Enhanced gas-liquid separator of energy-saving refrigerating system

Abstract

The invention discloses an energy-saving type refrigeration system reinforced gas-liquid separator, and relates to the related field of refrigeration systems, the energy-saving type refrigeration system reinforced gas-liquid separator comprises a shell, a sleeve is rotatably connected to the outer side of the middle of a gas outlet pipe, blades are arranged at the top of the outer side of the sleeve, a spiral separation plate is arranged on the inner wall of the middle of the shell, and a convergence plate is arranged at the bottom of the sleeve; a flow guide adjusting assembly is arranged outside the sleeve. According to the reinforced gas-liquid separator of the energy-saving refrigerating system, rotating flow is formed through the blades, a gas-liquid mixture is guided by the flow guide plate to flow in the specific direction, gas-liquid separation is smoother and more energy-saving, gas-liquid separation is conducted again through the spiral separation plate, and finally three-time separation is conducted through the convergence plate, so that the gas-liquid separation effect is improved, and meanwhile when the input flow becomes large, the gas-liquid separation efficiency is improved. The adjusting part adaptively disperses and guides the air flow, multiple times of contact is carried out between the separation parts, the separation effect is enhanced, it can be ensured that the gas-liquid mixture effectively makes contact with the separation parts when the flow speed is large, and the gas-liquid separation effect is kept.

Description

Technical Field

[0001] The present invention relates to the technical field of refrigeration systems, and specifically to an energy-saving refrigeration system enhanced gas-liquid separator. Background Art

[0002] With the continuous growth of global energy demand and the increasing awareness of environmental protection, the refrigeration industry is facing great pressure to reduce energy consumption and improve energy utilization efficiency. In many fields such as commercial buildings, industrial production, and cold chain logistics, refrigeration systems are widely used, and their energy consumption ratio cannot be ignored. As an important part of the refrigeration system, the performance of the gas-liquid separator directly affects the stability and energy efficiency of the refrigeration system. In the operation process of the traditional gas-liquid separator in the refrigeration system, the gas-liquid separation efficiency is relatively low, and the gaseous and liquid components in the refrigerant cannot be fully separated, resulting in some liquid refrigerant entering the compressor, causing the "liquid hammer" phenomenon, which will not only damage the compressor but also reduce the working efficiency of the compressor and increase energy consumption.

[0003] To solve the above defects, a prior art (Chinese patent with publication number CN116164454A and publication date May 26, 2023) discloses a gas-liquid separator and a refrigeration system. By providing at least one through hole on the side wall of the part of the input pipe extending into the container, the gas-liquid mixture can be discharged from the through hole and the outlet end of the input pipe simultaneously. The through hole shortens the flow distance of the gas-liquid mixture and increases the outlet for the gas-liquid mixture to flow out, thereby accelerating the discharge speed of the gas-liquid mixture, enabling the gas-liquid mixture to be quickly dispersed in the container and accelerating the gas-liquid separation rate.

[0004] A prior art (publication number CN116164449A, publication date May 26, 2023) discloses a gas-liquid separator and a refrigeration system. The container forms an air outlet interface and a liquid outlet interface through radial spinning. First, the input pipe and the functional components can be installed in the blank part of the container, and then the relative ends of the blank part of the container are respectively radially inwardly spun and contracted to form the air outlet interface and the liquid outlet interface. In this way, on the basis of the container being an integral structure, the assembly of functional components with relatively large radial dimensions and the container is realized, simplifying the structure of the container, the manufacturing process of the container, and reducing the assembly difficulty of the entire gas-liquid separator.

[0005] During the use of the above solution, the gas-liquid separation is accelerated by shortening the flow distance of the gas-liquid mixture for rapid sedimentation separation or by increasing the flow path of the gas-liquid mixture. However, when the gas-liquid mixture enters the separator, the gas flows vertically, contacts the separation components by its own flow, without a guiding direction, and the contact area is unstable, resulting in low processing efficiency. At the same time, when the input gas flow rate is large and the flow velocity is fast, the positions and states of the separation components inside the separator are fixed, making it easy to fail to comprehensively and effectively process the input gas-liquid mixture, resulting in liquid coal still being entrained in the separated gas in the later stage, thus causing a water hammer phenomenon and affecting the safety of use. Summary of the Invention

[0006] The purpose of the present invention is to provide an energy-saving refrigeration system enhanced gas-liquid separator to solve the problems in the existing refrigeration system enhanced gas-liquid separator mentioned in the above background technology. During the use process, when separating and processing the gas-liquid mixture, the effective contact area between the gas-liquid mixture and the separation components is limited, and the contact time is short, resulting in low gas-liquid separation efficiency. At the same time, when the input flow rate increases, the separation components are not easy to adjust adaptively to keep the input gas-liquid mixture in full contact with the separation components.

