Efficient separator

Abstract

The utility model discloses an efficient separator which comprises a support, a shell and a driving mechanism are arranged on the support, an air outlet, a liquid return opening, an air inlet, a liquid outlet and a plurality of liquid inlets are formed in the shell, the air outlet, the liquid return opening, the air inlet, the liquid outlet and the liquid inlets are all communicated with the interior of the shell, and a plurality of sets of separation assemblies are arranged in the shell. The multiple sets of separation assemblies are evenly distributed in the vertical direction of the shell, each separation assembly comprises a fixed disc connected with the shell and a rotating disc connected with the driving mechanism, and a penetrating through hole allowing liquid to flow to the center of the rotating disc is formed in the center of each fixed disc. A plurality of groups of concentric lower annular plates with different diameters are arranged on the rotating disc, a plurality of holes are distributed in the circumference of each lower annular plate, a plurality of upper annular plates which are adjacent to the lower annular plates and are equidistant in the radial direction extend vertically and downwards from the lower end surface of the fixed disc, and the upper annular plates and the lower annular plates jointly form a channel for air and liquid to flow. The separation efficiency is high, the equipment size is small, the energy consumption is low, and the solvent is directly separated and purified by combining with other equipment such as a reaction kettle and an evaporation kettle in a production workshop, so that the technological process is optimized, the energy consumption is reduced, the cost is saved, and the operation is convenient.

Description

Technical Field

[0001] The utility model relates to a high-efficiency separator. Background Art

[0002] A distillation tower is a tower-type gas-liquid contact device for distillation, including a plate-type distillation tower and a packed distillation tower. It utilizes the different volatilities of the components in the mixture, that is, the different vapor pressures of the components at the same temperature. The light components (low boiling substances) in the liquid phase are transferred to the gas phase, and the heavy components (high boiling substances) in the gas phase are transferred to the liquid phase, thereby achieving the purpose of separation. For example, the patent application number is CN202022547575.9, and the name is a packed distillation tower; another example is the patent application number CN202222898525.4, and the name is a plate-type distillation tower in an air separation device. Distillation tower, with the development of the chemical industry, packed distillation tower and plate distillation tower rely on gravity to make the liquid fall naturally to complete mass transfer and reaction, which takes a long time. Compared with traditional distillation towers, the high-efficiency separator of this application adopts the principle of centrifugal force. The specific surface area generated by the divided liquid is much larger than that of the packed tower, which completes the mass transfer and chemical reaction process more efficiently; it occupies a smaller space but can achieve the same or better effect and rate as the packed tower, which can not only achieve the purpose efficiently but also save costs; in terms of medium selection, compared with other separators, the ultra-gravity separator can separate high-viscosity liquids and azeotropic solutions. Utility Model Content

[0003] In view of the deficiencies in the prior art, the purpose of the utility model is to provide a high-efficiency separator that can solve the problems of low efficiency and single function of traditional distillation towers.

[0004] To achieve the above-mentioned purpose, the utility model provides the following technical scheme: a high-efficiency separator, comprising a bracket, a shell and a driving mechanism are arranged on the bracket, the shell is provided with an air outlet, a liquid return port, an air inlet, a liquid outlet and a plurality of liquid inlets, and the air outlet, the liquid return port, the air inlet, the liquid outlet and the plurality of liquid inlets are all connected with the inside of the shell, a plurality of groups of separation components are arranged in the shell, and the plurality of separation components are evenly distributed along the vertical direction of the shell, the separation components include a fixed disk connected to the shell and a rotating disk connected to the driving mechanism, a through hole is arranged in the center of the fixed disk for liquid to flow to the center of the rotating disk, a plurality of groups of lower annular plates with concentric centers and different diameters are arranged on the rotating disk, and a plurality of holes are distributed on the circumference of the lower annular plate, an upper annular plate is vertically extended downward from the lower end face of the fixed disk to be radially equidistant from the adjacent lower annular plate, and the upper annular plate and the lower annular plate together form a channel for gas and liquid circulation.

