Pulse-reverse electroplating of chromium from Sargent baths: Influence of anodic time on physical and electrochemical properties of electroplated Cr
Graphical abstract
Introduction
Chromium electroplating has been widely used for functional and decorative improvement of manufactured products in various fields because of its outstanding properties such as superior corrosion resistance, smooth surface, and high hardness [[1], [2], [3], [4], [5]]. Especially, its corrosion resistivity is extraordinarily higher than other commercial metals, which is attributed to the strongly passivated chromium surface in a form of chromium oxide, naturally formed in air [6]. In cases of other common metals, for example, iron, zinc, copper, and nikel, oxidized film also can be easily formed on their surface [7]. However, these metals tend to be oxidized partially and incompactly, allowing oxygen to penetrate into underlying metals and react with it continuously. On the contrary, the oxide layers on the chromium are so densely and compactly formed that the diffusion of oxygen is well blocked [8,9]. Moreover, passive film of chromium is highly stable in acidic condition.
However, in actual chromium electroplating process, the chromium coatings with excellent physical properties cannot be easily achieved due to the formation of cracks [1]. In general, electroplating of chromium from Cr6+ has been carried out by applying cathodic current, and an appropriate amount of sulfuric acid is added to obtain a bright chromium metal [[10], [11], [12], [13]]. Due to a high concentration of hydrogen ion in acidic electrolyte, a deposited crystal structure of chromium can be accompanied by numerous entangling of hydrogen atoms which leads to expansion of the chromium lattice and decrease in current efficiency during electrodeposition [14,15]. The entangled hydrogen escapes easily from the chromium lattice, leaving lots of vacancies. In this step, a tensile strain is generated to stabilize crystal structure, resulting in cracks on the deposit layer [2]. Consequently, a number of cracks on chromium coating caused by lattice contraction bring about decreases in originally desired properties, for examples, hardness, wear resistance, and especially corrosion resistance by facilitating infiltration of oxygen into underlying substrate [15,16].
Among the various electrochemical plating techniques, a promising candidate is pulse reverse (PR) electroplating to obtain crack-free chromium film [2]. The PR electroplating is a method to apply bipolar currents alternatively [14]. In this procedure, anodic current is used to re-oxidize hydrogen within deposited chromium layer through which the essential reason of cracks can be promptly eliminated [17]. In PR electroplating, there are several kinds of fabrication parameters, for examples, cathodic current density (ic), anodic current density (ia), cathodic pulse time (tc), anodic pulse time (ta), plating temperature and total passed charge [18,19]. In order to produce the electroplated film with a desired quality level in various applications, these process parameters need to be finely tuned to achieve desired properties [20,21]. Although significant progress has been accomplished in this field [2,22,23], the optimization of anodic time for PR electroplating is rarely reported. And the influence of electroplating conditions in case of PR process on film quality, such as crack density, film thickness, hardness, and corrosion behavior, has not been intensively studied.
In this study, physical properties and corrosion behavior of electroplated chromium were investigated with respect to variation of anodic pulse time in PR electroplating. Among four electrodeposition parameters (ic, tc, ia, and ta), we focus on anodic current time (ta) for PR electroplating to reduce cracks on chromium electroplating. The density of cracks, hardness, wear resistance and corrosion resistance could be controlled by anodic current time (ta). To the best of our knowledge, no previous study has been conducted to examine the mutual relationship between anodic current time in PR electroplating and the crack density of plated chromium. We clarified the correlation between effects of anodic pulses and physical properties of chromium film.
Section snippets
Electroplating method of chromium film
Electroplating was conducted with a three electrode system using a lead sheet (2 × 4 cm2) as a counter electrode and Ag/AgCl/KCl(3 M) electrode as a reference electrode. Ni-coated steel use stainless 304 (SUS304) plates were prepared as working electrodes for chromium electroplating in which electrode area was fixed as 2 × 2 cm2 and edge parts of specimens were insulated with polyimide film (Du Pont; Kapton). Prior to the electroplating process, all the substrates for electroplating were
Determination of cathodic current density for PR electroplating
PR electrodepositions were carried out under pulse-reverse current system comprised of cathodic pulses and anodic pulses using a Potentiostat (PGSTAT 128 N), as shown in Scheme 1. DC electroplating experiments were carried out to determine the adequate value of cathodic current density (ic) for PR electroplating. Only cathodic current was introduced for electrodeposition without any pulse current at current density of −0.1, −0.2, and −0.3 A cm−2, which was denoted as DC1, DC2, and DC3,
Conclusions
In summary, the anodic time, considered as the most important factor in PR electroplating, was controlled to identify various physical properties and corrosion resistance of Cr deposits. The increase of anodic time plays a significant role in reducing the crack density, but it also interferes with the uniform plating of the surface at long anodic time. The hardness and thickness of electrodeposited chromium was decreased with respect to an increase in anodic time for PR electroplating. The
Declaration of Competing interest
The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.
Acknowledgments
This work was supported by the National Research Foundation of Korea(NRF) Grant funded by the Korean Government(MSIP) (No. 2015R1A4A1042434) and by the Korea Institute of Energy Technology Evaluation and Planning(KETEP) and the Ministry of Trade, Industry & Energy(MOTIE) of the Republic of Korea (No. 20194030202340).
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