A CBS solid-liquid separation device and process

Abstract

The invention discloses a CBS solid-liquid separation device and process, comprising an evaporation chamber one, an evaporation chamber two installed on one side of the evaporation chamber one and a partition installed between the two, and also comprising a liquid inlet pipe arranged on the evaporation chamber one, and an evaporation mechanism is installed inside the evaporation chamber one; a screening component arranged inside the evaporation chamber one, and a local area of ​​the screening component is located inside the evaporation chamber two; a collecting component located on the evaporation chamber two; a driving component arranged inside the evaporation chamber two; and an auxiliary circulation component located inside the evaporation chamber two. The CBS solid-liquid separation device and process separates solids and liquids in wastewater through the screening component, and transports them to the driving component so that the solids are transported to the discharge end in a directional manner, and under the action of an air suction pump, the solids are transported to the collection frame through a conveying frame for storage, and the liquid in a gaseous state is rapidly circulated under the action of the auxiliary circulation component, so as to achieve the purpose of solid-liquid separation in the wastewater.

Description

Technical Field

[0001] The invention relates to the technical field of solid-liquid separation, and in particular to a CBS solid-liquid separation device and process. Background Art

[0002] Rubber accelerator CBS refers to rubber vulcanization accelerator. Rubber vulcanization is mainly carried out using sulfur, but the reaction between sulfur and rubber is very slow, so vulcanization accelerators came into being. The addition of accelerators to the rubber can activate the vulcanizer, thereby accelerating the cross-linking reaction between the vulcanizer and the rubber molecules, achieving the effect of shortening the vulcanization time and lowering the vulcanization temperature. The main vulcanization accelerators used are mainly divided into sulfonamides, thiazoles, thiurams, and some guanidines, thioureas and dithiocarbamates according to their chemical structure. Among them, sulfonamides have the best comprehensive performance and are the most widely used;

[0003] At present, the domestic rubber additives enterprises mainly use physical and chemical + biochemical combined treatment technology, resin adsorption technology, membrane separation technology, simple distillation technology, extraction technology, wet catalytic oxidation technology and other treatment methods and technologies for production wastewater treatment;

[0004] Domestic production of rubber vulcanization accelerator CBS mostly uses rubber accelerator M as raw material, and a large amount of wastewater is generated in the production process. In addition to high concentrations of COD and salts, the concentration of dissolved unreacted M is also high, so that solid particles are often present in the wastewater generated in the production process. During the discharge process, blockage often occurs due to the solid impurities in the wastewater, which can easily affect the discharge of wastewater. For this reason, we propose a CBS solid-liquid separation device and process. Summary of the invention

[0005] The object of the present invention is to provide a CBS solid-liquid separation device and process to solve the problems raised in the above background technology.

[0006] To achieve the above-mentioned purpose, the present invention provides the following technical solutions: a CBS solid-liquid separation device and process, comprising an evaporation chamber one for evaporating and discharging liquid, an evaporation chamber two installed on one side of the evaporation chamber one and a partition installed between the two, and also comprising a liquid inlet pipe arranged on the evaporation chamber one, and an evaporation mechanism for evaporating liquid is installed inside the evaporation chamber one; a screening component arranged inside the evaporation chamber one for separating solid and liquid in wastewater, and a local area of ​​the screening component is located inside the evaporation chamber two; a collecting component located on the evaporation chamber two for collecting solids in the wastewater; a driving component arranged inside the evaporation chamber two for directional transportation of fixed materials in the wastewater; and an auxiliary circulation component located inside the evaporation chamber two for accelerating the gas circulation rate on the partition, so that the solid and liquid in the wastewater are separated under the action of the screening component, and the solid materials are transported to the collecting component for collection through the driving component.