[0007] To achieve the above purpose, the present invention provides the following technical solution: An energy-saving refrigeration system enhanced gas-liquid separator, including a housing. The right top of the housing is connected with an air inlet pipe. The left side of the housing is provided with an air outlet pipe, and the air outlet pipe is set in an "L" shape. The top of the air outlet pipe is located inside the housing. An installation frame is sleeved outside the top of the air outlet pipe, and the installation frame is fixed on the inner wall of the housing. The bottom of the housing is provided with a liquid outlet pipe, and a wire mesh is arranged above the liquid outlet pipe. The middle outside of the air outlet pipe is rotatably connected with a sleeve, and blades are arranged on the outer top of the sleeve. A spiral separation plate is arranged on the middle inner wall of the housing. The bottom of the sleeve is connected with a converging plate through a truss. A flow guiding and adjusting component is arranged outside the sleeve, and the flow guiding and adjusting component includes movable plates hinged to the outside of the sleeve at equal angles and a regulating plate slidably connected to the bottom of the converging plate. The flow guiding and adjusting component adjusts and changes the air flow radius according to the size of the input air flow, so that the incoming air can still be in full contact with each layer of the circulation structure.

[0008] Furthermore, the blades are arranged opposite to the gas input part. The blades conduct preliminary diversion and separation of the gas-liquid mixture. The spiral separation plate is located below the blades and conducts secondary diversion and separation of the gas-liquid mixture. The converging plate conducts tertiary diversion and separation of the gas-liquid mixture, and the converging plate is located below the spiral separation plate.

[0009] Further, an air delivery ring is fixed to the bottom of the intake pipe. The air delivery ring is arranged at the inner top of the housing. The air delivery ring sleeves the outer side of the top of the air outlet pipe. The bottom of the air delivery ring is provided with air outlet openings at equal angles. The air outlet openings are arranged opposite to the blades. A net cover is installed at the top of the air outlet pipe.

[0010] Further, the blades are arranged in an arc structure. A streamline plate is fixedly installed on the side surface of the blades. The direction of the streamline plate enhances the guiding effect of the blades on the gas-liquid mixture, guiding the gas-liquid mixture to flow in a specific direction and avoiding air flow disorder.

[0011] Further, the flow guiding and adjusting assembly further includes grooves opened on the outer side of the bottom of the sleeve at equal angles. The grooves are slidably connected with sliders. The bottom of the sliders is fixedly connected with the bottom of the movable plate through first springs.

[0012] Further, a connecting rod is hinged to the outer side of the slider. The bottom of the connecting rod is hinged to the middle of the movable plate. The movable plate forms an extended rotation structure through the slider, the first spring and the connecting rod.

[0013] Further, a push plate is fixedly installed on the outer side of the movable plate. The push plate is slidably connected in the fixed cylinder in a sealed manner. The fixed cylinder is fixed to the outside of the sleeve. Both the push plate and the fixed cylinder are arranged in an arc structure.

[0014] Further, the inside of the fixed cylinder is communicated with the inside of the cylinder through a connecting pipe. The cylinders are installed at equal angles on the inner top of the inner cavity. The inner cavity is opened at the bottom of the converging plate. A sliding column is slidably connected in the cylinder. A regulating plate is fixed to the outer side of the sliding column.

[0015] Further, the directions of the cylinders and the sliding columns are consistent with the side direction of the converging plate. The regulating plate forms a telescopic sliding structure through the cylinders and the sliding columns. The regulating plate is arranged in a fan shape. The state of the regulating plate is adjusted following the movable plate. The state of the movable plate is adaptively adjusted according to the gas volume of the input gas-liquid mixture.

