Cyclone condensation separator

Abstract

The utility model relates to the technical field of cyclone separators, and discloses a cyclone condensation separator which comprises a separator shell, a cooling shell arranged at the top end of the separator shell, a pipeline I arranged inside the separator shell, a helical blade arranged on the surface of the pipeline I, a sleeve inserted into the top of the pipeline I, a pipeline II arranged outside the sleeve, and a spiral blade arranged on the surface of the pipeline II, the top end of the second pipeline penetrates through the cooling shell and is provided with a first flange plate, a spiral pipe for conveying refrigerants is arranged on the surface of the second pipeline, a medium outlet pipe is arranged at the medium outlet end of the spiral pipe, a medium inlet pipe is arranged at the medium inlet end of the spiral pipe, and a material receiving assembly is arranged at the bottom end of the inner wall of the separator shell. According to the gas-liquid separation device, the spiral pipe is arranged at the second pipeline, and a refrigerant is added into the spiral pipe through the medium inlet pipe and the medium outlet pipe, so that gas in the second pipeline is cooled, liquid in the gas is separated out through cooling and falls under the action of gravity, the gas-liquid separation effect in the gas can be improved, and the high-precision separation requirement can be met.

Description

Technical Field

[0001] The utility model relates to the technical field of cyclone separators, in particular to a cyclone condensation separator. Background Art

[0002] A cyclone separator is a device that uses the centrifugal force generated by rotational motion to separate solid particles from gas or liquid. Its operating principle is that when a gas or liquid stream containing solid particles enters the cyclone separator, the rotational motion caused by the tangential introduction causes the solid particles, which have a greater inertial centrifugal force, to be thrown toward the outer wall, thereby achieving separation from the gas or liquid.

[0003] Among them, the "cyclone separator" disclosed in the application number "201920719344.6" "comprises a container, the container comprises an upper cylinder and a lower cylinder; the upper cylinder is provided with an air inlet and an air outlet; the bottom of the lower cylinder is provided with a discharge port; it is characterized in that the cyclone separator is provided with a rotating shaft passing through the axis of the container, a scraper, and a connecting rod for fixing the scraper to the rotating shaft". In the utility model, when the cyclone separator is in operation, compared with the traditional cyclone separator, the residence time of the liquid material is significantly shortened, the color of the liquid material, the viscosity of the liquid material, and the content of dioxane in the liquid material are significantly reduced, and a good gas-liquid separation effect is achieved. Optimize the airflow distribution: a guide plate is provided at the air inlet of the cyclone separator so that the airflow can be evenly distributed when entering the separator, reducing the influence of uneven airflow distribution on the separation effect. At the same time, a plurality of swirl blades are provided inside the separator to guide the airflow to form a stable rotating flow field, thereby improving the separation efficiency.

[0004] However, the above method still has the following defects: although it can achieve gas-liquid separation, the gas-liquid separation effect is affected due to the different sizes of liquid particles in the gas or other factors, and cannot meet the requirements of high-precision separation. Utility Model Content

[0005] In view of the shortcomings of the existing technology, the present invention provides a cyclone condensation separator which has the advantages of facilitating efficient and high-precision separation of liquid from gas, improving the gas-liquid separation effect, and solving the problems raised by the above-mentioned background technology.

[0006] The utility model provides the following technical solution: a cyclone condensation separator, comprising a separator shell, a cooling shell being provided at the top of the separator shell, a pipe being provided inside the separator shell, a spiral blade being provided on the surface of the pipe being provided, a sleeve being inserted at the top of the pipe being provided, a pipe being provided outside the sleeve, the top of the pipe being passed through the cooling shell and being provided with a flange being provided, a spiral tube for conveying refrigerant being provided on the surface of the pipe being provided, a media outlet tube being provided at the media outlet end of the spiral tube, a media inlet tube being provided at the media inlet end of the spiral tube, a material receiving assembly being provided at the bottom end of the inner wall of the separator shell, and an air intake assembly being provided at the top of one side of the separator shell.

