Microetch Neutralizer Chemistry For Ni-Au Plating Defect Elimination
20220074067 · 2022-03-10
Inventors
- Paul V. Pesavento (Hutchinson, MN, US)
- Douglas P. Riemer (Waconia, MN, US)
- David A. Brouchous (Hutchinson, MN, US)
Cpc classification
C25D5/12
CHEMISTRY; METALLURGY
International classification
Abstract
A neutralizing composition comprising ascorbic acid as a reducing agent, citric acid as a chelator and a pH adjusting agent applied to microetched copper substrates bussed to stainless steel, which have been cleaned with an agent comprising permanganate ions. Unlike the prior art neutralizing agents comprising oxalic acid, which leave insoluble residue on the surface of the copper substrate, the present neutralizing composition leaves no residue and acts quickly. A surprising reduction in defects of Ni—Au plated copper substrates is achieved by utilization of the neutralization composition in a manufacturing process.
Claims
1. A neutralizing composition comprising: a reducing agent, a chelator; and a pH adjuster.
2. The neutralizing composition of claim 1, wherein the reducing agent is a carbocyclic acid selected from the group consisting of tartaric acid, acetic acid, malic acid, malonic acid, ascorbic acid, lactic acid, succinic acid, and salts thereof.
3. The neutralizing composition of claim 1, wherein the chelator is comprised of citric acid, ethylene diamine tetra-acetic acid (EDTA), or other divalent cation chelator.
4. The neutralizing composition of claim 1, wherein the reducing agent is present in an amount in the range of 12-18 wt. %, the chelator in an amount in the range of 11-15 wt. %, and the pH adjuster in an amount to bring the pH of the composition to a pH of about 2.
5. The neutralizing composition of claim 4, wherein the pH adjuster is selected from the group consisting of sodium hydroxide, potassium hydroxide, and mixtures thereof.
6. The neutralizing composition of claim 1, wherein the reducing agent comprises ascorbic acid, the chelator comprises citric acid and the pH adjuster is selected from the group consisting of sodium hydroxide, potassium hydroxide, and mixtures thereof.
7. A composition comprising: ascorbic acid in an amount of 15 wt. %, citric acid in an amount of 12 wt. %, and sodium hydroxide in an amount sufficient to achieve a pH of the composition of about 2.
8. A process of finish plating a copper substrate bussed to stainless steel with at least one selected from the group consisting of nickel and gold, comprising: recovering a microetched copper substrate bussed to stainless steel; cleaning the copper substrate with an alkaline solution comprising permanganate ions; and contacting a neutralizing composition with the cleaned copper substrate, wherein the neutralizing composition comprises the composition of claim 1, and thereafter plating on the copper substrate at least one selected from the group consisting of nickel and gold.
9. A process of finish plating a copper substrate bussed to stainless steel with at least one selected from the group consisting of nickel and gold, comprising: recovering a microetched copper substrate bussed to a stainless steel; cleaning the copper substrate with an alkaline solution comprising permanganate ions; and contacting a neutralizing composition with the cleaned copper substrate, wherein the neutralizing composition comprises the composition of claim 4, and thereafter plating on the copper substrate at least one selected from the group consisting of nickel and gold.
10. A process of finish plating a copper substrate bussed to stainless steel with at least one selected from the group consisting of nickel and gold, comprising: recovering a microetched copper substrate bussed to a stainless steel; cleaning the copper substrate with an alkaline solution comprising permanganate ions; and contacting a neutralizing composition with the cleaned copper substrate, wherein the neutralizing composition comprises the composition of claim 7, and thereafter plating on the copper substrate at least one selected from the group consisting of nickel and gold.
11. The process of claim 10, wherein the contacting step is carried out at a temperature up to about 50° C.
12. The process of claim 11, wherein the contacting step does not exceed about 30 seconds.
13. The process of claim 12, wherein the contacting step is performed as a continuing process and further comprising performing the contacting step at a speed of 3 meters/minute.
14. The process of claim 10, wherein the permanganate is neutralized in about 1 second.
15. The process of claim 10, wherein nickel is plated directly on the copper substrate to form a nickel plating and the gold is plated on the nickel plating.
16. A process of finish plating a copper substrate bussed to stainless steel with a nickel plating, followed by a gold plating over the nickel plating, comprising: recovering a microetched copper substrate bussed to a stainless steel; cleaning the copper substrate with an alkaline solution comprising permanganate ions; and contacting a neutralizing composition with the cleaned copper substrate, wherein the neutralizing composition comprises ascorbic acid in an amount of 15 wt. %, citric acid in an amount of 12 wt. %, and sodium hydroxide in an amount sufficient to achieve a pH of the composition of about 2, and thereafter plating the nickel directly on the copper substrate and thereafter plating the gold on the nickel plating.