[0005] Furthermore, the shell includes a bottom shell, a top shell and a plurality of intermediate shells, and the bottom shell, the top shell and the plurality of intermediate shells are fixedly connected by bolts.

[0006] Furthermore, the lower end sides of the plurality of intermediate shells are symmetrically provided with notches, the notches are connected to the interior of the shell, and the notches are provided with adjusting members for adjusting the vertical position of the fixed disk, thereby adjusting the spacing between the upper annular plate and the lower annular plate.

[0007] Furthermore, a baffle is extended to the fixed plate corresponding to the notch position, and an inner sealing layer is provided on the end face of the baffle that fits the inside of the intermediate shell. A transverse plate is provided toward the notch position of the baffle, and the transverse plate is fixedly connected with a fixed plate, and an outer sealing layer is provided on the end face of the fixed plate that fits toward the outer wall of the intermediate shell.

[0008] Furthermore, the adjusting member includes a boss extending laterally from the side wall of the intermediate shell, the boss is movably connected with a screw rod, the screw rod is threadedly connected to the fixing plate, and the fixing plate is driven to move vertically by rotating the screw rod, thereby driving the fixing disk to move up and down.

[0009] Furthermore, the air outlet and the liquid return port are distributed on the top shell, the air inlet is distributed on the side of the bottom shell, the liquid outlet is distributed on the bottom of the bottom shell, and the liquid inlet is distributed on the side of the middle shell.

[0010] Beneficial effects:

[0011] 1. Compared with the traditional distillation tower, the high-efficiency separator in this application has high separation efficiency, small equipment size and low energy consumption. It can be combined with other equipment such as reactors and evaporators in the production workshop to directly separate and purify the solvent, thereby optimizing the process flow, reducing energy consumption, saving costs and facilitating operation.

[0012] 2. The present application sets up multiple sets of separation components and the separation components include fixed plates and moving plates. The high-speed rotation in the equipment generates the gravitational acceleration of the separated and distilled liquid, and the rotational acceleration of the mechanical force greatly increases the kinetic energy of the liquid itself, resulting in an increase in the mass transfer capacity during the mass transfer process, thereby improving the efficiency and results of the mass transfer.

[0013] 3. The present application also provides an adjusting member, which is used to adjust the distance between the fixed disk and the rotating disk. For solvents with higher viscosity, the adjusting member can be used to increase the distance between the fixed disk and the rotating disk to reduce fluid resistance and improve mass transfer efficiency. For solvents with lower viscosity, the adjusting member can be used to appropriately reduce the distance to increase the gas-liquid contact area and mass transfer surface area. The distance between the fixed disk and the rotating disk can be adjusted according to the physical properties of the solvent itself to obtain better mass transfer efficiency. BRIEF DESCRIPTION OF THE DRAWINGS

[0014] Figure 1 This is a schematic diagram of a separator according to Embodiment 1;

[0015] Figure 2This is a schematic diagram of a separator according to Embodiment 2.

[0016] 1. Bracket; 2. Shell; 21. Bottom shell; 22. Top shell; 23. Intermediate shell; 3. Driving mechanism; 31. Main shaft; 32. Motor; 33. Pulley; 4. Air outlet; 5. Liquid return port; 6. Air inlet; 7. Liquid outlet; 8. Liquid inlet; 9. Separation component; 91. Fixed plate; 911. Through hole; 912. Upper annular plate; 92. Rotating plate; 921. Lower annular plate; 922. Hole; 10. Step surface; 11. Fastener; 12. Notch; 13. Adjusting member; 131. Boss; 132. Screw rod; 14. Baffle; 15. Inner sealing layer; 16. Transverse plate; 17. Fixed plate; 18. Outer sealing layer. DETAILED DESCRIPTION

[0017] In order to further explain the technical means and effects adopted by the present invention to achieve the predetermined purpose of the utility model, the specific implementation method, structure, characteristics and effects of the present invention are described in detail below in combination with the accompanying drawings and preferred embodiments.

