A method and device for intelligently recovering cobalt oxide from PTA residues

Abstract

The present invention discloses a method and device for intelligently recovering cobalt oxide from PTA residues, which relates to the technical field of cobalt oxide resource recovery. It includes a treatment tank. A first driving gear is installed at the top of the treatment tank. A reinforcing member is tightly connected to the side end of the treatment tank. A control brushless motor is installed at the top of the reinforcing member through a motor bracket. The bottom output end of the control brushless motor penetrates through the reinforcing member and is connected with a second driving gear. The first driving gear and the second driving gear are meshed and connected. Through the cooperation of the temperature adjustment adsorption component and the recovery adjustment component, the effective treatment of PTA residues, the efficient recovery of cobalt oxide, and the highly automated and intelligent control of the operation process are realized, the recycling rate of resources is improved, resource waste is reduced, and cross-infection generated during the recovery of cobalt oxide is reduced. Through the formation of multi-stage purification, the high purity of the finally recovered cobalt oxide is ensured, and the efficiency and purity of cobalt oxide recovery are prevented from being affected.

Description

Technical Field

[0001] The present invention relates to the technical field of cobalt oxide resource recovery, and specifically provides a method and device for intelligently recovering cobalt oxide from PTA residues. Background Art

[0002] Terephthalic acid (PTA) is an important petrochemical product ranked among the top fifty in the world in terms of production volume. It is the main raw material for producing polyester (PET) and is widely used in the production fields such as fiber polyester, polyester film, packaging bottles, PBT engineering plastics, plastic plasticizers, pesticides, and dyes. During the production process of PTA, the wastewater generated not only contains a large amount of organic compounds such as benzoic acid, terephthalic acid, and isophthalic acid, but also contains metal compounds such as cobalt and manganese. These metal compounds originate from the catalysts in the production process of terephthalic acid. After being treated by the activated sludge method, cobalt and manganese ions enter the sludge phase from the liquid phase and gradually accumulate. After dehydration and compression, a sludge cake is sent out for treatment.

[0003] However, in the prior art, in the operation of recovering cobalt oxide from PTA residues, due to the complex composition of PTA residues, containing various metal ions and other impurities, cross - contamination is likely to occur during the recovery of cobalt oxide, affecting the recovery efficiency and purity. Therefore, it is necessary to propose a method and device for intelligently recovering cobalt oxide from PTA residues. Summary of the Invention

[0004] The purpose of the present invention is to provide a method and device for intelligently recovering cobalt oxide from PTA residues, so as to solve the problem proposed in the above - mentioned background art that in the operation of recovering cobalt oxide from PTA residues, due to the complex composition of PTA residues, containing various metal ions and other impurities, cross - contamination is likely to occur during the recovery of cobalt oxide, affecting the recovery efficiency and purity.

[0005] To achieve the above purpose, the present invention provides the following technical solution: An intelligent cobalt oxide recovery device for PTA residues includes a treatment tank. A first transmission gear is installed at the top of the treatment tank. A reinforcement member is tightly connected to the side end of the treatment tank. A control brushless motor is installed on the top of the reinforcement member through a motor bracket. The bottom output end of the control brushless motor penetrates through the reinforcement member and is connected with a second transmission gear. The first transmission gear and the second transmission gear are meshed. The bottom of the axis end of the second transmission gear penetrates through the reinforcement member and is connected with a rotation adjustment rod. A temperature - adjustment adsorption assembly is installed at the bottom of the rotation adjustment rod. A position sensor is embedded on the side wall surface of the temperature - adjustment adsorption assembly. A recovery adjustment assembly is installed at the side end of the temperature - adjustment adsorption assembly;

[0006] The temperature adjustment adsorption assembly includes a first bevel gear, an axial end of the first bevel gear and a rotation adjustment rod are installed, the side end of the first bevel gear is meshingly connected with the second bevel gear, a stabilizing frame is installed on the outer side of the circumference of the second bevel gear, a speed regulator is installed on the outer side of the side end of the second bevel gear, the side end of the second bevel gear is connected with a temperature control box through a shaft column, a docking sealing core hole is opened on the side surface of the temperature control box, the axial end of the second bevel gear is connected with a central guide shaft, the central guide shaft and the shaft column are integrally formed, the outer circumference of the central guide shaft is fastened with a connecting rod, a nanocellulose adsorption roller is installed on the top of the connecting rod, an ultrafiltration membrane rack is installed on the bottom of the temperature control box, the bottom side end of the temperature control box is connected with a drain valve pipe, and a photoelectric sensor is installed on the side of the ultrafiltration membrane rack.