[0016] Further, a spiral groove is opened on the inner wall of the middle part of the housing. A spiral separation plate is rotatably connected in the spiral groove. The bottom of the spiral separation plate abuts against the outer top of the push plate. The push plate is slidably connected to the outer bottom of the sleeve through a second spring. The push plate is arranged in a "U" shape. The inner top of the push plate abuts against the lower part of the movable plate. A third spring is arranged on the upper inner wall of the housing. The bottom of the third spring abuts against the top of the spiral separation plate.

[0017] Compared with the prior art, the beneficial effects of the present invention are as follows: The energy-saving refrigeration system strengthens the gas-liquid separator. During use, it guides the gas-liquid mixture to flow in a specific direction, avoiding air flow disorder, making the gas-liquid separation smoother. And through the multi-layer separation structure, the gas and liquid are completely separated, avoiding the mutual entrainment and residue of the separated gas and liquid. The multi-layer circulation structure increases the contact area between the liquid film and the components, enabling the gas-liquid mixture to have more opportunities for gas-liquid separation in the separator, strengthening the mass transfer process between the gas and liquid, separating more liquid, thereby improving the separation efficiency, reducing the liquid droplets carried in the gas, and being beneficial to improving the performance and stability of the refrigeration system. At the same time, when the flow rate and flow volume of the input gas-liquid mixture are large, the adjustment mechanism can be adjusted according to the change of the air volume of the gas-liquid mixture. In the case of high wind speed, by expanding and changing the wind nest radius, the incoming air can still fully contact each layer of the circulation structure, and the gas and liquid can still be intensively separated through the adjustment components. The separator can maintain a good gas-liquid separation effect, avoiding the problem of insufficient gas-liquid separation caused by too high wind speed.

[0018] Further, after the gas-liquid mixture enters the separator, it forms a swirling flow through the rotation of the blades in cooperation with the streamline plate, enhancing the gas-liquid separation effect by using centrifugal force. And a spiral separation plate is arranged inside the separator to guide the gas-liquid mixture to flow in a specific direction, avoiding air flow disorder, making the gas-liquid separation smoother and more energy-saving. Finally, it is separated three times through the converging plate to improve the gas-liquid separation effect.

[0019] Further, when the input flow rate increases, the adjustment components adaptively disperse and guide the air flow, making multiple contacts between the separation components, strengthening the separation effect, so as to ensure that the gas-liquid mixture can effectively contact the separation components even when the flow rate is large, and maintain the gas-liquid separation effect.

[0020] Further, after the gas-liquid separation, when the liquid drips, it will also pass through the wire mesh. When the gas passes through the wire mesh, the liquid droplets are intercepted on the wire mesh, aggregated into larger liquid droplets and then fall, further improving the gas-liquid separation effect.

[0021] Further, through the lifting and rotation of the spiral separation plate, the gas-liquid separation efficiency can be increased, and the separated liquid can be rotated and dripped down to avoid remaining on the spiral separation plate. BRIEF DESCRIPTION OF THE DRAWINGS

[0022] Figure 1 is the overall front view structural schematic diagram of the present invention; Figure 2 is the front sectional top view structural schematic diagram of the housing of the present invention; Figure 3 is the separated structural schematic diagram of the housing and the internal structure of the present invention; Figure 4Schematic diagram of the separation structure of the blade, sleeve, spiral separation plate and collection plate of the present invention; Figure 5 Schematic diagram of the front sectional elevation structure of the gas transmission ring of the present invention; Figure 6 Schematic diagram of the structure of the sleeve, blade and streamline plate of the present invention; Figure 7 Schematic diagram of the top view of the connection of the sleeve, collection plate, movable plate and push rod of the present invention; Figure 8 Schematic diagram of the front sectional structure of the collection plate of the present invention; Figure 9 Schematic diagram of the top view of the distribution of the adjusting plate of the present invention; Figure 10 For the present invention Figure 8 Schematic diagram of a partial enlarged structure at one place; Figure 11 For the present invention Figure 8 Schematic diagram of another partial enlarged structure.

