Online recovery equipment for electroplating heavy metal nickel
By designing an online recycling equipment for electroplated heavy metal nickel, the ion exchange resin is fully utilized by using the exchange cylinder and rotary joint structure, and the continuous use is achieved through the solenoid valve, the problem of low utilization rate of ion exchange resin in the prior art is solved and the efficiency of wastewater treatment is improved.
Patent Information
- Application Number
- CN202420852246.0
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-04-23
- Publication Date
- 2025-05-27
- Estimated Expiration
- 2034-04-23
AI Technical Summary
During the existing electroplating wastewater treatment process, the utilization rate of ion exchange resin is low, resulting in some resins not being used and the treatment efficiency is not high.
An electroplated heavy metal nickel online recycling equipment is designed, using the exchange cylinder and rotary joint structure, and the gears and gear rings are rotated through the servo motor, so that the movable tube is evenly distributed on the top of the inner cavity of the exchange cylinder, thereby making full use of the ion exchange resin and the continuous use of the exchange cylinder is realized through the solenoid valve.
The utilization rate of ion exchange resin is improved, local unused situations are avoided, and the continuity and efficiency of wastewater treatment are ensured.
Smart Images

Figure CN222907623U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the technical field of heavy metal recovery, in particular to an on-line recovery device for electroplated heavy metal nickel. Background Technique
[0002] The water quality of electroplating wastewater is complex and its components are not easy to control. It contains heavy metal ions such as chromium, cadmium, nickel, copper, zinc, gold, silver and cyanide, etc., and some are highly toxic substances that are carcinogenic, teratogenic and mutagenic.
[0003] In the process of treating electroplating wastewater with a relatively high content of heavy metal nickel, the main recovery of metallic nickel is realized through an ion exchanger. In the actual implementation process, the ion exchange cylinder is filled with ion exchange resin, and then the wastewater is introduced into the inner cavity of the ion exchange cylinder, so that the ion exchange resin can absorb metallic nickel. However, during the actual exchange treatment, when the wastewater is directly introduced into the exchange cylinder, the wastewater is unevenly distributed, resulting in excessive use of local ion exchange resin, while some ion exchange resin is not used. And after the ion exchange resin is used for a certain period of time, it needs to be exported for treatment, and the treatment of wastewater needs to be stopped, thus affecting the efficiency of wastewater treatment. Therefore, we propose an on-line recovery device for electroplated heavy metal nickel. Content of the Utility Model
[0004] The purpose of the utility model is to provide an on-line recovery device for electroplated heavy metal nickel, which solves the problems put forward in the background technique.
[0005] To achieve the above purpose, the utility model provides the following technical scheme: an on-line recovery device for electroplated heavy metal nickel, including an exchange cylinder, the number of the exchange cylinders is two, the top of the exchange cylinder is movably penetrated by a rotary joint, the tops of the two rotary joints are respectively fixedly communicated with both ends of a connecting pipe, the outer wall of the connecting pipe is fixedly communicated with a water inlet pipe, the tail end of the rotary joint is fixedly communicated with a movable pipe, a plurality of uniformly distributed water outlet holes are opened at the bottom of the movable pipe, a filter screen plate is obliquely fixed on the lower side of the inner cavity of the exchange cylinder, a toothed ring is fixedly sleeved on the outer wall of the rotary joint, and a gear is meshed with the outer wall of the toothed ring, and the gear is fixed to the outer end of the transmission shaft of a servo motor.
[0006] By adopting the above technical scheme, the wastewater is introduced into the inner cavity of the exchange cylinder, and ion exchange resin particles are filled in the inner cavity of the exchange cylinder. Then, after the wastewater enters the rotary joint, it will enter the movable pipe and be discharged along the water outlet holes. At the same time, starting the servo motor can drive the gear to rotate, thereby driving the toothed ring to rotate, so that the rotary joint drives the movable pipe to rotate, and further enables the movable pipe to evenly distribute water at the top of the inner cavity of the exchange cylinder, so that the ion exchange resin particles are fully utilized, and the utilization rate is improved.
[0007] As a preferred embodiment of the present utility model, electromagnetic valves are fixedly connected to both ends of the communicating pipe.
[0008] By adopting the above technical solution, after the ion exchange resin in a single exchange cylinder has been used for a certain period of time, the corresponding electromagnetic valve can be closed, and then another electromagnetic valve can be opened, so that the wastewater is introduced into another exchange cylinder for treatment, thereby realizing continuous and uninterrupted wastewater treatment and ensuring the efficiency of wastewater treatment.
[0009] As a preferred embodiment of the present utility model, a discharge port is provided on the outer wall of the exchange cylinder near the filter mesh plate, and a cover plate is fixed at the discharge port by bolts.
[0010] By adopting the above technical solution, the setting of the cover plate enables the fully absorbed ion resin particles to be directly exported for treatment by opening the cover plate.