[0007] Preferably, an addition end is installed on the top side of the processing tank, and the addition end is configured as a two-way addition hole. A material guide valve tube is installed on the bottom side of the processing tank, and the side end of the material guide valve tube is connected to a small turntable tower, and the side end of the small turntable tower is connected to a recovery pipe.

[0008] Preferably, the side end of the recovery pipe is connected to a recovery material pump, the other side end of the recovery material pump is connected to an adsorption guide pipe, the adsorption guide pipe is connected to the top of the temperature control adjustment box through a control solenoid valve, the surface of the small turntable tower is connected to a chip removal pipe, and a separation membrane is installed inside the small turntable tower.

[0009] Preferably, the recovery and adjustment component includes a slide groove connecting frame, the interior of the slide groove connecting frame is slidably connected to a connecting support slide seat, the side end of the connecting support slide seat is installed with an electric telescopic guide rod, the top of the electric telescopic guide rod is installed with a docking outer tube, the side wall surface of the docking outer tube is connected to a telescopic material guide tube through an electric iris valve, and the docking outer tube and the docking sealing core hole are plugged together.

[0010] Preferably, the bottom of the slide connecting frame is fastened to a supporting side frame, a collecting and drying air chamber is installed on the top of the frame side of the supporting side frame, the telescopic material guide pipe and the collecting and drying air chamber are connected, a servo control motor is installed on the side end of the docking outer tube, and the output end of the servo control motor is connected to a gear set.

[0011] Preferably, an inner rotating tube is connected to the axial center end of one side of the gear set, and a plurality of groups of micro recovery and cleaning ends are embedded and installed on the top side surface of the inner rotating tube.

[0012] Preferably, the inner rotating tube and the docking outer tube form a rotor-stator structure under the drive of a servo control motor and a gear set, and the side end of the collecting and drying air chamber is connected to a collecting and discharging valve groove.

[0013] Preferably, a support frame is installed at the outer end of the bottom of the treatment tank, and the axial end of the first transmission gear penetrates through the treatment tank through an operation shaft column and is connected with a stirring and crushing structure.

[0014] Preferably, a waste discharge valve end is installed at the bottom end of the treatment tank. The waste discharge valve end and the material guiding valve pipe are electrically connected through an external controller at the bottom end of the treatment tank, and the control brushless motor and the servo control motor are sequentially connected with the external controller.

[0015] A method for an intelligent recovery cobalt oxide device for PTA residues includes the following steps:

[0016] S1. First, the PTA residues are placed into the treatment tank through the addition end set as a double-pass addition hole to form a separated one-side addition hole, and the external controller is made to start the control brushless motor, so that the second transmission gear and the first transmission gear drive the stirring and crushing structure to stir the PTA residues in the treatment tank. Water is added through an external peristaltic pump under the cooperation of a density sensor arranged in the treatment tank according to the stirring property. Then, an alkaline solvent or a chelating agent is added through the other-side addition hole of the addition end set as a double-pass addition hole, and the pH value of the solution is adjusted to 9-10 by using the Hengger reaction to neutralize the acidic substances in the PTA residues and promote the formation of hydroxide precipitates of cobalt and manganese.

[0017] S2. Then, the hydroxide precipitates of cobalt and manganese are guided to a small rotary disc column through the material guiding valve pipe, and the remaining liquid and PTA residue waste are discharged through the waste discharge valve end. After the operation in the small rotary disc column, the materials operated are transported to a temperature control adjustment box under the cooperation of a recovery pump and an adsorption delivery pipe, and under the cooperation of the temperature control adjustment box and a built-in high-precision temperature sensor, through the interval adjustment of temperature control, the best operation environment for the recovery of cobalt oxide is obtained.

[0018] S3. Secondly, after the treatment, according to the position fixed-point information of the position sensor, when the cobalt oxide is recovered subsequently, the remaining substances are discharged through the ultrafiltration membrane layer rack and the liquid discharge valve pipe, facilitating the subsequent recovery and utilization of other substances.

[0019] S4. Then, by using a recovery adjustment component, the cobalt oxide generated in the temperature control adjustment box is uniformly adsorbed and recovered, facilitating subsequent purification treatment.

