Abstract
In this work, we have studied tin electrodeposition on polycrystalline gold electrodes from two different supporting electrolytes: sulfuric acid (SA) and methanesulfonic acid (MSA), both of them commonly used in the industry. This work aims to understand the effect of the different electrolyte anions on the deposition process. We show at least three different tin deposition mechanisms on gold: irreversible adsorption, underpotential deposition, and overpotential (bulk) deposition. Underpotential deposition leads to the formation of a layer of tin in SA and MSA with a coverage around ML (monolayer) and ML, respectively. The UPD Sn layer is however somewhat uncharacteristic as it is associated with island formation and surface alloying. Cyclic voltammograms in an extended potential range showed five distinct peaks: two cathodic peaks associated with tin underpotential and overpotential deposition, and three main anodic peaks, corresponding to the oxidation of the bulk Sn, of the AuSn intermetallic layer, and of the adsorbed Sn(II) to Sn(IV). Both voltammetric and rotating disk electrode measurements show that the kinetics of tin electrodeposition in MSA is slower than in SA, which we ascribe to Sn-MSA complex formation in solution. Slow Sn deposition in MSA promotes AuSn formation, in contrast to SA in which bulk tin deposition is more prominent. Complete Levich-type mass transport control of tin deposition in SA and MSA was only reached at low scan rate due to concurrent HER on the uncovered gold surface during the deposition process at higher scan rates. An unexpected surface-confined passivation process is observed in both electrolytes.
Highlights
Tin electrodeposition has become one of the most popular surface coating processes due to several applications in different industrial sectors, such as packaging, microelectronics, automotive and industrial, jewelry and other decorative purposes, batteries for electrochemical storage, amongst many others.[1]
Our study aims at investigating how the tin electrodeposition process on a model gold electrode surface differs between these two acidic electrolyte solutions, in order to understand in more detail the effect of the methanesulfonic acid (MSA) electrolyte
Tin underpotential and overpotential deposition and tin stripping.—Figure 1 shows a comparison of the cyclic voltammograms (CV) of gold in sulfuric, methanesulfonic and perchloric acid in an extended potential region, including the Hydrogen Evolution Reaction (HER)
Summary
Tin electrodeposition has become one of the most popular surface coating processes due to several applications in different industrial sectors, such as packaging, microelectronics, automotive and industrial, jewelry and other decorative purposes, batteries for electrochemical storage, amongst many others.[1] Tin electroplating offers many important properties to the substrate because of its good wettability, solderability and compatibility It is one of the few metals that is suitable for being in contact with food and chemical products. Methanesulfonic acid presents an excellent metal salt solubility, high conductivity, stability, wide operating window,[18] a relatively low toxicity and good biodegradability.[3] Our study aims at investigating how the tin electrodeposition process on a model gold electrode surface differs between these two acidic electrolyte solutions, in order to understand in more detail the effect of the MSA electrolyte. Reference electrode was in contact with the electrolyte via a Luggin capillary; the gap between the RE Luggin capillary and the working electrode is about 2 cm
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