[0007] Preferably, the screening assembly includes a filter plate arranged inside evaporation chamber one, and one end of the filter plate is arranged inside evaporation chamber two and is inclined downward, wherein a water storage plate is arranged inside evaporation chamber one and is below the filter plate, and one end of the water storage plate is arranged inside evaporation chamber two and is inclined upward, wherein the water storage plate is composed of a water storage area and a circulation area, and the water storage area is arranged inside evaporation chamber one, and the end of the circulation area is arranged inside evaporation chamber two, so that the moisture in the solid is filtered through the filter plate to the water storage plate and transported to the inside of evaporation chamber two.

[0008] Preferably, the driving assembly includes a shell, a double-helix feeding mechanism, a discharge end, a motor body, and a conveying frame, wherein the shell is installed inside the second evaporation chamber, and one end of the filter plate and the water storage plate are connected to the shell; the double-helix mechanism is installed inside the shell, wherein the end of the filter plate passes through the shell and extends into the interior thereof; the discharge end is installed at the end of the shell, and the end of the double-helix mechanism is located inside the discharge end; the motor body is installed inside the second evaporation chamber, and the motor body is installed with two single helix mechanisms inside the second evaporation chamber, respectively corresponding to the double-helix mechanisms; the conveying frame is installed on the discharge end, and the end of the conveying frame is connected to the collecting assembly, so that the solid material can be transported by the double-helix mechanism.

[0009] Preferably, the collecting assembly comprises a collecting frame arranged on the second evaporation chamber, and an air suction pump is installed on the collecting frame, wherein the end of the conveying frame is connected to the collecting frame so that the solid material can be sucked by the air suction pump.

[0010] Preferably, a plurality of clamping plates for limiting and fixing the evaporation mechanism are installed inside the evaporation chamber 1, so that the evaporation mechanism can be fixed by the clamping plates, and the liquid can be evaporated into gaseous state through the evaporation mechanism.

[0011] Preferably, a gear body one is installed on the output end of the motor body, and a gear body two for meshing with the gear body one is arranged inside the evaporation chamber two, and a rotating shaft for rotationally connected to the discharge end is installed on the gear body two, and a transmission member for connecting to an auxiliary circulation component is installed on the rotating shaft, so that the auxiliary circulation component can accelerate the gas flow rate on the side of the partition through the transmission member.

[0012] Preferably, the transmission member comprises a hinge plate 1 mounted on a rotating shaft, and a hinge plate 2 for rotationally connecting thereto is mounted on the hinge plate 1, wherein a connecting column for connecting to an auxiliary circulation component is mounted on the hinge plate 2.

[0013] Preferably, the auxiliary circulation component includes an output column connected to the connecting column, and a sleeve body for sliding connection with the output column is installed on the partition, wherein an air intake pipe for penetrating the inner wall of the partition and extending to the inside of an evaporation chamber is installed on the sleeve body, and a frame body is installed on the side wall of the partition inside the evaporation chamber, and an air blowing pipe is installed on the air intake pipe, so as to accelerate the circulation of liquid in a gaseous state through the air intake pipe and the air blowing pipe.

[0014] Preferably, both the air suction pipe and the air blowing pipe are provided with a one-way valve, and the frame body is provided with a groove body to prevent the liquid in a gaseous state from entering the air suction pipe and the air blowing pipe through the one-way valve.

[0015] A CBS solid-liquid separation process comprises the following steps:

[0016] S1: Solid-liquid separation in wastewater: wastewater generated by the production of rubber vulcanization accelerator CBS is transported into the evaporation chamber 1 through the liquid inlet pipe, and solid-liquid separation is performed through the screening component;

[0017] S2: Evaporation of liquid in wastewater and transportation of solids: the liquid in the wastewater is evaporated by the evaporation mechanism, and the solids in the wastewater are directionally transported by the driving component;

[0018] S3: Solid collection in wastewater: solid materials transported to the discharge end are collected by the collection assembly;

[0019] S4: Accelerating the gas flow rate on the side of the partition: During the transportation of solid materials in the wastewater, the gas flow rate on the side of the partition is accelerated by the motor body under the action of the auxiliary flow component;

[0020] S5: Reprocessing: The liquid in gaseous state is transported to the biochemical unit for reprocessing.