[0020] Compared with the prior art, the beneficial effects of the present invention are:

[0021] 1. In the present invention, the second transmission gear and the rotating adjustment rod are synchronously and in the same direction rotated under the cooperation of the temperature adjustment adsorption component and the driving of the brushless motor, so as to drive the first bevel gear to form an operation, and then according to the rotation of the first bevel gear, the second bevel gear is driven to cooperate with the speed regulator, so that the central guide shaft drives the connecting rod and the nanocellulose adsorption roller to rotate inside the temperature control adjustment box, so that when the generated cobalt oxide and liquid fall on the surface of the ultrafiltration membrane layer frame, the ultrafiltration membrane layer frame and the cobalt oxide filtered on the surface are monitored by the photoelectric sensor. When the preset value is reached, the nanocellulose adsorption roller will contact the cobalt oxide filtered on the surface of the ultrafiltration membrane layer frame, and the fiber structure of the nanocellulose adsorption roller can selectively adsorb the cobalt oxide particles according to its physical and chemical properties, thereby realizing effective treatment of PTA residues, efficient recovery of cobalt oxide, and highly automated and intelligent control of the operation process, improving the recycling rate of resources, reducing resource waste, and reducing the cross infection generated by cobalt oxide during recovery, and through the multi-stage purification formed, the high purity of the finally recovered cobalt oxide is ensured, and the efficiency and purity of cobalt oxide recovery are avoided.

[0022] 2. In the present invention, after the cobalt oxide is treated, the electric telescopic guide rod is started under the control of an external controller in cooperation with the recovery and adjustment component, so that the connecting support slide can slide and adjust the position in the slide groove of the slide groove connecting frame, and the telescopic action of the electric telescopic guide rod can be used to adjust the position of the docking outer tube according to actual needs, so that the docking outer tube and the docking sealing core hole can be plugged in, and the generated cobalt oxide is guided to the collection and drying air chamber through the telescopic guide pipe controlled by the electric iris valve. Under the action of the collection and drying air chamber, the generated cobalt oxide is fully dried, and when the docking outer tube and the docking sealing core hole are plugged in, the docking outer tube and the nanocellulose adsorption roller form a buckle, that is, when the nanocellulose adsorption roller is connected, the outer tube and the nanocellulose adsorption roller are connected. The cellulose adsorption roller is adjusted to stop at the docking sealing core hole, the docking outer tube is inserted, and the nanocellulose adsorption roller is wrapped. Then the external controller starts the servo control motor, so that the servo control motor drives the gear set to rotate, so that the inner rotating tube can rotate when docking with the outer tube. When the inner rotating tube rotates, the multiple groups of micro-recovery and cleaning ends on the inner rotating tube can recover and clean the cobalt oxide particles adsorbed on the surface of the nanocellulose adsorption roller. At the same time, the nanocellulose adsorption roller after adsorption saturation can be regenerated through a specific desorption process (such as changing the pH value, temperature or using a specific solvent) to release the adsorbed cobalt oxide, so that the multiple groups of micro-recovery and cleaning ends can collect the cobalt oxide more comprehensively. BRIEF DESCRIPTION OF THE DRAWINGS

[0023] Figure 1 This is a schematic diagram of the main structure of an intelligent cobalt oxide recovery device for PTA residues according to the present invention;

[0024] Figure 2It is a schematic side view structure diagram of an intelligent cobalt oxide recovery device for PTA residue in the present invention;

[0025] Figure 3 It is a schematic internal sectional view structure diagram of the main body in an intelligent cobalt oxide recovery device for PTA residue in the present invention;

[0026] Figure 4 It is a schematic installation position structure diagram of a drain valve pipe and an ultrafiltration membrane layer rack in an intelligent cobalt oxide recovery device for PTA residue in the present invention;

[0027] Figure 5 It is a schematic structure diagram of a temperature adjustment adsorption component in an intelligent cobalt oxide recovery device for PTA residue in the present invention;

[0028] Figure 6 It is a partial schematic structure diagram of a temperature adjustment adsorption component in an intelligent cobalt oxide recovery device for PTA residue in the present invention;

[0029] Figure 7 It is a schematic structure diagram of a recovery adjustment component in an intelligent cobalt oxide recovery device for PTA residue in the present invention;

[0030] Figure 8 It is a partial internal sectional view structure diagram of a recovery adjustment component in an intelligent cobalt oxide recovery device for PTA residue in the present invention.