17. The process of claim 16, further comprising performing the contacting step at a temperature up to about 50° C. for a time of about 30 seconds.
18. The process of claim 16, wherein the step of contacting is performed continuously.
19. The process of claim 16, wherein the permanganate ions are neutralized in less than one second.
20. The process of claim 16, wherein yield loss in plating are reduced below 1%.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0014]
[0015]
[0016]
[0017]
[0018]
[0019]
DETAILED DESCRIPTION OF THE EMBODIMENTS
[0020] As shown in
[0021] While mineral acids have been used historically, the typical mineral acid process will etch away conductors on the stainless steel rendering it unsuitable, which has led to the use of organic acids. However, the typical organic acid, oxalic acid, forms insoluble salts as described above and thus is undesirable.
[0022] As shown in the schematic representation of
[0023] As shown in
[0024] Turning to the inventive neutralizer formulation or composition of the present disclosure, the composition is comprised of mild organic acids. Ascorbic acid, citric acid and a pH adjuster, such as sodium hydroxide, to control pH to about 2.0 can be used. The microetch process utilizes a cleaning agent to remove the soot, wherein the cleaning agent comprises permanganate ions. The neutralizer according to the present embodiments can neutralize the permanganate ions in about 1 second. The neutralizer composition of the present disclosure comprises a mild organic acid, such as a carboxylic acid selected from the group consisting of tartaric acid, acetic acid, malic acid, malonic acid, ascorbic acid, lactic acid, succinic acid, and salts thereof, a chelator, such as citric acid, and a pH adjusting agent, such as sodium hydroxide, potassium hydroxide and lithium hydroxide. Typically, sodium hydroxide, potassium hydroxide and mixtures thereof are used. Sodium hydroxide is preferred. As the mild organic acid can be used ascorbic acid, which acts as a reducing agent. As the chelator can be used citric acid, or equivalent. Adjustment of the pH by the base should be in an amount effective to bring the pH to about 2. The mild organic acid can be present in an amount of from 12 to 18 wt. %, the chelator can be present in an amount of from 11 to 15 wt. % and sufficient pH adjuster to bring the pH of the composition to about 2. In some embodiment, use of the formulation according to the present disclosure is carried out at temperatures up to and including 50° C. for a period of about 30 seconds. In other embodiments, use of the formulation according to the present disclosure is carried out at temperatures above 50° C. Conventional surfactants may be included in the compositions. Such surfactants include ionic, non-ionic and amphoteric surfactants. Among the ionic surfactant, cationic and anionic surfactants can be used. Mixtures of the surfactants can also be used. Surfactants may be included in the compositions in amounts between 0.001 g/L to 50 g/L.
[0025] The neutralizer formulation of the present disclosure permits much shorter processing times than were experienced by prior art formulations. The shorter processing times allowed by the chemistry of the formulations of the disclosure enable high manufacturing line throughput. Processing times of 30 seconds are attainable. The current state of the art utilizing organic acids, when processing at temperatures less than 50° C., require a minimum immersion time of 60 minutes which would not likely lend itself well to a continuous process, but rather would likely require a batch-based immersion tank. In contrast, the neutralizer composition of the present disclosure can effectively neutralize the permanganate ions present in the soot cleaning chemistry almost instantaneously, and within one second of contact, at temperatures of about 50° C. After neutralization, the copper substrate can be treated with plasma to further prepare the substrate for Ni—Au plating.
[0026]
EXAMPLE
[0027] The following example is provided for illustration purposes only and is not intended to limit the scope or teaching of the invention in any way.
[0028] A formulation of neutralizer comprising ascorbic acid as the reducing agent in an amount of 15 wt. %, a chelator comprising citric acid in an amount of about 12 wt. %, and sufficient base, such as sodium hydroxide, to adjust the pH to about 2, was made. In one example the formulation was heated to temperatures up to and including about 50° C. for a time of about 30 seconds to form a residue free copper surface and neutralizes permanganate from a chrome etch. It also conditions stainless steel for good passivation. Subsequent Ni—Au plating on the residue free copper surface results in defects less than 10%. When combined with a plasma treatment before plating, defects were reduced to less than 0.1%. When utilized in a continuous process, machine throughput was increased to 3 meters per minute.
[0029] While we have described certain embodiments, it should be understood that such embodiments are illustrative only and not limiting, as one of ordinary skill in the art, to which this disclosure is directed, will understand that other embodiments of this disclosure and modifications of the disclosed embodiments can be achieved without the exercise of invention.