[0021] Compared with the prior art, the present invention has the following beneficial effects:

[0022] 1. The present invention separates solids and liquids in wastewater through a screening component, and transports the solids to a driving component through a filter plate, so that the solids pass through a shell and enter a double-helix mechanism so that the solids are directionally transported to a discharge end, and the solids are transported to a collection frame through a conveying frame for storage under the action of an air suction pump, and the liquid in a gaseous state is rapidly circulated under the action of an auxiliary circulation component, thereby achieving the purpose of solid-liquid separation in the wastewater, and collecting the solids in the wastewater to avoid blockage caused by the solids in the wastewater during the later discharge process.

[0023] 2. The present invention is provided with an auxiliary circulation component. During the transportation of solids, the auxiliary circulation component enables the suction pipe and the blowing pipe to accelerate the circulation rate of the liquid in the gaseous state on the side wall of the partition through the motor body to prevent the gaseous liquid on the side wall of the partition from adhering to its surface and reducing the flow rate.

[0024] 3. The present invention is provided with a screening assembly, which filters the liquid in the solid by means of a filter plate arranged in a downward slope, and transports the liquid by means of a water storage plate arranged in an upward slope, so as to prevent the liquid from entering the evaporation chamber 2. When the solid is transported into the driving assembly, the liquid falls from the filter plate onto the water storage plate, and moves along the surface of the water storage plate to the water storage area for storage. BRIEF DESCRIPTION OF THE DRAWINGS

[0025] Figure 1 It is a schematic diagram of the overall structure of the present invention;

[0026] Figure 2 It is a schematic diagram of the structure of the present invention;

[0027] Figure 3 This is a schematic diagram of the structure of the collection component of the present invention;

[0028] Figure 4 This is a schematic diagram of the structure of the drive assembly of the present invention;

[0029] Figure 5 It is a schematic diagram of the local structure of the driving component of the present invention;

[0030] Figure 6 It is a schematic diagram of the local structure of the present invention;

[0031] Figure 7 It is a partial structural schematic diagram of the evaporation chamber of the present invention;

[0032] Figure 8 This is a schematic diagram of the structure of the auxiliary circulation component of the present invention;

[0033] Fig. 9 It is a schematic diagram of the transmission structure of the present invention.

[0034] In the figure: 1-evaporation chamber one; 2-evaporation chamber two; 3-partition; 4-liquid inlet pipe; 5-evaporation mechanism; 6-screening assembly; 7-collection assembly; 8-driving assembly; 9-auxiliary circulation assembly; 10-cage; 11-gear body one; 12-gear body two; 13-rotating shaft; 14-transmission member; 61-filter plate; 62-water storage plate; 621-water storage area; 622-circulation area; 71-collection frame; 72-air suction pump; 81-housing; 82-double screw mechanism; 83-discharging end; 84-motor body; 85-conveying frame; 91-output column; 92-sleeve body; 93-suction pipe; 94-frame body; 95-blowing pipe; 96-check valve; 97-trough body; 141-hinge plate one; 142-hinge plate two; 143-connecting column. DETAILED DESCRIPTION

[0035] 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 described embodiments 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 creative work are within the scope of protection of the present invention.

[0036] See also Figure 1-9 The present invention provides a technical solution: a CBS solid-liquid separation device and process. The solution solves the problem that solid impurities in wastewater often cause blockage during the discharge process, which easily affects the discharge of wastewater. The solution makes corresponding improvements to the above problems, including an evaporation chamber 1 for evaporating and discharging liquid, an evaporation chamber 2 installed on one side of the evaporation chamber 1, and a partition 3 installed between the two, and the partition 3 is installed at the connection between the evaporation chamber 1 and the evaporation chamber 2, and a pipeline for conveying gaseous liquid is installed on the evaporation chamber 1, and also includes a liquid inlet pipe 4 installed on the evaporation chamber 1, so that the wastewater enters the evaporation chamber 1 through the liquid inlet pipe 4, and an evaporation mechanism 5 for evaporating the liquid is installed in the evaporation chamber 1, and a plurality of card plates 10 for limiting and fixing the evaporation mechanism 5 are installed in the evaporation chamber 1, so that when the wastewater enters the evaporation chamber 1, the evaporation mechanism 5 evaporates the liquid, and the evaporated gaseous liquid is transported along the pipeline to the biochemical unit for further treatment;