[0018] Refer to Figure 1As shown, the first embodiment of the present utility model is a high-efficiency separator, including a bracket 1, a shell 2 and a driving mechanism 3 are arranged on the bracket 1, the driving mechanism 3 includes a main shaft 31 and a motor 32, one end of the main shaft 31 passes through the shell 2 and is connected to the top of the shell 2 through a bearing, and the other end passes through the bottom of the shell 2 and is connected to a pulley 33, and the pulley 33 is connected to the motor 32 through a belt, the shell 2 includes a bottom shell 21, a top shell 22 and a plurality of intermediate shells 23, the bottom shell 21, the top shell 22 and the plurality of intermediate shells 23 are all fixedly connected by bolts, an air outlet 4 and a liquid return port 5 are arranged on the upper end of the top shell 22, and a liquid inlet 8 is arranged on the side wall of the middle shell, the bottom shell 21 is provided with a liquid outlet 7 and an air inlet 6, the air inlet 6 is arranged on the side wall of the bottom shell 21, and the liquid outlet 7 is arranged at the bottom of the bottom shell 21, the air outlet 4, the liquid return port 5, the liquid inlet 8, the liquid outlet 7 and the air inlet 6 are all connected inside the shell 2, and the shell 2 is provided with a liquid outlet 4, a liquid return port 5, a liquid inlet 8, a liquid outlet 7 and a gas inlet 6. A plurality of separation components 9 are provided, and the plurality of separation components 9 are evenly distributed along the vertical direction of the shell 2. The separation components 9 include a fixed disk 91 connected to the shell 2 and a rotating disk 92 connected to the main shaft 31. The inner walls of the upper ends of the bottom shell 21 and the intermediate casing 23 are provided with a step surface 10. The lower end of the fixed disk 91 is in contact with the step surface 10 and is fixedly connected by a fastener 11. A through hole 911 is provided in the center of the fixed disk 91 for liquid to flow to the center of the rotating disk 92. The rotating disk 92 is provided with a plurality of lower annular plates 921 with different concentric centers, and a plurality of holes 922 are distributed on the circumference of the lower annular plate 921. The holes 922 are used to more evenly throw away the material when the inner ring of the rotating disk 92 collides with the material liquid. An upper annular plate 912 is vertically extended downward from the lower end surface of the fixed disk 91, and the upper annular plate 912 and the lower annular plate 921 are radially equidistant from the adjacent lower annular plate 921. The upper annular plate 912 and the lower annular plate 921 together form a channel for gas and liquid circulation. When working, continuous gas enters the shell 2 from the air inlet 6, and under the action of the pressure difference, the channel formed by the upper annular plate 912 and the lower annular plate 921 flows in a zigzag manner from the outside to the center, and then enters the upper separation component 9 through the through hole 911 on the fixed disk 91 until it finally leaves from the air outlet 4; the raw material enters from the liquid inlet 8, and the material evaporated from the air outlet 4 enters from the liquid return port 5, and the evaporated material or raw material enters the shell 2 and enters the center of the corresponding rotating disk 92 through the through hole 911 on the fixed disk 91. The material or raw material is repeatedly thrown to the upper annular plate 912 by the high-speed rotating lower annular plate 921 of the main shaft 31 connected to the rotating disk 92, until it is thrown to the next fixed disk 91 and then enters the center of the next rotating disk 92 through the through hole 911, until it is finally gathered on the bottom shell 21 and led out through the liquid outlet 7. After multiple separation and aggregation processes, the liquid is thrown away from the rotating disk 92 in extremely fine droplets. The high-speed moving droplets are collided, sheared and splashed on the fixed disk 91. Under the action of the centrifugal force of the rotating gas, a gas-liquid interface with a very large specific surface area and constantly renewed is formed, thereby having an extremely high mass transfer rate.

