9). A sealing ring (21) is rotatably connected inside the rotating cavity (20). A connecting block (18) is provided inside the rotating cavity (20). The swing rod (8) is connected to the sealing ring (21) through the connecting rod (12). A motor (23) is provided inside the separation tank (1), and the power output end of the motor (23) is connected to the rotating table (13).

2. The gas-liquid separation system according to claim 1, characterized in that: The inner side of the second flow cavity (11) is provided with several elastic connecting ropes (29), which are made of elastic material.

3. The gas-liquid separation system according to claim 1, characterized in that: A diversion seat (27) is provided in the middle of the bottom wall of the processing chamber (2), and a drain pipe (26) is provided at the bottom of the separation tank (1). The drain pipe (26) is connected to the edge of the bottom wall of the processing chamber (2).

4. The gas-liquid separation system according to claim 3, characterized in that: The outer ring at the bottom of the central column (3) is provided with a spiral blade (4), the diameter of which is three-quarters of the inner diameter of the processing cavity (2).

5. The gas-liquid separation system according to claim 1, characterized in that: The bottom of the separation tank (1) is provided with an inlet pipe (24) and an outlet pipe (25). The outlet pipe (25) is connected to the bottom of the second elastic heat exchange membrane (28). The first flow chamber (9) is connected to the outlet pipe (25), and the second flow chamber (11) is connected to the inlet pipe (24).

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