[0031] In the figure: 1. treatment tank; 2. addition end; 3. reinforcement member; 4. control brushless motor; 5. second transmission gear; 6. first transmission gear; 7. rotation adjustment rod; 8. temperature adjustment adsorption component; 81. first bevel gear; 82. second bevel gear; 83. stabilizing frame; 84. central guide shaft; 85. connecting rod; 86. nano-cellulose adsorption roller; 87. speed regulator; 88. photoelectric sensor; 9. position sensor; 10. support frame; 11. guide valve pipe; 12. small rotary disc column; 13. recovery pipe; 14. recovery adjustment component; 141. chute connecting frame; 142. connecting support sliding seat; 143. electric telescopic guide rod; 144. support side frame; 145. collection and drying air chamber; 146. telescopic feeding pipe; 147. docking outer pipe; 148. inner rotating pipe; 149. micro recovery cleaning end; 1490. gear set; 1491. servo control motor; 15. recovery feed pump; 16. adsorption and delivery pipe; 17. chip removal pipe; 18. collection and discharge valve groove; 19. stirring and crushing structure; 20. drain valve pipe; 21. docking sealing core hole; 22. ultrafiltration membrane layer rack. Detailed implementation manners

[0032] The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to 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. All other embodiments obtained by those of ordinary skill in the art based on the embodiments of the present invention without creative efforts shall fall within the protection scope of the present invention.

[0033] Referring to Figures 1 - 8 As shown in the figure: An intelligent cobalt oxide recovery device for PTA residue includes a treatment tank 1. A first transmission gear 6 is installed at the top of the treatment tank 1. A reinforcing member 3 is fixedly connected to the side end of the treatment tank 1. A control brushless motor 4 is installed on the top of the reinforcing member 3 through a motor bracket. The bottom output end of the control brushless motor 4 penetrates through the reinforcing member 3 and is connected with a second transmission gear 5. The first transmission gear 6 and the second transmission gear 5 are meshed and connected. The bottom of the axial center end of the second transmission gear 5 penetrates through the reinforcing member 3 and is connected with a rotation adjustment rod 7. A temperature adjustment adsorption assembly 8 is installed at the bottom of the rotation adjustment rod 7. A position sensor 9 is embedded on the side wall surface of the temperature adjustment adsorption assembly 8. A recovery adjustment assembly 14 is installed at the side end of the temperature adjustment adsorption assembly 8; The temperature adjustment adsorption assembly 8 includes a first bevel gear 81. The axial center end of the first bevel gear 81 is installed with the rotation adjustment rod 7. A second bevel gear 82 is meshed with the side end of the first bevel gear 81. A stabilizing frame 83 is installed on the outer circumference of the second bevel gear 82. A speed regulator 87 is installed on the outer side of the second bevel gear 82. The side end of the second bevel gear 82 is connected with a temperature control adjustment box through a shaft column. A docking sealing core hole 21 is opened on the side surface of the temperature control adjustment box. The axial center end of the second bevel gear 82 is connected with a central guide shaft 84. The central guide shaft 84 and the shaft column are integrally formed. A connecting rod 85 is fixedly connected to the outer circumference of the central guide shaft 84. A nano-cellulose adsorption roller 86 is installed at the top of the connecting rod 85. An ultrafiltration membrane layer rack 22 is installed at the bottom of the temperature control adjustment box. A drain valve pipe 20 is communicated with the bottom side end of the ultrafiltration membrane layer rack 22. An optoelectronic sensor 88 is installed on the side of the ultrafiltration membrane layer rack 22.

[0034] According to Figures 1 - 4As shown, an addition end 2 is installed on the top side of the treatment tank 1, and the addition end 2 is set as a double-pass addition hole. A material guide valve pipe 11 is installed on the bottom side of the treatment tank 1. The side end of the material guide valve pipe 11 is connected to a small turntable tower 12, and the side end of the small turntable tower 12 is connected to a recovery pipe 13. Under the action of the treatment tank 1, it is used to treat PTA residue, and the addition end 2 set as a double-pass addition hole is set for adding required materials or liquids, and the double-pass setting is convenient to avoid the mutual mixing of materials and liquids during subsequent addition. Phase interference, and the guide valve pipe 11 is used to guide the hydroxide precipitate formed by cobalt and manganese to the small turntable tower 12. Under the cooperation of the small turntable tower 12 and the built-in separation membrane, during operation, the hydroxide precipitate liquid (continuous phase) formed by cobalt and manganese flows from top to bottom, and the chelating agent (dispersed phase) is sprayed onto the disk surface through the small holes on the turntable and rotates with the disk surface. The two phases are fully in contact and mass transfer on the disk surface, and then other substances are discharged from the chip discharge pipe 17 of the tower, and the initially formed cobalt oxide is transported from the recovery pipe 13.