[0019] Refer to Figure 2 As shown, the second embodiment is basically the same as the first embodiment, with the only difference being that: a plurality of the lower end sides of the intermediate casings 23 are symmetrically provided with notches 12, the notches 12 are connected to the interior of the shell 2, and the notches 12 are each provided with an adjusting member 13, the adjusting member 13 is used to adjust the vertical position of the fixing plate 91, and thereby adjust the spacing between the upper annular plate 912 and the lower annular plate 921.

[0020] A baffle 14 is extended from the fixed disk 91 corresponding to the position of the notch 12, and an inner sealing layer 15 is provided on the end face of the baffle 14 that fits with the interior of the intermediate casing 23. A transverse plate 16 is provided on the baffle 14 toward the notch 12, and a fixed plate 17 is fixedly connected to the transverse plate 16. An outer sealing layer 18 is provided on the end face of the fixed plate 17 that fits with the outer wall of the intermediate casing 23.

[0021] The adjusting member 13 includes a boss 131 extending laterally from the side wall of the intermediate casing 23 , and a screw rod 132 is movably connected to the boss 131 , and the screw rod 132 is threadedly connected to the fixing plate 17 , and the fixing plate 17 is driven to move vertically by rotating the screw rod 132 , thereby driving the fixing plate 91 to move up and down.

[0022] The above improvements are as follows: Figure 2As shown, since the current fixed disk 91 is fixedly connected to the shell 2, it is rather troublesome to adjust the spacing between the fixed disk 91 and the rotating disk 92 by adjusting the position of the rotating disk 92 on the rotating shaft. Therefore, notches 12 are symmetrically provided on the side of the lower end of the intermediate casing 23. The notches 12 are connected to the inside of the shell 2. Adjusting members 13 are provided at the notches 12. The adjusting members 13 are used to adjust the vertical position of the fixed disk 91, and then adjust the spacing between the upper annular plate 912 and the lower annular plate 921 to ensure that the upper annular plate 912 and the lower annular plate 921 are at a reasonable spacing. The fixed disk 91 is provided with a baffle 14 extending from the position corresponding to the notch 12, and the end surface of the baffle 14 that fits the inside of the intermediate casing 23 is provided with an inner sealing layer 15, and the baffle 14 is provided with a transverse plate 16 facing the notch 12, and the transverse plate 16 is fixedly connected with a fixed plate 17, and the end surface of the fixed plate 17 that fits the outer wall of the intermediate casing 23 is provided with an outer sealing layer 18, and the inner sealing layer 15 and the outer sealing layer 18 are used to ensure that the gas does not leak from the notch 12, and the adjusting member 13 includes a boss 131 extending laterally from the side wall of the intermediate casing 23, and a screw rod 132 is movably connected to the boss 131, and the screw rod 132 is threadedly connected to the fixed plate 17, and the screw rod 132 is symmetrically rotated by synchronous rotation. 132 then drives the vertical movement of the fixed plate 17, and then drives the movement of the fixed disk 91, so as to adjust the distance between the upper annular plate 912 and the lower annular plate 921, which is relatively convenient and quick. When distilling different materials, according to the physical properties of the materials themselves, for example, solvents with higher viscosity, the distance between the fixed disk 91 and the rotating disk 92 can be increased by the adjusting member 13 to reduce fluid resistance and improve mass transfer efficiency. For solvents with lower viscosity, the distance can be appropriately reduced by the adjusting member 13 to increase the gas-liquid contact area and the mass transfer surface area, and the distance between the fixed disk 91 and the rotating disk 92 can be adjusted according to the physical properties of the solvent itself to obtain better mass transfer efficiency.

[0023] The above description is only a preferred embodiment of the present invention and does not constitute any form of limitation to the present invention. Although the present invention has been disclosed as a preferred embodiment as above, it is not intended to limit the present invention. Any technical personnel in this field can make some changes or modify the technical contents disclosed above into equivalent embodiments without departing from the scope of the technical solution of the present invention. However, any brief modifications, equivalent changes and modifications made to the above embodiments based on the technical essence of the present invention without departing from the content of the technical solution of the present invention are still within the scope of the technical solution of the present invention.