[0023] In the figure: 1. housing; 2. intake pipe; 3. outlet pipe; 4. liquid outlet pipe; 5. mounting bracket; 6. mesh cover; 7. wire mesh; 8. gas transmission ring; 9. gas outlet; 10. sleeve; 11. blade; 12. streamline plate; 13. spiral separation plate; 14. truss; 15. collection plate; 16. movable plate; 17. groove; 18. slider; 19. first spring; 20. connecting rod; 21. push plate; 22. fixed cylinder; 23. cylinder; 24. inner cavity; 25. sliding column; 26. adjusting plate; 27. connecting pipe; 28. spiral groove; 29. push rod; 30. second spring; 31. third spring. Specific embodiments

[0024] Next, the technical solutions in the embodiments of the present invention will be clearly and completely described in conjunction with the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, rather than all the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.

[0025] Embodiment 1: Please refer to Figures 1 - 11, the present invention provides the following technical solution: An energy-saving refrigeration system enhanced gas-liquid separator, including a housing 1, an air inlet pipe 2 is connected to the top right of the housing 1, an air outlet pipe 3 is arranged on the left side of the housing 1, the air outlet pipe 3 is arranged in an "L" shape, the top of the air outlet pipe 3 is located inside the housing 1, an installation frame 5 is sleeved outside the top of the air outlet pipe 3, the installation frame 5 is fixed on the inner wall of the housing 1, a liquid outlet pipe 4 is arranged at the bottom of the housing 1, a wire mesh 7 is arranged above the liquid outlet pipe 4, the middle part of the air outlet pipe 3 is rotatably connected with a sleeve 10, a blade 11 is arranged at the top outside the sleeve 10, a spiral separation plate 13 is arranged on the middle inner wall of the housing 1, the bottom of the sleeve 10 is connected with a converging plate 15 through a truss 14, a flow guiding and adjusting component is arranged outside the sleeve 10, and the flow guiding and adjusting component includes a movable plate 16 hinged to the outside of the sleeve 10 at equal angles and an adjusting plate 26 slidably connected to the bottom of the converging plate 15. The flow guiding and adjusting component adjusts and changes the airflow radius according to the input airflow size, so that the incoming air can still fully contact each layer of the circulation structure.

[0026] During use, the gas-liquid mixture enters the device from the air inlet pipe 2 on the housing 1. After passing through multiple separations inside the device, the gas is discharged from the air outlet pipe 3, and the liquid is discharged from the liquid outlet pipe 4 at the bottom. The sleeve 10 sleeved outside the air outlet pipe 3 is in the gas-liquid mixture. By blowing the blade 11, the blade 11 rotates, and then drives the sleeve 10 to rotate synchronously, so that the gas-liquid mixture forms a spiral airflow and is conveyed downward. After the gas-liquid mixture contacts the blade 11, the gas and liquid can be preliminarily separated. Then the gas-liquid mixture contacts the spiral separation plate 13, and the spiral separation plate 13 can increase the contact area and time between the gas-liquid mixture and it, thereby further improving the gas-liquid separation effect. Finally, the gas and liquid are separated three times through the converging plate 15. The liquid stays in contact with the inner wall of the converging plate 15, and the gas continues to flow, so as to achieve a better separation effect. The wire mesh 7 separates the gas-liquid mixture for the last time. At the same time, when the flow rate of the input gas-liquid mixture is large, the movable plate 16 unfolds due to centrifugal force, and then expands the airflow radius of the gas flowing downward, so that the flowing gas-liquid mixture can make multiple contacts between the separation components and be fully separated. The adjusting plate 26 synchronously adjusts the extending length, thereby increasing the contact area and strengthening the gas-liquid separation effect, avoiding the problem of insufficient separation due to fast flow rate.