[0037] In order to prevent the solid mixed in the wastewater from blocking the pipeline during the discharge process, the present solution is provided with a screening component 6 for separating the solid and liquid in the wastewater inside the evaporation chamber 1, and a partial area of ​​the screening component 6 is located inside the evaporation chamber 2, so that the solid and liquid in the wastewater can be separated by the screening component 6;

[0038] The screening assembly 6 in this scheme includes a filter plate 61 fixedly installed inside the evaporation chamber 1, and one end of the filter plate 61 is arranged inside the evaporation chamber 2 and is inclined downward. It should be noted that the inclined downward shape described in this scheme is the shape from the evaporation chamber 1 to the evaporation chamber 2, and the inclined downward shape is set to facilitate the transportation of solids, wherein a water storage plate 62 is fixedly installed inside the evaporation chamber 1 and is located below the filter plate 61, and one end of the water storage plate 62 is located inside the evaporation chamber 2 and is set to be inclined upward. As for this scheme, The inclined upward slope is the same as the inclined downward slope, both of which are shapes from evaporation chamber 1 to evaporation chamber 2, so that in the process of conveying solids by the filter plate 61, the liquid adhering to the solids falls onto the water storage plate 62, wherein the water storage plate 62 is composed of a water storage area 621 and a flow area 622, and the water storage area 621 is arranged inside the evaporation chamber 1, and the end of the flow area 622 is arranged inside the evaporation chamber 2. It should be noted that the size of the water storage area 621 in this solution can be improved accordingly according to actual conditions;

[0039] The solids in the wastewater have a certain recycling value. In order to avoid wasting resources, the solids in the wastewater need to be recycled. Therefore, a collecting component 7 for collecting the solids in the wastewater is provided in the evaporation chamber 2.

[0040] In order to prevent a small amount of liquid from remaining in the solid, a specific design is required for the transportation of the solid during the collection of the solid. Therefore, a driving component 8 for directional transportation of the solid in the wastewater is provided inside the evaporation chamber 2 in this solution.

[0041] The driving assembly 8 in this scheme includes a shell 81, a double helix mechanism 82, a discharge end 83, a motor body 84, and a conveying frame 85, wherein the shell 81 is fixedly installed inside the evaporation chamber 2, and one end of the filter plate 61 and the water storage plate 62 are connected to the shell 81, and a trough 97 for conveying liquid to the water storage plate 62 is provided inside the shell 81 to prevent a small amount of liquid in the solid from entering the collecting assembly 7, and then the solid conveys the liquid to the water storage plate 62 through the trough 97 during the conveying process; wherein the double helix mechanism 82 is installed inside the shell 81, and the end of the filter plate 61 penetrates the shell 81 and extends into the inside thereof, while the water storage plate 62 is still connected to the shell 81, and a plurality of through holes are provided on the double helix mechanism 82, and the radius of the through hole is smaller than the solid, so that when the solid is directionally conveyed under the action of the double helix mechanism 82, the liquid falls into the trough 97 along the through hole, and enters the water storage plate 62 along the trough 97;

[0042] The discharge end 83 is installed at the end of the shell 81, and the end of the double helical mechanism 82 is located inside the discharge end 83; the motor body 84 is installed inside the evaporation chamber 2, and the motor body 84 is installed with two single helical mechanisms corresponding to the double helical mechanism 82 inside the evaporation chamber 2, so that the two motor bodies 84 drive the double helical mechanism 82 to rotate, so that the solid is transported in a directional manner, and during the transportation process, if there is liquid in the solid, it falls into the trough body 97 along the through hole, and is transported to the water storage plate 62 along the trough body 97; and the conveying frame 85 is installed on the discharge end 83, and the end of the conveying frame 85 is connected to the collecting component 7;

