A gold-plated cylinder body structure and electroplating equipment

Abstract

This invention provides a gold plating tank structure and electroplating equipment, including a main tank with a channel on its outer wall and a central column inside; an inner anode mesh disposed on the outer wall of the central column; an outer anode mesh disposed on the inner side of the main tank wall; and a secondary tank connected to the outer wall of the main tank via a channel. The volume ratio of the main tank to the secondary tank is 1:0.2 to 1:1. The inner and outer anode meshes are used to output current for electroplating the product, while the main tank is used to electroplat the product to be electroplated. The volume ratio of the main tank to the secondary tank is adjusted to improve electroplating quality and the efficiency of the electroplating solution. By adjusting the volume ratio of the main tank to the secondary tank to 1:0.2 to 1:1, and determining the volume ratio between the main tank and the secondary tank according to the properties of the electroplating solution and the function of the secondary tank, this invention avoids situations where the secondary tank is too large or too small, which could affect product quality and cause waste. It also avoids waste of the gold plating solution, thereby improving gold plating efficiency and production efficiency.

Description

Technical Field

[0001] This utility model relates to the field of gold plating equipment technology, and in particular to a gold plating cylinder structure and electroplating equipment. Background Technology

[0002] The volume ratio of the main tank and auxiliary tank in traditional gold casting machines is unreasonable: First, it fails to consider the properties of the added chemical components and the function of the auxiliary tank, resulting in the auxiliary tank being too large or too small. An undersized auxiliary tank affects product quality, while an oversized one increases gold consumption and investment, leading to waste. Second, it fails to consider the electroplating characteristics of the main tank. An overly deep main tank makes operation inconvenient for workers, and also affects the product quality and production speed of the intermediate layer. An undersized main tank (distance between the inner and outer anode meshes) affects product quality and production speed, while an oversized one increases investment and wastes plating solution.

[0003] In summary, in the existing technology, the unreasonable volume ratio of the main groove and the auxiliary groove of the cylinder of the gold casting machine will affect the quality of the product, as well as cause waste and low efficiency, which will lead to excessively high costs. Utility Model Content

[0004] Therefore, the purpose of this utility model is to provide a gold plating cylinder structure and electroplating equipment to overcome the shortcomings of the prior art.

[0005] In a first aspect, this utility model provides a gold-plated cylinder structure, comprising:

[0006] The main channel has a channel on its outer wall, a central column inside the main channel, and a main channel wall on its upper surface.

[0007] An inner anode mesh is disposed on the outer wall of the central column;

[0008] An outer anode mesh is disposed on the inner side of the main tank wall;

[0009] The secondary tank is connected to the outer wall of the main tank and is connected to the main tank via the channel. The volume ratio of the main tank to the secondary tank is 1:0.2 to 1:1.

[0010] The inner anode mesh and the outer anode mesh are used to output current to electroplate the product, the main tank is used to electroplate the product to be electroplated, and the volume ratio of the main tank to the auxiliary tank is used to improve the electroplating quality and the utilization efficiency of the electroplating solution.

[0011] Compared with the prior art, the beneficial effects of this utility model are: by adjusting the volume ratio of the main tank to the auxiliary tank to 1:0.2 to 1:1, and determining the volume ratio between the main tank and the auxiliary tank according to the properties of the electroplating solution and the function of the auxiliary tank, it is possible to avoid the situation where the auxiliary tank is too large or too small, which would affect product quality and cause waste. It is also possible to avoid the waste of gold plating solution and improve gold plating efficiency and production efficiency.

[0012] Furthermore, the volume ratio of the main tank to the secondary tank is 1:0.35 to 1:0.65.

[0013] Furthermore, the volume ratio of the main tank to the secondary tank is 1:0.2 to 1:0.45.

[0014] Furthermore, the volume ratio of the main tank to the secondary tank is 1:0.5 to 1:1.

[0015] Furthermore, the distance between the inner anode mesh and the outer anode mesh is 12cm to 26cm.

[0016] Furthermore, the distance between the inner anode mesh, the outer anode mesh and the product to be plated with gold is greater than 4 cm.

[0017] Furthermore, the central column is located at the center of the main groove.

[0018] Secondly, this utility model also provides an electroplating device, including the above-mentioned gold plating cylinder structure. Attached Figure Description

[0019] Figure 1 This is a schematic diagram of the gold-plated cylinder structure in the first embodiment of this utility model.

[0020] Explanation of key component symbols:

[0021] 10. Main tank; 11. Channel; 12. Central column; 13. Main tank wall;

[0022] 20. Inner anode mesh;

[0023] 30. External anode mesh;

[0024] 40. Secondary tank.