[0027] Embodiment 2: On the basis of Embodiment 1, an air delivery ring 8 and a streamline plate 12 are also disclosed. Please refer to Figures 2 - 7As shown in the figure, its specific structure is as follows: The blade 11 is arranged opposite to the gas input part. The blade 11 preliminarily guides and separates the gas-liquid mixture. The spiral separation plate 13 is located below the blade 11 and conducts secondary guiding and separation of the gas-liquid mixture. The converging plate 15 conducts tertiary guiding and separation of the gas-liquid mixture. The converging plate 15 is located below the spiral separation plate 13. A gas transmission ring 8 is fixed at the bottom of the air inlet pipe 2. The gas transmission ring 8 is arranged at the inner top of the housing 1. The gas transmission ring 8 is sleeved on the outer side of the top of the air outlet pipe 3. The bottom of the gas transmission ring 8 is provided with air outlet openings 9 at equal angles. The air outlet openings 9 are arranged opposite to the blade 11. A net cover 6 is installed at the top of the air outlet pipe 3. The blade 11 is arranged in an arc structure. A streamline plate 12 is fixedly installed on the side surface of the blade 11. The trend of the streamline plate 12 enhances the guiding effect of the blade 11 on the gas-liquid mixture, guiding the gas-liquid mixture to flow in a specific direction and avoiding air flow disorder.

[0028] During use, after the gas-liquid mixture is input from the air inlet pipe 2, the gas transmission ring 8 evenly disperses the input gas-liquid mixture. The gas transmission ring 8 blows out the gas-liquid mixture through the air outlet openings 9. The gas-liquid mixture blows the blade 11. The streamline plate 12 on the blade 11 can enhance the guiding effect on the air flow, making the gas-liquid mixture rotate downward in a spiral shape. Then it passes through the spiral separation plate 13. The structure of the spiral separation plate 13 enables the gas-liquid mixture to pass through the spiral layers layer by layer in sequence, so that the liquid in the gas-liquid mixture remains on the spiral separation plate 13 and the gas continues to flow. When passing through the converging plate 15, the setting of the converging plate 15 causes the gas-liquid mixture to contact the side wall of the converging plate 15, thereby conducting tertiary separation of the gas-liquid mixture, strengthening the separation effect of the gas-liquid mixture and making the separation more thorough. Before the gas is discharged, the net cover 6 at the top of the air outlet pipe 3 can intercept trace amounts of liquid, so that the gas is separated more cleanly.

[0029] Embodiment 3: On the basis of Embodiment 2, a slider 18, a first spring 19 and a connecting rod 20 are also disclosed. Please refer to Figures 3 - 4 and Figures 7 - 11 As shown in the figure, its specific structure is as follows: The flow guiding and adjusting assembly further includes grooves 17 opened at equal angles on the outer side of the bottom of the sleeve 10. The grooves 17 are slidably connected with a slider 18. The bottom of the slider 18 is fixedly connected with the bottom of the movable plate 16 through a first spring 19. A connecting rod 20 is hinged on the outer side of the slider 18. The bottom of the connecting rod 20 is hinged to the middle of the movable plate 16. The movable plate 16 constitutes an extended rotation structure through the slider 18, the first spring 19 and the connecting rod 20.

[0030] During use, when the input gas flow rate is large and the flow velocity is fast, the rotation speed of the blade 11 driving the sleeve 10 will also increase. After the sleeve 10 rotates centrifugally, the movable plate 16 rotates outward due to centrifugal force and expands. When the movable plate 16 rotates, the slider 18 will slide downward in the groove 17, thereby compressing the first spring 19. After the movable plate 16 expands, the radius of the rotating air flow will be enlarged, thereby forcing the rapidly flowing gas-liquid mixture to flow layer by layer in the spiral separation plate 13, so as to maintain the separation effect on the gas-liquid mixture.

[0031] Furthermore, a push plate 21, a fixed cylinder 22, a cylinder 23 and a sliding column 25 are also disclosed. Please refer to Figures 3 - 4 and Figures 7 - 11 As shown, a push plate 21 is fixedly installed on the outer side of the movable plate 16. The push plate 21 is hermetically slidably connected in the fixed cylinder 22. The fixed cylinder 22 is fixed to the outside of the sleeve 10. Both the push plate 21 and the fixed cylinder 22 are provided with arc-shaped structures. The inside of the fixed cylinder 22 is connected to the inside of the cylinder 23 through a connecting pipe 27. The cylinder 23 is installed at equal angles on the inner side top of the inner cavity 24. The inner cavity 24 is opened at the bottom of the converging plate 15. A sliding column 25 is slidably connected in the cylinder 23. An adjusting plate 26 is fixed to the outer side of the sliding column 25. The directions of the cylinder 23 and the sliding column 25 are the same as the side direction of the converging plate 15. The adjusting plate 26 forms a telescopic sliding structure through the cylinder 23 and the sliding column 25. The adjusting plate 26 is provided with a fan-shaped structure. The state of the adjusting plate 26 is adjusted following the movable plate 16. The state of the movable plate 16 is adaptively adjusted according to the gas volume of the input gas-liquid mixture.