[0043] The collecting assembly 7 in this scheme includes a collecting frame 71 fixedly mounted on the evaporation chamber 2, and an air pump 72 is mounted on the collecting frame 71, wherein the end of the conveying frame 85 is connected to the collecting frame 71, and when the double-screw mechanism 82 allows the solid material to enter the discharge end 83, at this time, under the action of the air pump 72, the solid material enters the collecting frame 71 along the conveying frame 85. It should be noted that the air pump 72 in this scheme is a prior art, and thus this scheme does not make too many descriptions, and the output end of the air pump 72 can be set as a filter screen that blocks the solid material to prevent the solid material from entering the output end of the air pump 72;

[0044] A gear body 11 is installed on the output end of the motor body 84, and a gear body 12 for meshing with the gear body 11 is arranged inside the evaporation chamber 2, and a rotating shaft 13 for rotationally connecting with the discharge end 83 is installed on the gear body 12, so that when the motor body 84 rotates, the gear body 11 meshes with the gear body 2 12 to rotate synchronously, and an auxiliary circulation component 9 for accelerating the gas flow rate on the partition 3 is arranged inside the evaporation chamber 2, and a transmission member 14 for connecting the auxiliary circulation component 9 is installed on the rotating shaft 13, so that the rotating shaft 13 drives the auxiliary circulation component 9 under the action of the transmission member 14 to accelerate the flow rate of the gaseous liquid on the side wall of the partition 3.

[0045] The transmission member 14 in this embodiment includes a hinge plate 141 mounted on the rotating shaft 13, and a hinge plate 142 for rotationally connecting with the hinge plate 141 is mounted on the hinge plate 141. It should be noted that the hinge plate 141 and the hinge plate 142 are connected by a column, wherein the hinge plate 142 is mounted with a connecting column 143 for connecting with the auxiliary circulation component 9, so that when the rotating shaft 13 drives the hinge plate 141 to rotate, the hinge plate 142 drives the connecting column 143 to move;

[0046] The auxiliary circulation component 9 in this scheme includes an output column 91 connected to the connecting column 143, and a sleeve body 92 for sliding connection with the output column 91 is installed on the partition 3, so that the connecting column 143 drives the output column 91 to perform a directional limiting action inside the sleeve. It should be noted that the relationship between the sleeve body 92 and the output column 91 in this scheme is similar to the principle of the prior art syringe, so that during the rotation of the rotating shaft 13, the output column 91 performs an air suction and blowing action inside the sleeve body 92, wherein the sleeve body 92 is installed with an air suction pipe 93 for penetrating the inner wall of the partition 3 and extending to the inside of the evaporation chamber 1, and the partition 3 A frame body 94 is installed on the side wall inside the evaporation chamber 1, and a blowing pipe 95 is installed on the intake pipe 93. Both the intake pipe 93 and the blowing pipe 95 are provided with a one-way valve 96, and a groove body 97 is provided on the frame body 94, wherein an automatic exhaust valve is also installed on the intake pipe 93, which automatically closes when liquid water enters, in order to prevent the liquid in the gaseous state from entering into the sleeve. It should be noted that the automatic exhaust valve is a prior art and will not be elaborated on in detail. The one-way valve 96 on the intake pipe 93 and the blowing pipe 95 is used to prevent air from entering the intake pipe 93 during blowing, and to ensure that the blowing pipe 95 is in a closed and sealed state during inhalation.