[0007] As an optimal technical solution of the present invention, a drain pipe is provided at the bottom of one side of the separator housing, a drain valve is provided on the surface of the drain pipe, a flange plate 2 is provided at the bottom of the separator housing, a mounting plate 1 is provided at the top of the separator housing, and a mounting plate 2 is provided at the bottom end of the cooling housing, and the mounting plate 1 and the mounting plate 2 are fixedly connected by a number of bolts and nuts.

[0008] As a preferred technical solution of the present invention, the edge of the spiral blade is fixedly connected to the inner wall of the separator shell, and a sealing ring is provided at the connection between the pipe 1 and the pipe 2.

[0009] As a preferred technical solution of the present invention, the inner wall of the pipe 1 is provided with a plurality of evenly spaced air guide plates, and the air guide plates are arranged at an angle.

[0010] As a preferred technical solution of the present invention, one end of the media outlet pipe passes through the cooling shell and is provided with a third flange, and one end of the media inlet pipe passes through the cooling shell and is provided with a fourth flange.

[0011] As an optimal technical solution of the present utility model, the material receiving assembly includes a material receiving hopper, which is fixedly installed at the bottom of the inner wall of the separator shell. A material discharge pipe is provided at the bottom end of the material receiving hopper, and mounting plates are provided on both sides of the material discharge pipe. A vibration motor is provided on the side of the mounting plate facing away from the material discharge pipe, and a material guide plate is provided at the bottom end of the inner wall of the separator shell.

[0012] As an optimal technical solution of the present invention, the air intake assembly includes an air inlet pipe, which is fixedly installed on the top of one side of the separator shell, and the gas inside the air inlet pipe enters the interior of the separator shell tangentially, and a sealing plate is provided at the connection between the air inlet pipe and the spiral blade.

[0013] As a preferred technical solution of the present invention, an air inlet pipe is provided at one end of the air inlet pipe away from the separator housing, and a fixing plate is provided at one end of the air inlet pipe away from the air inlet pipe, and a surface of the fixing plate is provided with a plurality of evenly spaced mounting holes.

[0014] Compared with the prior art, the present invention has the following beneficial effects:

[0015] 1. The cyclone condensation separator allows the gas to enter the interior of the separator shell through the provided air intake component. Under the centrifugal action of the spiral blades, the gas forms a cyclone inside the separator shell, and the liquid is separated from the gas under the action of centrifugal force. The receiving hopper in the receiving component can shrink the gas to the center due to its conical structure. When it reaches a certain position in the receiving hopper, the gas moves upward and enters the interior of pipe one and pipe two to flow out. Through the spiral tube provided at pipe two, and adding refrigerant to the interior through the media inlet pipe and the media outlet pipe, the gas in pipe two is cooled and cooled, and the liquid in the gas is precipitated after cooling and falls under the action of gravity, thereby improving the gas-liquid separation effect in the gas and meeting the high-precision separation requirements.

[0016] 2. The cyclone condensation separator can fully disperse the rising gas by arranging multiple air guide plates inside the first pipe, thereby facilitating the condensation of the gas at the second pipe and improving the gas-liquid separation effect.

[0017] 3. The cyclone condensation separator, by setting the separator shell to a cylindrical structure and arranging spiral blades with a long stroke inside, can guide the airflow to form a stable rotating flow field to improve the separation efficiency. BRIEF DESCRIPTION OF THE DRAWINGS

[0018] Figure 1 This is a schematic diagram of the three-dimensional structure of the utility model;

[0019] Figure 2 This is a schematic diagram of the explosion structure of the separator housing of the utility model;

[0020] Figure 3 This is a schematic diagram of the cross-sectional structure of the separator housing of the utility model;

[0021] Figure 4 This is a schematic diagram of the cross-sectional structure of a pipeline of the present invention;

[0022] Figure 5 For this utility model Figure 4 A in the figure shows the enlarged structural diagram;

[0023] Figure 6 For this utility model Figure 3 The enlarged structural diagram at B in FIG.