[0032] During use, when the movable plate 16 expands, it will synchronously drive the push plate 21 to slide in the fixed cylinder 22, thereby sending the gas in the fixed cylinder 22 to the cylinder 23 through the connecting pipe 27. The sliding column 25 in the cylinder 23 is pushed out. After the sliding column 25 is pushed out, it drives the adjusting plate 26 to extend out of the inner cavity 24 of the converging plate 15, thereby changing the passing area at the bottom of the converging plate 15 and increasing the contact area on the side, so that the gas-liquid mixture can be separated even at high flow rates, thereby improving the practicability of the gas-liquid separator.

[0033] Embodiment 4: On the basis of Embodiment 3, it is also disclosed. Please refer to the figure shown. The specific structure is as follows: A spiral groove 28 is opened on the inner wall of the middle part of the housing 1. A spiral separation plate 13 is rotatably connected in the spiral groove 28. The bottom of the spiral separation plate 13 abuts against the outer top of the push rod 29. The push rod 29 is slidably connected to the outer bottom of the sleeve 10 through a second spring 30. The push rod 29 is provided with a "U" - shaped structure. The inner top of the push rod 29 abuts against the lower part of the movable plate 16. A third spring 31 is provided on the upper inner wall of the housing 1. The bottom of the third spring 31 abuts against the top of the spiral separation plate 13.

[0034] During use, when the sleeve 10 rotates at a high speed, the movable plate 16 expands centrifugally, squeezing the push rod 29 below, thereby compressing the second spring 30. After the push rod 29 moves downward, the third spring 31 drives the spiral separation plate 13 to move downward. Also, due to the arrangement of the spiral groove 28, the spiral separation plate 13 can rotate while moving vertically, so that the gas-liquid contact can be more uniform and comprehensive. When the input air flow is small, the movable plate 16 retracts and resets, and the second spring 30 pushes the push rod 29 to reset and move upward. The spiral separation plate 13 is pushed to rotate and move upward, thereby compressing the third spring 31. And during the process of the spiral separation plate 13 rotating and moving upward, the liquid separated by itself can be gathered and dripped down to avoid residue.

[0035] The content not described in detail in this specification belongs to the prior art well-known to those skilled in the art.

[0036] Although the present invention has been described in detail with reference to the foregoing embodiments, those skilled in the art can still modify the technical solutions described in the foregoing embodiments, or perform equivalent replacements for some of the technical features. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principle of the present invention shall be included within the protection scope of the present invention.

Claims

1. An energy-saving refrigeration system enhanced gas-liquid separator, comprising a shell (1), an air inlet pipe (2) being connected to the top of the right side of the shell (1), an air outlet pipe (3) being arranged on the left side of the shell (1), the air outlet pipe (3) being arranged in an "L"-shaped structure, the top of the air outlet pipe (3) being located inside the shell (1), a mounting frame (5) being sleeved on the outer side of the top of the air outlet pipe (3), the mounting frame (5) being fixed on the inner wall of the shell (1), a liquid outlet pipe (4) being arranged at the bottom of the shell (1), and a wire mesh (7) being arranged above the liquid outlet pipe (4); Features: A sleeve (10) is rotatably connected to the outer side of the middle of the air outlet pipe (3), a blade (11) is provided on the outer top of the sleeve (10), a spiral separation plate (13) is provided on the inner wall of the middle of the shell (1), and the bottom of the sleeve (10) is connected to a converging plate (15) via a truss (14); The sleeve (10) is provided with a flow guide adjustment component on the outside, and the flow guide adjustment component comprises a movable plate (16) hinged at an equal angle to the outside of the sleeve (10) and an adjustment plate (26) slidably connected to the bottom of the converging plate (15). The flow guide adjustment component adjusts the airflow radius according to the size of the input airflow, so that the incoming air can still fully contact each layer of the circulation structure.