[0035] according to Figures 1 - 4 As shown, the side end of the recovery pipe 13 is connected to a recovery material pump 15, and the other side end of the recovery material pump 15 is connected to an adsorption guide pipe 16. The adsorption guide pipe 16 is connected to the top of the temperature control adjustment box through a control solenoid valve. The surface of the small turntable tower 12 is connected to a chip discharge pipe 17. A separation membrane is installed inside the small turntable tower 12. Under the action of the recovery material pump 15, the cobalt oxide initially formed in the recovery pipe 13 is extracted and transported to the adsorption guide pipe 16, so that the adsorption ultrafiltration membrane in the adsorption guide pipe 16 performs adsorption operation to further purify or treat the initially formed cobalt oxide.

[0036] according to Figure 7 and Figure 8 As shown, the recovery and adjustment component 14 includes a slide groove connecting frame 141, and the interior of the slide groove connecting frame 141 is slidably connected to a connecting support slide 142, and an electric telescopic guide rod 143 is installed on the side end of the connecting support slide 142, and a docking outer tube 147 is installed on the top of the electric telescopic guide rod 143. The side wall surface of the docking outer tube 147 is connected to a telescopic guide tube 146 through an electric iris valve, and the docking outer tube 147 and the docking sealing core hole 21 are plugged together. After the cobalt oxide is treated, the electric telescopic guide rod 143 is started under the control of an external controller, so that the connecting support slide 142 can slide and adjust its position in the slide groove of the slide groove connecting frame 141. In conjunction with the telescopic action of the electric telescopic guide rod 143, the position of the docking outer tube 147 can be adjusted according to actual needs, so that the docking outer tube 147 and the docking sealing core hole 21 are plugged together, and the generated cobalt oxide is guided to the collection and drying air chamber 145 through the telescopic guide tube 146 controlled by the electric iris valve.

[0037] according to Figure 7 and Figure 8As shown, the bottom of the slide connecting frame 141 is fastened with a supporting side frame 144, and a collecting and drying air chamber 145 is installed on the top of the frame side of the supporting side frame 144. The telescopic guide pipe 146 is connected to the collecting and drying air chamber 145, and a servo control motor 1491 is installed on the side end of the docking outer tube 147. The output end of the servo control motor 1491 is connected to a gear set 1490. Under the action of the collecting and drying air chamber 145, the generated cobalt oxide is fully dried. When the docking outer tube 147 and the docking sealing core hole 21 are plugged in, the docking outer tube 147 and the nanocellulose adsorption roller 86 are buckled, that is, when the nanocellulose adsorption roller 86 is adjusted to stop at the docking sealing core hole 21, the docking outer tube 147 is inserted and the nanocellulose adsorption roller 86 is wrapped. Then the external controller starts the servo control motor 1491, so that the servo control motor 1491 drives the gear set 1490 to rotate, so that the inner rotating tube 148 can rotate in the docking outer tube 147.

[0038] according to Figure 7 and Figure 8 As shown, the gear shaft center end on one side of the gear set 1490 is connected to the inner rotating tube 148, and a plurality of groups of micro-recovery and cleaning ends 149 are embedded and installed on the top side surface of the inner rotating tube 148. When the inner rotating tube 148 rotates, the plurality of groups of micro-recovery and cleaning ends 149 on the inner rotating tube 148 can recover and clean the cobalt oxide particles adsorbed on the surface of the nanocellulose adsorption roller 86.

[0039] according to Figure 7 and Figure 8 As shown, the inner rotating tube 148 and the docking outer tube 147 form a rotor-stator structure under the drive of the servo control motor 1491 and the gear set 1490, and the side end of the collecting and drying air chamber 145 is connected to the collecting and discharging valve slot 18. Under the action of the rotor-stator structure formed by the inner rotating tube 148 and the docking outer tube 147, the docking outer tube 147 is in a fixed stop state after being inserted into the docking sealing core hole 21, and the inner rotating tube 148 rotates outside the nanocellulose adsorption roller 86, thereby transporting the swept cobalt oxide from the telescopic guide tube 146 to the collecting and drying air chamber 145, and transporting it from the collecting and discharging valve slot 18 to the next purification process.

[0040] according to Figures 1 - 4 As shown, a support frame 10 is installed at the outer end of the bottom of the processing tank 1, and the axial end of the first transmission gear 6 passes through the processing tank 1 through an operating shaft column to connect with a stirring and crushing structure 19. The support frame 10 is installed on the outer side of the bottom of the processing tank 1 to provide stability and structural support, thereby ensuring that the entire device is stable and does not shake during operation, especially when the PTA residue is subjected to dynamic treatment such as stirring or crushing through the stirring and crushing structure 19 in the processing tank 1, the overall stability is guaranteed.