[0024] In the figure: 1. Separator housing; 2. Cooling housing; 3. Pipe 1; 4. Spiral blade; 5. Casing; 6. Pipe 2; 7. Spiral tube; 8. Media outlet pipe; 9. Media inlet pipe; 10. Air guide plate; 11. Material receiving assembly; 1101. Material receiving hopper; 1102. Material discharge pipe; 1103. Mounting plate; 1104. Vibration motor; 12. Drain pipe; 13. Air intake assembly; 1301. Air inlet pipe; 1302. Sealing plate; 1303. Air inlet pipe; 1304. Fixing plate; 14. Mounting plate 1; 15. Flange plate 2; 16. Flange plate 1; 17. Material guide plate. DETAILED DESCRIPTION

[0025] The following will be combined with the drawings in the embodiments of the present invention to clearly and completely describe the technical solutions in the embodiments of the present invention. Obviously, the embodiments described are only part of the embodiments of the present invention, not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without making creative efforts are within the scope of protection of the present invention.

[0026] See also Figure 1-6 The cyclone condensation separator includes a separator shell 1, a cooling shell 2 is provided at the top of the separator shell 1, a pipe 3 is provided inside the separator shell 1, so that the gas moves upward and enters the interior of the pipe 1 3 and the pipe 2 6 to flow out, and a spiral blade 4 is provided on the surface of the pipe 1 3. By increasing the conveying stroke of the spiral blade 4, the airflow can be guided to form a stable rotating flow field to improve the separation efficiency. A sleeve 5 is inserted at the top of the pipe 1 3, and a pipe 2 6 is provided on the outside of the sleeve 5. The top of the pipe 2 6 passes through the cooling shell 2 and is provided with a flange 16. A spiral tube 7 for conveying refrigerant is provided on the surface of the pipe 2 6, and a medium outlet pipe 8 is provided at the medium outlet end of the spiral tube 7, and a medium inlet pipe 9 is provided at the medium inlet end of the spiral tube 7. By setting a spiral tube 7 at the pipe 2 6 and adding refrigerant thereto through the medium inlet pipe 9 and the medium outlet pipe 8, the gas in the pipe 2 6 is cooled and the liquid in the gas is precipitated after cooling and falls under the action of gravity, thereby improving the gas-liquid separation effect in the gas and meeting the high-precision separation requirements. A material receiving assembly 11 is provided at the bottom end of the inner wall of the separator housing 1. The material receiving assembly 11 is provided to collect the liquid at the separation point and to vibrate and drop the solid particles in the gas to avoid clogging at the material receiving point, which affects the gas separation. An air inlet assembly 13 is provided at the top of one side of the separator housing 1 to facilitate the gas to enter the interior of the separator housing 1 tangentially.

[0027] The material receiving assembly 11 includes a receiving hopper 1101, which is fixedly mounted at the bottom of the inner wall of the separator housing 1. A discharge pipe 1102 is provided at the bottom end of the receiving hopper 1101. Both sides of the discharge pipe 1102 are provided with mounting plates 1103. A vibration motor 1104 is provided on the side of the mounting plate 1103 facing away from the discharge pipe 1102. A guide plate 17 is provided at the bottom end of the inner wall of the separator housing 1. A distance is left between the discharge pipe 1102 and the guide plate 17 to facilitate discharge. Through the receiving hopper 1101, the gas can be contracted to the center due to its conical structure. When it reaches a certain position in the receiving hopper 1101, the gas moves upward and enters the interior of pipe 1 3 and pipe 2 6 to flow out.

[0028] The inner wall of the pipe 1 3 is provided with a number of evenly spaced air guide plates 10, and the air guide plates 10 are arranged at an angle to facilitate the dispersion of the passing gas and improve the subsequent condensation effect;

[0029] A drain pipe 12 is provided at the bottom of one side of the separator housing 1, and a drain valve is provided on the surface of the drain pipe 12 to facilitate the discharge of the liquid. A flange 2 15 is provided at the bottom of the separator housing 1 to facilitate the installation of the separator housing 1 to a suitable position. A mounting plate 1 14 is provided at the top of the separator housing 1, and a mounting plate 2 is provided at the bottom end of the cooling housing 2. The mounting plate 1 14 and the mounting plate 2 are fixedly connected by a number of bolts and nuts. The mounting plate 1 14, the mounting plate 2, the bolts and the nuts, and the sealing strip therebetween facilitate the separation of the separator housing 1 and the cooling housing 2, facilitate the subsequent disassembly of the cooling housing 2, and facilitate subsequent maintenance.