[0047] A CBS solid-liquid separation process, applicable to the above CBS solid-liquid separation system:

[0048] S1: Solid-liquid separation in wastewater: The wastewater generated by the production of rubber vulcanization accelerator CBS is transported into the evaporation chamber 1 through the liquid inlet pipe 4, and solid-liquid separation is performed through the screening component 6;

[0049] S2: Evaporation of liquid in wastewater and transportation of solids: the liquid in the wastewater is evaporated by the evaporation mechanism 5, and the solids in the wastewater are directionally transported by the driving component 8;

[0050] S3: Solid collection in wastewater: solid materials transported to the discharge end 83 are collected by the collection assembly 7;

[0051] S4: Accelerating the gas flow rate on the side of the partition 3: During the transportation of solid materials in the wastewater, the gas flow rate on the side of the partition 3 is accelerated by the motor body 84 under the action of the auxiliary flow component 9;

[0052] S5: Reprocessing: The liquid in gaseous state is transported to the biochemical unit for reprocessing

[0053] Specifically, the staff passes the wastewater into the evaporation chamber 1 through the liquid inlet pipe 4, the wastewater is filtered along the filter plate 61, and the liquid falls onto the water storage plate 62, while the solid enters the double helix mechanism 82 along the filter plate 61. At this time, the motor body 84 starts to drive the double helix mechanism 82 to rotate, and the solid material enters the discharge end 83 through the shell 81. During the rotation process, any liquid on the solid enters the tank body 97 along the through hole, and enters the water storage area 621 along the water storage plate 62 for storage, and enters the discharge end 83. The solids are collected along the conveying frame 85 into the collecting frame 71 under the action of the suction pump 72. During the rotation of the motor body 84, the gear body 11 meshes with the gear body 2 12 to rotate synchronously, so that the gear body 2 12 drives the rotating shaft 13 to rotate, thereby driving the output column 91 to perform directional movement in the sleeve body 92 under the action of the hinge plate 141, the hinge plate 2 142 and the connecting column 143, so that the flow rate of the gaseous liquid is accelerated through the suction pipe 93, the blowing pipe 95 and the one-way valve 96.

[0054] It should be noted that, in this article, relational terms such as first and second, etc. are only used to distinguish one entity or operation from another entity or operation, and do not necessarily require or imply any such actual relationship or order between these entities or operations. Moreover, the terms "include", "comprise" or any other variants thereof are intended to cover non-exclusive inclusion, so that a process, method, article or device including a series of elements includes not only those elements, but also other elements not explicitly listed, or also includes elements inherent to such process, method, article or device.

[0055] Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that various changes, modifications, substitutions and variations may be made to the embodiments without departing from the principles and spirit of the present invention, and that the scope of the present invention is defined by the appended claims and their equivalents.

Claims

1. A CBS solid-liquid separation device, comprising an evaporation chamber 1 (1) for evaporating and discharging a liquid, an evaporation chamber 2 (2) installed on one side of the evaporation chamber 1 (1), and a partition (3) installed between the two, characterized in that: Also includes: A liquid inlet pipe (4) is arranged on the evaporation chamber one (1), and an evaporation mechanism (5) for evaporating liquid is installed inside the evaporation chamber one (1); A screening component (6) is arranged inside the first evaporation chamber (1) and is used to separate solid and liquid in the wastewater, and a local area of ​​the screening component (6) is located inside the second evaporation chamber (2); A collecting assembly (7) located on the second evaporation chamber (2) and used for collecting solids in the wastewater; A driving assembly (8) disposed inside the second evaporation chamber (2) for directional transport of fixed substances in the wastewater; and; An auxiliary circulation component (9) is located inside the second evaporation chamber (2) and is used to accelerate the gas flow rate on the partition (3); the screening component (6) includes a filter plate (61) arranged inside the first evaporation chamber (1), and one end of the filter plate (61) is arranged inside the second evaporation chamber (2) and is inclined downward, wherein a water storage plate (62) is arranged inside the first evaporation chamber (1) and is located below the filter plate (61), and one end of the water storage plate (62) is arranged inside the second evaporation chamber (2) and is arranged in an inclined upward shape, wherein the water storage plate (62) is composed of a water storage area (621) and a flow area (622), and the The water storage area (621) is arranged inside the first evaporation chamber (1), and the end of the circulation area (622) is arranged inside the second evaporation chamber (2); the driving component (8) comprises a shell (81), a double helical mechanism (82), a discharge end (83), a motor body (84), and a conveying frame (85); the shell (81) is installed inside the second evaporation chamber (2), and one end of the filter plate (61) and the water storage plate (62) are connected to the shell (81); the double helical mechanism (82) is installed inside the shell (81), and the end of the filter plate (61) passes through the shell (81) and extends into the interior thereof; The discharge end (83) is mounted on the end of the shell (81), and the end of the double helical mechanism (82) is located inside the discharge end (83); the motor body (84) is mounted inside the second evaporation chamber (2), and the motor body (84) is mounted inside the second evaporation chamber (2) with two single helical mechanisms corresponding to the double helical mechanism (82); the conveying frame (85) is mounted on the discharge end (83), and the end of the conveying frame (85) is connected to the collection component (7); the collection component (7) comprises a collection frame (71) arranged on the second evaporation chamber (2), and an air suction pump (72) is mounted on the collection frame (71), wherein the end of the conveying frame (85) is connected to the collection frame (71).