[0041] According to Figure 1 As shown, a waste discharge valve end is installed at the bottom end of the treatment tank 1. The waste discharge valve end and the material guiding valve pipe 11 are electrically connected through an external controller at the bottom end of the treatment tank 1. Moreover, the control brushless motor 4 and the servo control motor 1491 are sequentially connected to the external controller. A waste discharge valve end is installed at the bottom end of the treatment tank 1 for discharging the treated waste or finished products from the treatment tank 1. Under the action of the external controller, it is convenient to make the overall operation form an automated integrated operation, improving the operation efficiency.

[0042] The wiring diagrams of the control brushless motor 4, the nanocellulose adsorption roller 86, the photoelectric sensor 88, the position sensor 9, the servo control motor 1491 and the temperature control adjustment box in the present invention belong to the common knowledge in the art. Their working principles are already known technologies, and their models are selected according to actual use. Therefore, the control methods and wiring arrangements of the control brushless motor 4, the nanocellulose adsorption roller 86, the photoelectric sensor 88, the position sensor 9, the servo control motor 1491 and the temperature control adjustment box will not be explained in detail.

[0043] The method of using the device and the working principle are as follows: first, the PTA residue is placed in the treatment tank 1 through a separate addition hole formed by the addition end 2 set as a double-pass addition hole, and the brushless motor 4 is controlled by the external controller to drive the second transmission gear 5 and the first transmission gear 6 to drive the stirring and crushing structure 19 to stir the PTA residue in the treatment tank 1, and water is added through an external peristaltic pump in cooperation with the density sensor built into the treatment tank 1 according to the stirring property, and then an alkaline solvent or a chelating agent is added through the addition hole on the other side of the addition end 2 set as a double-pass addition hole, and the pH value of the solution is adjusted to 9-10 by the Hengel reaction to neutralize the acidic substances in the PTA residue, and promote the formation of hydroxide precipitation of cobalt and manganese, and then the cobalt and manganese are added through the guide valve pipe 11. Manganese forms hydroxide precipitation and is guided to the small turntable tower 12, so that under the cooperation of the small turntable tower 12 and the built-in separation membrane, when working, cobalt and manganese form hydroxide precipitation liquid (continuous phase) flowing from top to bottom, and the chelating agent (dispersed phase) is sprayed onto the disk surface through the small holes on the turntable and rotates with the disk surface. The two phases are fully in contact and mass transfer on the disk surface, and then other substances are discharged from the tower's chip discharge pipe 17, and the initially formed cobalt oxide is transported from the recovery pipe 13, and the remaining liquid and PTA residue waste are discharged through the waste discharge valve end. After the operation of the small turntable tower 12, under the cooperation of the recovery material pump 15 and the adsorption guide pipe 16, the adsorption ultrafiltration membrane in the adsorption guide pipe 16 performs adsorption operation to further purify or treat the initially formed The cobalt oxide is formed, and then the material to be operated is transported to the temperature control box, and with the cooperation of the temperature control box and the built-in high-precision temperature sensor, the temperature is adjusted in the range to obtain the best operating environment for the recovery of the cobalt oxide. After the initially formed cobalt oxide enters the temperature control box, under the drive of the brushless motor 4, the second transmission gear 5 and the rotating adjustment rod 7 are rotated synchronously and in the same direction, so as to drive the first bevel gear 81 to form an operation, and then according to the rotation of the first bevel gear 81, the second bevel gear 82 is driven to cooperate with the speed regulator 87, so that the central guide shaft 84 drives the connecting rod 85 and the nanocellulose adsorption roller 86 to rotate inside the temperature control box, so that when the generated cobalt oxide and liquid fall into the ultrafiltration membrane layer frame 2 2 surface, the ultrafiltration membrane frame 22 and the cobalt oxide filtered on the surface are monitored by the photoelectric sensor 88. When the preset value is reached, the nanocellulose adsorption roller 86 will contact the cobalt oxide filtered on the surface of the ultrafiltration membrane frame 22, and the fiber structure of the nanocellulose adsorption roller 86 can selectively adsorb the cobalt oxide particles according to its physical and chemical properties. Then, after the cobalt oxide is treated, the electric telescopic guide rod 143 is started under the control of the external controller, so that the connecting support slide 142 can slide and adjust the position in the slide groove of the slide groove connecting frame 141. With the telescopic action of the electric telescopic guide rod 143, the position of the docking outer tube 147 can be adjusted according to actual needs, so that the docking outer tube 147 and the docking sealing core hole 21 can be plugged in.The produced cobalt oxide is guided to the collection and drying chamber 145 through the telescopic material guiding pipe 146 controlled by the electric iris valve. Under the action of the collection and drying chamber 145, the produced cobalt oxide is fully dried. When the docking outer pipe 147 and the docking sealing core hole 21 are inserted, the docking outer pipe 147 and the nanocellulose adsorption roller 86 are buckled. That is, when the nanocellulose adsorption roller 86 is adjusted to stop at the docking sealing core hole 21, the docking outer pipe 147 is inserted and wraps the nanocellulose adsorption roller 86. Then, the external controller starts the servo control motor 1491, so that the servo control motor 1491 drives the gear set 1490 to rotate, facilitating the rotation of the inner rotating pipe 148 in the docking outer pipe 147. When the inner rotating pipe 148 rotates, the multiple groups of micro recovery and cleaning ends 149 on the inner rotating pipe 148 can recover and clean the cobalt oxide particles adsorbed on the surface of the nanocellulose adsorption roller 86. At the same time, the nanocellulose adsorption roller 86 after adsorption saturation can be regenerated through a specific desorption process (such as changing the pH value, temperature or using a specific solvent) to release the adsorbed cobalt oxide, enabling the multiple groups of micro recovery and cleaning ends 149 to collect cobalt oxide more comprehensively. The overall device effectively recovers cobalt oxide from PTA residues, improves the recycling rate of resources, reduces resource waste, reduces cross-infection generated during the recovery of cobalt oxide, and through the formed multi-stage purification, ensures the high purity of the finally recovered cobalt oxide, avoiding affecting the efficiency and purity of cobalt oxide recovery.