[0030] The air intake assembly 13 includes an air intake pipe 1301, which is fixedly mounted on the top of one side of the separator housing 1. The gas inside the air intake pipe 1301 enters the interior of the separator housing 1 tangentially. A blocking plate 1302 is provided at the connection between the air intake pipe 1301 and the spiral blade 4 to facilitate the tangential entry of the gas into the interior of the separator housing 1 and facilitate the centrifugal operation of the gas in conjunction with the spiral blade 4.

[0031] An air inlet pipe 1303 is provided at one end of the air inlet pipe 1301 away from the separator housing 1, and a fixing plate 1304 is provided at one end of the air inlet pipe 1303 away from the air inlet pipe 1301. The surface of the fixing plate 1304 is provided with a plurality of evenly spaced mounting holes to facilitate gas delivery with the air supply equipment;

[0032] The edge of the spiral blade 4 is fixedly connected to the inner wall of the separator housing 1, which facilitates the fixing of the spiral blade 4 and also has a sealing effect. A sealing ring is provided at the connection between the pipe 1 3 and the pipe 2 6 to facilitate the sealing of the connection between the pipe 1 3 and the pipe 2 6.

[0033] One end of the outlet pipe 8 passes through the cooling shell 2 and is provided with a flange three, and one end of the inlet pipe 9 passes through the cooling shell 2 and is provided with a flange four, which facilitates the use of relevant pipelines and equipment for transporting refrigerant, so that the refrigerant enters the interior of the spiral tube 7 to condense and cool the gas inside the pipe 2 6.

[0034] When in use, it is preferred to place the cyclone condensation separator in a suitable position, fix it with the spiral nut group and flange 2 15, and then connect the fixed plate 1304 through the air supply equipment to prepare to transport gas to the inside of the air inlet pipe 1301, and then through flange 3 and flange 4, cooperate with relevant pipelines and equipment for transporting refrigerant, so that the refrigerant enters the inside of the spiral tube 7 to prepare for condensation and cooling of the gas inside the pipeline 2 6, and then transport the gas to the inside of the air inlet pipe 1301 through the air supply equipment, so that the gas enters the separator shell 1 tangentially, and the gas is centrifuged by the spiral blade 4, so that the gas forms a cyclone inside the separator shell 1, and the liquid is separated from the gas under the action of centrifugal force. At the same time, by increasing the transport stroke of the spiral blade 4, the airflow can be guided to form a stable rotating flow field, which can improve the efficiency of the process. High gas-liquid separation efficiency; the gas is transported to the receiving hopper 1101. Due to the conical structure of the receiving hopper 1101, the gas can be contracted to move closer to the center. When it reaches a certain position of the receiving hopper 1101, the gas moves upward and enters the interior of pipe 1 3 and pipe 2 6 to flow out. When the gas passes through the air guide plate 10 inside pipe 1 3, the gas is fully dispersed. When the gas passes through pipe 2 6, it passes through the spiral tube 7 provided on the outer wall of pipe 2 6 and refrigerant is added to the interior through the medium inlet pipe 9 and the medium outlet pipe 8, so that the gas in pipe 2 6 is cooled and the liquid in the gas is precipitated after cooling and falls under the action of gravity, thereby improving the gas-liquid separation effect in the gas and meeting the high-precision separation requirements. The liquid enters the bottom of the separator housing 1 through the discharge pipe 1102 and is discharged by cooperating with the drain pipe 12;

[0035] When the gas is transported to the interior of the separator housing 1, some fine solid impurities remain inside the gas. Under the action of centrifugation, they enter the bottom end of the inner wall of the separator housing 1. In order to prevent the discharge pipe 1102 from being blocked, the vibration motor 1104 can be controlled to vibrate it, so that the fine solid impurities fall to the bottom end of the inner wall of the separator housing 1 together with the liquid, and are vibrated and dropped, and finally discharged together with the liquid.