[0011] As a preferred embodiment of the present utility model, a feed port is provided on one side of the top of the exchange cylinder, and an end cover is threadedly connected to the feed port.
[0012] By adopting the above technical solution, the setting of the feed port facilitates the introduction of ion exchange resin into the exchange cylinder.
[0013] As a preferred embodiment of the present utility model, a drain pipe is fixedly communicated with the bottom of the exchange cylinder.
[0014] By adopting the above technical solution, the setting of the drain pipe enables the wastewater from which nickel has been removed to be exported for further treatment.
[0015] As a preferred embodiment of the present utility model, the top of the servo motor is fixedly connected to the top of the exchange cylinder through a fixing frame.
[0016] By adopting the above technical solution, the high stability of the servo motor during use can be ensured.
[0017] Compared with the prior art, the beneficial effects of the present utility model are as follows:
[0018] An electroplating heavy metal nickel online recovery device of the technical solution of the present application can drive the gear to rotate through the servo motor, thereby enabling the toothed ring to rotate, and further enabling the rotary joint to drive the movable pipe to rotate. Thus, when the movable pipe is used to replenish water into the inner cavity of the exchange cylinder, the sewage can be evenly distributed in the exchange cylinder, so that the ion exchange resin filled in the inner cavity of the exchange cylinder can be fully utilized, avoiding the situation of local non-use, and improving the utilization rate of the ion exchange resin;
[0019] By closing one solenoid valve and opening another solenoid valve, it is possible to enable another exchange cylinder for recycling after the ion exchange resin in a single exchange cylinder is fully absorbed, and by opening the end plate, the ion exchange resin to be processed can be directly exported, which is convenient to operate, thus not affecting the continuity of wastewater treatment and further ensuring the efficiency of wastewater treatment. BRIEF DESCRIPTION OF THE DRAWINGS
[0020] Other features, objects, and advantages of the present utility model will become more apparent by reading the following detailed description of non-limiting embodiments with reference to the accompanying drawings:
[0021] Figure 1 FIG. is a schematic diagram of the overall structure of an on-line nickel electroplating heavy metal recovery device of the present utility model;
[0022] Figure 2 FIG. is a schematic cross-sectional structure diagram of an on-line nickel electroplating heavy metal recovery device of the present utility model;
[0023] Figure 3 FIG. is a schematic structure diagram of a movable tube of an on-line nickel electroplating heavy metal recovery device of the present utility model.
[0024] In the figure:
[0025] 1. Exchange cylinder; 11. Drain pipe; 12. Cover plate; 13. Filter screen plate;
[0026] 2. Rotary joint; 21. Movable tube; 22. Connecting pipe; 23. Water inlet pipe; 24. Solenoid valve; 25. Tooth ring; 26. Gear; 27. Servo motor; 28. Water outlet hole. DETAILED DESCRIPTION OF THE EMBODIMENTS
[0027] Please refer to Figures 1-3 , the present utility model provides a technical solution: an on-line nickel electroplating heavy metal recovery device, including an exchange cylinder 1, the number of exchange cylinders 1 is two, the top of the exchange cylinder 1 is movably penetrated by a rotary joint 2, the tops of the two rotary joints 2 are respectively fixedly communicated with both ends of a connecting pipe 22, the outer wall of the connecting pipe 22 is fixedly communicated with a water inlet pipe 23, the tail end of the rotary joint 2 is fixedly communicated with a movable tube 21, the bottom of the movable tube 21 is provided with a plurality of uniformly distributed water outlet holes 28, a filter screen plate 13 is obliquely fixed on the lower side of the inner cavity of the exchange cylinder 1, a tooth ring 25 is fixedly sleeved on the outer wall of the rotary joint 2, a gear 26 is meshed with the outer wall of the tooth ring 25, and the gear 26 is fixed to the outer end of the transmission shaft of a servo motor 27;
[0028] During actual use, the wastewater is introduced into the inner cavity of the exchange cylinder 1, and ion exchange resin particles are filled in the inner cavity of the exchange cylinder 1. Then, after the wastewater enters the rotary joint 2, it will enter the movable pipe 21 and be discharged along the water outlet holes 28. At the same time, starting the servo motor 27 can drive the gear 26 to rotate, thereby driving the toothed ring 25 to rotate, causing the rotary joint 2 to drive the movable pipe 21 to rotate, and further enabling the movable pipe 21 to distribute water evenly at the top of the inner cavity of the exchange cylinder 1, so that the ion exchange resin particles can be fully utilized, thereby improving the utilization rate;
[0029] Furthermore, a drain pipe 11 is fixedly connected to the bottom of the exchange cylinder 1. The setting of the drain pipe 11 enables the wastewater with nickel removed to be discharged and processed again;
[0030] Even further, a discharge port is provided on the outer wall of the exchange cylinder 1 near the filter mesh plate 13, and a cover plate 12 is fixed at the discharge port by bolts. The setting of the cover plate 12 enables the fully absorbed ion resin particles to be directly discharged for treatment by opening the cover plate 12;
[0031] It is worth introducing that a feed port is provided on one side of the top of the exchange cylinder 1, and an end cover is threadedly connected to the feed port. The setting of the feed port facilitates the introduction of ion exchange resin into the exchange cylinder 1;
[0032] It should be noted that the top of the servo motor 27 is fixedly connected to the top of the exchange cylinder 1 through a fixing bracket, so as to ensure high stability during the use of the servo motor 27;
[0033] As Figure 1 shown; electromagnetic valves 24 are fixedly connected to both ends of the connecting pipe 22. Thus, after the ion exchange resin in a single exchange cylinder 1 has been used for a certain period of time, the corresponding electromagnetic valve 24 can be closed, and then another electromagnetic valve 24 can be opened, enabling the wastewater to be introduced into another exchange cylinder 1 for treatment, thereby realizing continuous and uninterrupted wastewater treatment and ensuring the efficiency of wastewater treatment.