[0044] Although the present invention has been described in detail with reference to the foregoing embodiments, for those skilled in the art, they can still modify the technical solutions recorded 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 in the protection scope of the present invention.

Claims

1. An intelligent cobalt oxide recovery device for PTA residue, characterized in that: The invention comprises a treatment tank (1), wherein a first transmission gear (6) is installed on the top of the treatment tank (1), a reinforcement member (3) is fastened to the side end of the treatment tank (1), a brushless control motor (4) is installed on the top of the reinforcement member (3) through a motor frame, a second transmission gear (5) is connected to the bottom output end of the brushless control motor (4) through the reinforcement member (3), the first transmission gear (6) and the second transmission gear (5) are meshingly connected, a rotation adjustment rod (7) is connected to the bottom of the axial end of the second transmission gear (5) through the reinforcement member (3), a temperature adjustment adsorption component (8) is installed on the bottom of the rotation adjustment rod (7), a position sensor (9) is embedded in the side wall surface of the temperature adjustment adsorption component (8), and a recovery adjustment component (14) is installed on the side end of the temperature adjustment adsorption component (8); The temperature adjustment adsorption component (8) comprises a first bevel gear (81), the axial end of the first bevel gear (81) is installed with a rotating adjustment rod (7), the side end of the first bevel gear (81) is meshingly connected with a second bevel gear (82), a stabilizing frame (83) is installed on the outer side of the circumference of the second bevel gear (82), a speed regulator (87) is installed on the outer side of the side end of the second bevel gear (82), the side end of the second bevel gear (82) is connected with a temperature control box through a shaft column, and the side surface of the temperature control box is provided with a butt seal. The core hole (21) is provided with a central guide shaft (84) connected to the axial end of the second bevel gear (82), the central guide shaft (84) and the shaft column are integrally formed, the outer peripheral side of the central guide shaft (84) is fastened with a connecting rod (85), the top of the connecting rod (85) is installed with a nanocellulose adsorption roller (86), the bottom of the temperature control and adjustment box is installed with an ultrafiltration membrane rack (22), the bottom side end of the temperature control and adjustment box is connected with a drain valve pipe (20), and the side of the ultrafiltration membrane rack (22) is installed with a photoelectric sensor (88); An addition end (2) is installed on the top side of the treatment tank (1), and the addition end (2) is configured as a double-pass addition hole. A material guide valve pipe (11) is installed on the bottom side of the treatment tank (1), and the side end of the material guide valve pipe (11) is connected to a small turntable tower (12), and the side end of the small turntable tower (12) is connected to a recovery pipe (13); The side end of the recovery pipe (13) is connected to a recovery material pump (15), and the other side end of the recovery material pump (15) is connected to an adsorption guide pipe (16). The adsorption guide pipe (16) is connected to the top of the temperature control box through a control solenoid valve. The surface of the small turntable tower (12) is connected to a chip removal pipe (17), and a separation membrane is installed inside the small turntable tower (12).