Claims

1. A high-efficiency separator, comprising a bracket (1), characterized in that: The support (1) is provided with a shell (2) and a driving mechanism (3); the shell (2) is provided with an air outlet (4), a liquid return port (5), an air inlet (6), a liquid outlet (7) and a plurality of liquid inlets (8); the air outlet (4), the liquid return port (5), the air inlet (6), the liquid outlet (7) and the plurality of liquid inlets (8) are all in communication with the interior of the shell (2); a plurality of groups of separation components (9) are provided in the shell (2); the plurality of groups of separation components (9) are evenly distributed along the vertical direction of the shell (2); the separation components (9) include a fixed disk (91) connected to the shell (2); ) and a rotating disk (92) connected to a driving mechanism (3); a through hole (911) is provided at the center of the fixed disk (91) for liquid to flow toward the center of the rotating disk (92); a plurality of groups of lower annular plates (921) with concentric centers and different diameters are provided on the rotating disk (92), and a plurality of holes (922) are distributed around the circumference of the lower annular plates; an upper annular plate (912) is vertically extended downward from the lower end surface of the fixed disk (91) and is radially equidistant from the adjacent lower annular plates (921); the upper annular plate (912) and the lower annular plate (921) together form a channel for gas and liquid to circumferentially flow.

2. The high-efficiency separator according to claim 1, characterized in that: The housing (2) comprises a bottom shell (21), a top shell (22) and a plurality of intermediate shells (23), and the bottom shell (21), the top shell (22) and the plurality of intermediate shells (23) are all fixedly connected by bolts.

3. The high-efficiency separator according to claim 2 is characterized in that: The inner walls of the upper ends of the bottom shell (21) and the middle shell (23) are provided with stepped surfaces (10), and the lower end surface of the fixing plate (91) is in contact with the stepped surfaces (10) and fixedly connected via a fastener (11).

4. The high-efficiency separator according to claim 2, characterized in that: The lower ends of the plurality of intermediate casings (23) are symmetrically provided with notches (12), the notches (12) being connected to the interior of the casing (2), and the notches (12) are each provided with an adjusting member (13), the adjusting member (13) being used to adjust the vertical position of the fixing plate (91), thereby adjusting the spacing between the upper annular plate (912) and the lower annular plate (921).

5. The high-efficiency separator according to claim 4 is characterized in that: The fixed disk (91) is provided with a baffle (14) extending from the position corresponding to the notch (12); the end surface of the baffle (14) abutting against the inside of the intermediate casing (23) is provided with an inner sealing layer (15); the baffle (14) is provided with a transverse plate (16) facing the notch (12); the transverse plate (16) is fixedly connected to a fixed plate (17); and the end surface of the fixed plate (17) abutting against the outer wall of the intermediate casing (23) is provided with an outer sealing layer (18).

6. The high-efficiency separator according to claim 5, characterized in that: The adjusting member (13) comprises a boss (131) extending transversely from the side wall of the intermediate casing (23), a screw rod (132) being movably connected to the boss (131), the screw rod (132) being threadedly connected to the fixing plate (17), and the fixing plate (17) is driven to move vertically by rotating the screw rod (132), thereby driving the fixing plate (91) to move up and down.

7. The high-efficiency separator according to claim 3 or 6, characterized in that: The air outlet (4) and the liquid return port (5) are distributed on the top shell (22), the air inlet (6) is distributed on the side of the bottom shell (21), the liquid outlet (7) is distributed on the bottom of the bottom shell (21), and the liquid inlet (8) is distributed on the side of the middle shell (23).

8. The high-efficiency separator according to claim 7, characterized in that: The driving mechanism (3) comprises a main shaft (31) and a motor (32); one end of the main shaft (31) passes through the housing (2) and is connected to a bracket (1) on the top housing (22) via a bearing; the other end is connected to a pulley (33); the pulley (33) and the motor (32) are driven by a belt.

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