[0034] The implementation principle of an on-line recovery device for electroplated heavy metal nickel in this application is as follows: during actual use, wastewater is introduced into the inner cavity of the exchange cylinder 1, and ion exchange resin particles are filled in the inner cavity of the exchange cylinder 1. Then, after the wastewater enters the rotary joint 2, it will enter the movable pipe 21 and be discharged along the water outlet holes 28. At the same time, starting the servo motor 27 can drive the gear 26 to rotate, thereby driving the toothed ring 25 to rotate, so that the rotary joint 2 drives the movable pipe 21 to rotate, and then the movable pipe 21 can evenly distribute water at the top of the inner cavity of the exchange cylinder 1, so that the ion exchange resin particles are fully utilized, thereby improving the utilization rate. After the ion exchange resin in a single exchange cylinder 1 has been used for a certain period of time, the corresponding solenoid valve 24 can be closed, and then another solenoid valve 24 can be opened to introduce the wastewater into another exchange cylinder 1 for treatment, so as to realize continuous and uninterrupted wastewater treatment and ensure the efficiency of wastewater treatment.
[0035] In addition, all components included in the on-line recovery device for electroplated heavy metal nickel of the present utility model are common standard components or components known to those skilled in the art. Its structure and principle can be known to those skilled in the art through technical manuals or obtained through conventional experimental methods. At the idle place of this device, all the above-mentioned electrical components, which refer to power components, electrical components, and the adapted monitoring computer and power supply, are connected by wires. For the specific connection means, reference should be made to the following working principle to complete the electrical connection according to the sequence of operation of each electrical component. The detailed connection means are well-known technologies in the art. The following mainly introduces the working principle and process, and no further description of electrical control will be made.
Claims
1. An online recovery device for electroplating heavy metal nickel, comprising an exchange cylinder (1), characterized in that: The number of the exchange cylinders (1) is two. A rotary joint (2) is movably penetrated through the top of the exchange cylinder (1). The tops of the two rotary joints (2) are fixedly connected to the two ends of a connecting pipe (22) respectively. The outer wall of the connecting pipe (22) is fixedly connected to a water inlet pipe (23). The tail end of the rotary joint (2) is fixedly connected to a movable pipe (21). The bottom of the movable pipe (21) is provided with a plurality of evenly distributed water outlet holes (28). A filter screen plate (13) is obliquely fixed to the lower side of the inner cavity of the exchange cylinder (1). A gear ring (25) is fixedly sleeved on the outer wall of the rotary joint (2). A gear (26) is meshed with the outer wall of the gear ring (25). The gear (26) is fixed to the outer end of the transmission shaft of the servo motor (27).
2. The online recovery equipment for electroplating heavy metal nickel according to claim 1, characterized in that: Both ends of the connecting pipe (22) are fixedly connected with electromagnetic valves (24).
3. The online recovery equipment for electroplating heavy metal nickel according to claim 1, characterized in that: The outer wall of the exchange cylinder (1) is provided with a discharge port near the filter screen plate (13), and a cover plate (12) is fixed at the discharge port by bolts.
4. The online recovery equipment for electroplating heavy metal nickel according to claim 1, characterized in that: A feed inlet is provided on one side of the top of the exchange cylinder (1), and an end cover is threadedly connected to the feed inlet.
5. The online recovery equipment for electroplating heavy metal nickel according to claim 1, characterized in that: The bottom of the exchange cylinder (1) is fixedly connected to a drainage pipe (11).
6. The online recovery equipment for electroplating heavy metal nickel according to claim 1, characterized in that: The top of the servo motor (27) is fixedly connected to the top of the exchange cylinder (1) via a fixed frame.