[0025] The following detailed description, in conjunction with the accompanying drawings, will further illustrate this utility model. Detailed Implementation

[0026] To facilitate understanding of this utility model, a more complete description will be given below with reference to the accompanying drawings. Several embodiments of this utility model are shown in the drawings. However, this utility model can be implemented in many different forms and is not limited to the embodiments described herein. Rather, these embodiments are provided so that the disclosure of this utility model will be more thorough and complete.

[0027] It should be noted that when a component is said to be "fixed to" another component, it can be directly on the other component or there may be an intervening component. When a component is said to be "connected to" another component, it can be directly connected to the other component or there may be an intervening component. The terms "vertical," "horizontal," "left," "right," and similar expressions used in this document are for illustrative purposes only.

[0028] Unless otherwise defined, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention pertains. The terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the invention. The term "and / or" as used herein includes any and all combinations of one or more of the associated listed items.

[0029] Example 1

[0030] Please see Figure 1 The figure shows the structure of the gold plating tank in the first embodiment of the present invention, including a main tank 10, an inner anode mesh 20, an outer anode mesh 30, and a secondary tank 40.

[0031] The main tank 10 has a channel 11 on its outer wall, a central column 12 inside the main tank 10, and a main tank wall 13 on the main tank 10. The inner anode mesh 20 is disposed on the outer wall of the central column 12, and the outer anode mesh 30 is disposed on the inner side of the main tank wall 13. The secondary tank 40 is connected to the outer wall of the main tank 10 and is connected to the main tank 10 via the channel 11. The volume ratio of the main tank 10 to the secondary tank 40 is 1:0.2 to 1:1. In this embodiment, the volume ratio of the main tank 10 to the secondary tank 40 is 1:0.35 to 1:0.65. The inner anode mesh 20 and the outer anode mesh 30 are used to output current to electroplate the product, and the main tank 10 is used to electroplate the product to be electroplated. The volume ratio of the main tank 10 to the secondary tank 40 is used to improve the electroplating quality and the utilization efficiency of the electroplating solution.

[0032] Understandably, when gold mud or additives dissolve slowly, the volume ratio between the main tank 10 and the secondary tank 40 is adjusted to between 1:0.35 and 1:0.65. Since gold mud or difficult-to-dissolve additives require a larger dissolution space and a longer dissolution time, a smaller secondary tank 40 will affect the dissolution quality and speed. Specifically, in this embodiment, the volume ratio between the main tank 10 and the secondary tank 40 is 1:0.65 to improve the volumetric speed of the gold mud or additives.

[0033] Specifically, in this embodiment, the inner anode mesh 20 is disposed at the center of the main groove 10, so that the inner anode mesh 20 and the outer anode mesh 30 are arranged concentrically.

[0034] Furthermore, if the product is too close to the inner anode mesh 20 or the outer anode mesh 30, the difference between the high and low potentials of the product will be large. The side closer to the inner anode mesh 20 or the outer anode mesh 30 is more prone to burning or will have more and thicker gold plating, while the side away from the inner anode mesh 20 or the outer anode mesh 30 will have less gold plating and a thinner plating. In this embodiment, the distance between the inner anode mesh 20 and the outer anode mesh 30 is 26cm, so that the hanging space in the main tank 10 is large, which in turn allows the product to be gold-plated to be further away from the outer anode mesh 30 and the inner anode mesh 20, thereby increasing the gold plating speed and resulting in a better quality gold-plated product.

[0035] Furthermore, in this embodiment, the distance between the inner anode mesh 20, the outer anode mesh 30 and the product to be plated with gold is 8cm.

[0036] It is worth noting that by adjusting the distance between the inner anode mesh 20 and the outer anode mesh 30 according to different production settings, the product quality can be optimized, thereby improving production efficiency, increasing production speed, improving product quality, and reducing operational difficulty.

[0037] Example 2

[0038] The difference between the gold-plating cylinder structure in this embodiment and the gold-plating cylinder structure in the first embodiment is as follows:

[0039] The volume ratio of the main tank 10 to the secondary tank 40 is 1:0.2 to 1:0.45. Specifically, in this embodiment, the volume ratio of the main tank 10 to the secondary tank 40 is 1:0.3.

[0040] It should be noted that when using gold solution or additives that dissolve quickly, the volume ratio of the main tank 10 to the secondary tank 40 is set to 1:0.2 to 1:0.45. In this embodiment, the volume ratio of the main tank 10 to the secondary tank 40 is specifically 1:0.3. This achieves better product quality and production efficiency, as well as better gold utilization, reducing investment and waste. It is also worth noting that gold solution or easily soluble additives can be dissolved using a smaller secondary tank 40, reducing the amount of gold used.