[0036] Although the embodiments of the present invention have been shown and described, it will be understood by those skilled in the art that various changes, modifications, substitutions and variations may be made to these embodiments without departing from the principles and spirit of the present invention, and the scope of the present invention is defined by the appended claims and their equivalents.

Claims

1. A cyclone condensation separator, comprising a separator housing (1), characterized in that: The top of the separator shell (1) is provided with a cooling shell (2), the interior of the separator shell (1) is provided with a pipe (3), the surface of the pipe (3) is provided with a spiral blade (4), the top of the pipe (3) is plugged with a sleeve (5), the outside of the sleeve (5) is provided with a pipe (6), the top of the pipe (6) passes through the cooling shell (2) and is provided with a flange (16), the surface of the pipe (6) is provided with a spiral tube (7) for conveying refrigerant, the outlet end of the spiral tube (7) is provided with a medium outlet tube (8), the inlet end of the spiral tube (7) is provided with a medium inlet tube (9), the bottom end of the inner wall of the separator shell (1) is provided with a material receiving assembly (11), and the top of one side of the separator shell (1) is provided with an air intake assembly (13).

2. The cyclone condensation separator according to claim 1, characterized in that: A drain pipe (12) is provided at the bottom of one side of the separator housing (1), a drain valve is provided on the surface of the drain pipe (12), a flange plate 2 (15) is provided at the bottom of the separator housing (1), a mounting plate 1 (14) is provided at the top of the separator housing (1), and a mounting plate 2 is provided at the bottom end of the cooling housing (2), and the mounting plate 1 (14) and the mounting plate 2 are fixedly connected by a plurality of bolts and nuts.

3. The cyclone condensation separator according to claim 1, characterized in that: The edge of the spiral blade (4) is fixedly connected to the inner wall of the separator shell (1), and a sealing ring is provided at the connection between the pipe 1 (3) and the pipe 2 (6).

4. The cyclone condensation separator according to claim 1, characterized in that: The inner wall of the pipe (3) is provided with a plurality of air guide plates (10) spaced evenly apart, and the air guide plates (10) are arranged at an angle.

5. The cyclone condensation separator according to claim 1, characterized in that: One end of the media outlet pipe (8) passes through the cooling shell (2) and is provided with a third flange, and one end of the media inlet pipe (9) passes through the cooling shell (2) and is provided with a fourth flange.

6. The cyclone condensation separator according to claim 1, characterized in that: The material receiving assembly (11) includes a material receiving hopper (1101), which is fixedly mounted on the bottom of the inner wall of the separator housing (1); a material discharge pipe (1102) is provided at the bottom end of the material receiving hopper (1101); mounting plates (1103) are provided on both sides of the material discharge pipe (1102); a vibration motor (1104) is provided on the side of the mounting plate (1103) facing away from the material discharge pipe (1102); and a material guide plate (17) is provided at the bottom end of the inner wall of the separator housing (1).

7. The cyclone condensation separator according to claim 1, characterized in that: The air intake assembly (13) includes an air intake pipe (1301), which is fixedly mounted on the top of one side of the separator housing (1), and the gas inside the air intake pipe (1301) enters the interior of the separator housing (1) tangentially, and a sealing plate (1302) is provided at the connection between the air intake pipe (1301) and the spiral blade (4).

8. The cyclone condensation separator according to claim 7, characterized in that: An air inlet pipe (1303) is provided at one end of the air inlet pipe (1301) that faces away from the separator housing (1), and a fixing plate (1304) is provided at one end of the air inlet pipe (1303) that faces away from the air inlet pipe (1301). The surface of the fixing plate (1304) is provided with a plurality of evenly spaced mounting holes.

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