Patent Application
20090159452
1. Technical Field
The present invention generally relates to an electroplating method, and particularly, relates to an electroplating method for an insulative substrate.
2. Discussion of Related Art
Properties of carbon fibers such as high tensile strength, low weight, low thermal expansion, high electrical conductivity and heat conductivity make it very popular in many fields such as aerospace and motorsports. Generally, carbon fibers are widely employed in composite materials to improve performance thereof. For example, a copper-carbon fiber composite is disclosed in Keiidhi Kuniya et al. Development of Copper-Carbon Fiber Composite for Electrodes of Power Semiconductor Devices, IEEE Transactions on Components, Hybrids, and Manufacturing Technology, vol. 6, No. 4, pp. 467-472, Dec. 1983.
It is to be understood that in metal-carbon fiber composite, carbon fibers and metal cannot thoroughly soaked with each other due to the differences of surface properties. In order to improve a bonding between metal and carbon fibers, carbon fibers are usually pre-processed using electroless plating, electroplating, physical vapor deposition, or chemical vapor deposition. Electroplating is highly preferred for its simple process, low cost and high level plating layer.
Currently, carbon fibers are immersed in a plating bath and connected to an electrode during a plating process, a redox reaction occurs on surfaces of carbon fibers and plating layer is thereby deposited. However, a current distribution density is non-uniform on surfaces of carbon fibers; as a result, deposition speed of metal particles is also non-uniform. Specifically, the closer the carbon fibers are to the electrode, the higher the particles deposition speed. Therefore, the obtained plating layer is non-uniform, metal-carbon fiber composite made from such carbon fibers can't reach its expected performance. Therefore, there is a desire to develop a method of forming a uniform plating layer.
An electroplating method includes steps of: providing a substrate having a first portion and a second portion connected to the first portion; forming a metallic layer on a surface of the second portion; immersing the first portion of the substrate in an electrolyte solution, applying a current to the metallic layer to electroplate the first portion of the substrate with a metal layer; and moving the substrate in a direction away from the electrolyte solution during electroplating the first portion of the substrate.
This and other features and advantages of the present invention as well as the preferred embodiments thereof and an electroplating method in accordance with the invention will become apparent from the following detailed description and the descriptions of the drawings.
Many aspects of the present invention can be better understood with reference to the following drawings. The components in the drawings are not necessarily drawn to scale, the emphasis instead being placed upon clearly illustrating the principles of the present invention.
In step 1, as shown in
The substrate 100 is made of an dielectric material, for example, carbon fiber or plastic. Examples of plastic include polypropylene, polycarbonate, and copolymer of propylene, butadiene and styrene. Silks can be spun from above materials and the substrate 100 can be woven from the plastic silks. In the present embodiment, the substrate 100 is made of carbon fiber, and a thickness of the substrate 100 is in a range from about 1 micrometer to 100 micrometers. The substrate 100 is a rectangular shaped sheet. However, it is understood that the substrate 100 can also be threadlike or club-shaped. In order to remove dust and smear attached on the substrate 100, the substrate is processed using plasma or an acid solution.
In step 2, an metallic layer 200 is formed or disposed on a surface of the second portion 120. Referring to
In this embodiment, the substrate 100 is a carbon fiber cloth. The first portion 110 and the second portion 120 have a same width. Electrically conductive silver pastes are coated on entire surfaces 121, 122 and then cured, thereby forming the metallic layer 200. It is understood that other metals such as aurum, copper, nickel and aluminum can also be used to make electrically conductive pastes for the metallic layer 200. In addition, the metallic layer 200 can also be formed by laminating a layer of electrically conductive metal powder on the two surfaces 121, 122 or disposing sheet metals on the two surfaces 121, 122. Sheet metals are especially convenient when substrate 100 is threadlike shaped. In such condition, the substrate 100 can be clamped between two sheet metals.
In step 3, referring to
It is understood that pneumatic, fluid drive, or electric drive elevating apparatus can also be employed as the elevating means 431. In addition, both the cathode 410 and the substrate 100 can be connected to the elevating system 430. The elevating system 430 can directly control the movement of the substrate 100.
The process of depositing the plating layer 300 will be described in detail in the following context. Firstly, the metallic layer 200 is electrically connected to the cathode 410; secondly, the controller 432 controls the elevating means 431 to lower the second guide rail 4312 such that the first portion 110 of the substrate 100 is immersed in the plating bath 420; finally, the power supply is switched on, a redox reaction occurs on the two opposite surfaces 111, 112, and the plating layer 300 is thereby deposited. It is to be understood that side surfaces of the first portion 110 can also have plating layer 300 deposited thereon.
During the electroplating process, the controller 432 controls the elevating means 431 to elevate the second guide rail 4312 and the cathode 410, as a result, the substrate 100 is gradually pulled out of the plating bath 420. Therefore, plating time in different areas of the two opposite surfaces 111, 112 is different, specifically, plating time gradually increases from an end of the first portion 110 that adjacent to the second portion 120 (hereinafter as proximal end) to the opposite end (hereinafter as distal end). In contrast, a current distribution density gradually decreases from the proximal end to the distal end. The plating time and the current distribution density establish an equilibrium, and a uniform plating layer 300 can be obtained. In the present embodiment, the substrate 100 is elevated in a uniform motion. However, it is to be understood that the substrate 100 can be also elevated in a non-uniform motion.
When metal particles are deposited on the two opposite surfaces 111 and 112, the metal particles act as an assistant electrode which can accelerate the electroplating process and improve a uniformity of current distribution density. As a result, when the substrate 100 is pulled out of the plating bath 420, the controller 432 stops the second guide rail 4312, and the substrate 100 is removed from the second guide rail 4312 and dried, as a result, a substrate 100 with uniform plating layer 300 formed on the two opposite surfaces 111, 112 is obtained.
In order to further improve a thickness uniformity of the plating layer 300, the cathode 410 is connected to a current regulating apparatus (not shown) for regulating an output current of the cathode 410 such that current distribution density on the portion of the two opposite surfaces 111, 112 that are immersed in the plating bath 420 remain at a certain valve. For example, when the substrate 100 is elevated in a uniform motion at a velocity of v, cathode 410 has an initial output current of I0, and the first portion 100 has a length of L, the current regulating apparatus decreases the output current of the cathode 410 at an acceleration of ΔI wherein ΔI satisfy a equation of ΔI=vI0/L.
The second portion 120 and the metallic layer 200 can be removed according to a practical demand. For example, the substrate 100 can be cut along a boundary between the first portion 110 and the second portion 120 and the second portion 120 is removed. The remained first portion 110 has a very uniform plating layer 300.
In the present embodiment, a long contacting boundary exists between the metallic layer 200 and the first portion 110; as a result, uniformity of current distribution density in a width direction of the first portion 110 is improved and a deposition speed of plating layer 300 is substantially same in the width direction of the first portion 110. Furthermore, the substrate 100 is pulled out of the plating bath 420 gradually, the deposited metal particles on the two opposite surfaces 111, 112 act as assistant electrode which can improve a current distribution density of the portion of opposite surfaces 111, 112 immersed in the plating bath, as a result, a thickness of the plating layer 300 is further improved.
Finally, it is to be understood that the above-described embodiments are intended to illustrate rather than limit the invention. Variations may be made to the embodiments without departing from the spirit of the invention as claimed. The above-described embodiments illustrate the scope of the invention but do not restrict the scope of the invention.
| Number | Date | Country | Kind |
|---|---|---|---|
| 200710203211.5 | Dec 2007 | CN | national |