[0041] In this embodiment, the distance between the inner anode mesh 20 and the outer anode mesh 30 is 18cm. The distance between the inner anode mesh 20, the outer anode mesh 30, and the product to be plated is 7cm. This allows for optimal product quality and higher production efficiency. Appropriate electroplating solution depth can increase production speed, improve product quality, and reduce operational difficulty.

[0042] Example 3

[0043] The difference between the gold-plating cylinder structure in this embodiment and the gold-plating cylinder structure in the first embodiment is as follows:

[0044] The volume ratio of the main tank 10 to the secondary tank 40 is 1:0.5 to 1:1. Specifically, in this embodiment, the volume ratio of the main tank 10 to the secondary tank 40 is 1:0.8.

[0045] It should be noted that when the volume of the main tank 10 is less than 60 liters, the volume ratio of the main tank 10 to the secondary tank 40 is set to 1:0.5 to 1:1. In this embodiment, the volume ratio of the main tank 10 to the secondary tank 40 is specifically 1:0.8. This allows for better product quality and production efficiency, as well as better utilization of gold, reducing investment and waste.

[0046] It is worth noting that setting a reasonable and appropriate main tank to 10 and secondary tank to 40 volume ratio for different types of pharmaceutical solutions can not only improve product quality and production efficiency, but also enhance the utilization efficiency of gold, thereby reducing investment and waste.

[0047] In this embodiment, the distance between the inner anode mesh 20 and the outer anode mesh 30 is 12cm. The distance between the inner anode mesh 20, the outer anode mesh 30, and the product to be plated is 6cm. This allows for optimal product quality and higher production efficiency. Appropriate electroplating solution depth can increase production speed, improve product quality, and reduce operational difficulty.

[0048] This utility model also proposes an electroplating device, including the gold plating tank structure in the above embodiments.

[0049] In summary, the gold plating tank structure in the above embodiments of this utility model, by adjusting the volume ratio of the main tank 10 to the secondary tank 40 to 1:0.2 to 1:1, and determining the volume ratio between the main tank 10 and the secondary tank 40 according to the properties of the electroplating solution and the function of the secondary tank 40, can avoid the secondary tank 40 being too large or too small, which would affect product quality and cause waste. It can also avoid the waste of gold plating solution and improve gold plating efficiency and production efficiency.

[0050] In the description of this specification, the references to terms such as "one embodiment," "some embodiments," "example," "specific example," or "some examples," etc., indicate that a specific feature, structure, material, or characteristic described in connection with that embodiment or example is included in at least one embodiment or example of the present invention. In this specification, the illustrative expressions of the above terms do not necessarily refer to the same embodiment or example. Furthermore, the specific features, structures, materials, or characteristics described may be combined in any suitable manner in one or more embodiments or examples.

[0051] The embodiments described above are merely illustrative of several implementations of this utility model, and while the descriptions are relatively specific and detailed, they should not be construed as limiting the scope of this utility model patent. It should be noted that those skilled in the art can make various modifications and improvements without departing from the concept of this utility model, and these all fall within the protection scope of this utility model. Therefore, the protection scope of this utility model patent should be determined by the appended claims.

Claims

1. A gold plated cylinder structure, characterized by, include: The main channel has a channel on its outer wall, a central column inside the main channel, and a main channel wall on its upper surface. An inner anode mesh is disposed on the outer wall of the central column; An outer anode mesh is disposed on the inner side of the main tank wall; A secondary tank is connected to the outer wall of the main tank and communicates with the main tank via the channel. The volume ratio of the main tank to the secondary tank is 1:0.2 to 1:

1. The inner anode mesh and the outer anode mesh are used to output current to electroplate the product, the main tank is used to electroplate the product to be electroplated, and the volume ratio of the main tank to the auxiliary tank is used to improve the electroplating quality and the utilization efficiency of the electroplating solution.

2. The gold plated cartridge structure of claim 1, wherein, The volume ratio of the main tank to the secondary tank is 1:0.35 to 1:0.

65.

3. The gold plated cartridge structure of claim 1, wherein, The volume ratio of the main tank to the secondary tank is 1:0.2 to 1:0.

45.

4. The gold plated cartridge structure of claim 1, wherein, The volume ratio of the main tank to the secondary tank is 1:0.5 to 1:

1.

5. The gold plated cartridge structure of claim 1, wherein, The distance between the inner anode mesh and the outer anode mesh is 12cm to 26cm.

6. The gold plated can structure of claim 1, wherein, The distance between the inner anode mesh, the outer anode mesh and the product to be plated with gold is greater than 4 cm.

7. The gold plated can structure of claim 1, wherein The central column is located at the center of the main channel.

8. An electroplating apparatus characterized by comprising: Includes the gold-plated cylinder structure as described in any one of claims 1 to 7.

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