2. A CBS solid-liquid separation device according to claim 1, characterized in that: A plurality of clamping plates (10) for limiting and fixing the evaporation mechanism (5) are installed inside the evaporation chamber 1 (1).

3. A CBS solid-liquid separation device according to claim 1, characterized in that: A gear body 1 (11) is mounted on the output end of the motor body (84), and a gear body 2 (12) for meshing with the gear body 1 (11) is arranged inside the evaporation chamber 2 (2), and a rotating shaft (13) for rotationally connecting with the discharge end (83) is mounted on the gear body 2 (12), and a transmission member (14) for connecting with the auxiliary circulation component (9) is mounted on the rotating shaft (13).

4. A CBS solid-liquid separation device according to claim 3, characterized in that: The transmission member (14) comprises a hinge plate 1 (141) mounted on the rotating shaft (13), and a hinge plate 2 (142) for rotationally connecting with the hinge plate 1 (141) is mounted on the hinge plate 1 (141), wherein a connecting column (143) for connecting with the auxiliary circulation component (9) is mounted on the hinge plate 2 (142).

5. A CBS solid-liquid separation device according to claim 1 or 4, characterized in that: The auxiliary circulation component (9) comprises an output column (91) connected to a connecting column (143), and a sleeve body (92) for sliding connection with the output column (91) is installed on the partition (3), wherein an air intake pipe (93) for penetrating the inner wall of the partition (3) and extending to the inside of the evaporation chamber (1) is installed on the sleeve body (92), and a frame body (94) is installed on the side wall of the partition (3) inside the evaporation chamber (1), and an air blowing pipe (95) is installed on the air intake pipe (93).

6. A CBS solid-liquid separation device according to claim 5, characterized in that: The air suction pipe (93) and the air blowing pipe (95) are both provided with a one-way valve (96), and the frame body (94) is provided with a groove body (97).

7. A separation process of a CBS solid-liquid separation device according to any one of claims 1 to 6, characterized in that: The following steps are involved: S1: Solid-liquid separation in wastewater: wastewater generated by the production of rubber vulcanization accelerator CBS is transported into the evaporation chamber 1 (1) through the liquid inlet pipe (4), and solid-liquid separation is performed through the screening component (6); S2: Evaporation of liquid in wastewater and transportation of solids: the liquid in the wastewater is evaporated by the evaporation mechanism (5), and the solids in the wastewater are directionally transported by the driving component (8); S3: solid collection in wastewater: solid materials transported to the discharge end (83) are collected by the collection assembly (7); S4: Accelerating the gas flow rate on the side of the partition (3): During the transportation of solid materials in the wastewater, the gas flow rate on the side of the partition (3) is accelerated by the motor body (84) under the action of the auxiliary flow component (9); S5: Reprocessing: The liquid in gaseous state is transported to the biochemical unit for reprocessing.

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