2. The intelligent cobalt oxide recovery device for PTA residue according to claim 1 is characterized in that: The recovery and adjustment assembly (14) comprises a slide groove connecting frame (141), the interior of the slide groove connecting frame (141) is slidably connected to a connecting support slide seat (142), the side end of the connecting support slide seat (142) is mounted with an electric telescopic guide rod (143), the top of the electric telescopic guide rod (143) is mounted with a docking outer tube (147), the side wall surface of the docking outer tube (147) is connected to a telescopic material guide tube (146) via an electric iris valve, and the docking outer tube (147) and the docking sealing core hole (21) are plugged together.

3. The intelligent cobalt oxide recovery device for PTA residue according to claim 2 is characterized in that: The bottom of the slide connecting frame (141) is fastened to a supporting side frame (144), a collecting and drying air chamber (145) is mounted on the top of the frame side of the supporting side frame (144), the telescopic material guide tube (146) and the collecting and drying air chamber (145) are connected, and a servo control motor (1491) is mounted on the side end of the docking outer tube (147), and the output end of the servo control motor (1491) is connected to a gear set (1490).

4. The intelligent cobalt oxide recovery device for PTA residue according to claim 3 is characterized in that: An inner rotating tube (148) is connected to a gear shaft center end on one side of the gear set (1490), and a plurality of groups of micro recovery and cleaning ends (149) are mounted and engaged on the top surface of the inner rotating tube (148).

5. The intelligent cobalt oxide recovery device for PTA residue according to claim 4 is characterized in that: The inner rotating tube (148) and the docking outer tube (147) form a rotor-stator structure under the drive of the servo control motor (1491) and the gear set (1490), and the side end of the collection and drying air chamber (145) is connected to a collection and discharge valve groove (18).

6. The intelligent cobalt oxide recovery device for PTA residue according to claim 5 is characterized in that: A support frame (10) is installed at the outer bottom end of the processing tank (1), and the axial end of the first transmission gear (6) penetrates the processing tank (1) through an operating shaft column and is connected to a stirring and crushing structure (19).

7. The intelligent cobalt oxide recovery device for PTA residue according to claim 6 is characterized in that: A waste discharge valve end is installed at the bottom end of the processing tank (1), and the waste discharge valve end and the material guide valve pipe (11) are located at the bottom end of the processing tank (1) and are electrically connected through an external controller, and the control brushless motor (4) and the servo control motor (1491) are connected to the external controller in sequence.

8. A method for an intelligent cobalt oxide recovery device from PTA residue, characterized in that: The PTA residue intelligent cobalt oxide recovery device according to claim 7 is used, comprising the following steps: S1. First, a separate addition hole is formed on one side of the addition end (2) configured as a double-pass addition hole to place the PTA residue into the treatment tank (1), and the external controller starts to control the brushless motor (4), so that the second transmission gear (5) and the first transmission gear (6) drive the stirring and crushing structure (19) to stir the PTA residue in the treatment tank (1), and water is added through an external peristaltic pump in cooperation with a density sensor built into the treatment tank (1) according to the stirring property, and then an alkaline solvent or a chelating agent is added through the addition hole on the other side of the addition end (2) configured as a double-pass addition hole, and the pH value of the solution is adjusted to 9 to 10 by using the Hunger reaction to neutralize the acidic substances in the PTA residue and promote the formation of hydroxide precipitation of cobalt and manganese; S2. Next, the hydroxide precipitate formed by cobalt and manganese is guided to the small rotary disc tower (12) through the guide valve pipe (11), and the remaining liquid and PTA residue waste are discharged through the waste discharge valve end. After the operation of the small rotary disc tower (12), the material being operated is transported to the temperature control box in cooperation with the recovery material pump (15) and the adsorption guide pipe (16). In cooperation with the temperature control box and the built-in high-precision temperature sensor, the temperature is adjusted within a range to obtain the best operating environment for the recovery of cobalt oxide. S3, after the treatment, according to the position fixed point information of the position sensor (9), when the cobalt oxide is subsequently recovered, the remaining substances are discharged through the ultrafiltration membrane layer frame (22) and the drain valve pipe (20), so as to facilitate the subsequent recovery and utilization of other substances; S4. Next, the cobalt oxide produced in the temperature control box is uniformly adsorbed and recovered by using the recovery and adjustment component (14) to facilitate subsequent purification treatment.

Images