2. The energy-saving refrigeration system enhanced gas-liquid separator according to claim 1, characterized in that: The blade (11) is arranged opposite to the gas input portion, the blade (11) performs preliminary diversion and separation on the gas-liquid mixture, the spiral separation plate (13) is located below the blade (11) and performs secondary diversion and separation on the gas-liquid mixture, the convergence plate (15) performs tertiary diversion and separation on the gas-liquid mixture, and the convergence plate (15) is located below the spiral separation plate (13).

3. The energy-saving refrigeration system enhanced gas-liquid separator according to claim 1, characterized in that: An air delivery ring (8) is fixed to the bottom of the air inlet pipe (2), the air delivery ring (8) is arranged on the inner top of the shell (1), the air delivery ring (8) is sleeved on the outer top of the air outlet pipe (3), the bottom of the air delivery ring (8) is provided with air outlets (9) at equal angles, the air outlets (9) are arranged opposite to the blades (11), and a mesh cover (6) is installed on the top of the air outlet pipe (3).

4. The energy-saving refrigeration system enhanced gas-liquid separator according to claim 1, characterized in that: The blade (11) is configured as an arc-shaped structure, and a streamline plate (12) is fixedly mounted on the side of the blade (11), wherein the direction of the streamline plate (12) increases the guiding effect of the blade (11) on the gas-liquid mixture, guiding the gas-liquid mixture to flow in a specific direction, thereby avoiding airflow turbulence.

5. The energy-saving refrigeration system enhanced gas-liquid separator according to claim 1, characterized in that: The flow guide adjustment assembly further comprises a groove (17) formed at an equal angle on the outside of the bottom of the sleeve (10), the groove (17) being slidably connected to a slider (18), the bottom of the slider (18) being fixedly connected to the bottom of the movable plate (16) via a first spring (19).

6. The energy-saving refrigeration system enhanced gas-liquid separator according to claim 5, characterized in that: A connecting rod (20) is hingedly connected to the outer side of the slider (18), the bottom of the connecting rod (20) is hingedly connected to the middle of the movable plate (16), and the movable plate (16) forms an extended rotation structure through the slider (18), the first spring (19) and the connecting rod (20).

7. The energy-saving refrigeration system enhanced gas-liquid separator according to claim 6, characterized in that: A push plate (21) is fixedly mounted on the outer side of the movable plate (16). The push plate (21) is sealingly slidably connected to a fixed cylinder (22). The fixed cylinder (22) is fixed to the outside of the sleeve (10). Both the push plate (21) and the fixed cylinder (22) are configured as arc structures.

8. The energy-saving refrigeration system enhanced gas-liquid separator according to claim 7, characterized in that: The interior of the fixed cylinder (22) is connected to the interior of the cylinder (23) via a connecting pipe (27). The cylinder (23) is mounted at an equal angle on the inner top of the inner cavity (24). The inner cavity (24) is opened at the bottom of the converging plate (15). A sliding column (25) is slidably connected in the cylinder (23). An adjusting plate (26) is fixed to the outer side of the sliding column (25).

9. The energy-saving refrigeration system enhanced gas-liquid separator according to claim 8, characterized in that: The directions of the cylinder (23) and the sliding column (25) are consistent with the direction of the side of the converging plate (15); the adjusting plate (26) forms a telescopic sliding structure through the cylinder (23) and the sliding column (25); the adjusting plate (26) is arranged as a fan-shaped structure; the state of the adjusting plate (26) is adjusted following the movable plate (16); the state of the movable plate (16) is adaptively adjusted according to the gas volume of the input gas-liquid mixture.

10. The energy-saving refrigeration system enhanced gas-liquid separator according to claim 1, characterized in that: A spiral groove (28) is provided on the inner wall of the middle part of the shell (1), and a spiral separation plate (13) is rotatably connected in the spiral groove (28). The bottom of the spiral separation plate (13) abuts against the outer top of a push rod (29). The push rod (29) is slidably connected to the outer bottom of the sleeve (10) via a second spring (30). The push rod (29) is arranged in a "U"-shaped structure. The inner top of the push rod (29) abuts against the bottom of the movable plate (16). A third spring (31) is provided on the upper inner wall of the shell (1), and the bottom of the third spring (31) abuts against the top of the spiral separation plate (13).

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