Silicate glasses represent metastable materials that are susceptible to aqueous corrosion by atmospheric water vapor or liquid water in engineered environments and technological applications such as solar energy conversion systems1, pharmaceutical use2, and the immobilization of high-level nuclear waste from spent nuclear fuel3,4,5. Besides its role in the technological fields of application, natural volcanic glasses represent a major component of Earth's exposed surface and are thus involved in global biogeochemical cycles and the evolution of long-term climate6,7. The atmospheric alteration by water vapor is a key factor in both technological applications and natural environments.Distinguishing this effect from that of the alteration by liquid water is important as the surface-to-volume (S/V) ratio of glass to solution is significantly different8,9. The present work, however, focuses on the corrosion behavior of silicate glass in liquid water. When a glass comes in contact with an aqueous solution, a number of coupled reaction and transport processes occur at the glass/water interface, generally forming a structurally complex surface alteration layer (SAL). However, the mechanisms, kinetics, and rate-limiting factors of silicate glass corrosion are still a matter of intensive debate, reflected by the existence of various corrosion models5,10,11,12,13. Therefore, understanding the complex interplay between reaction and transport processes at the glass/water interface in time and space and at a microscopic level is fundamental for the development of analytical and numerical models predicting the long-term silicate glass corrosion14.
One widely accepted model presumes that the SAL forms by volume interdiffusion of hydronium from the solution into the glass and network modifiers from the glass into the solution (leaching), whereby silanol groups form by the exchange with the cations15,16. In the course of the reaction, it is assumed that the silanol groups recombine, releasing molecular water by forming new siloxane bonds and eventually leaving behind a porous residual silica-rich SAL (Figure 1A). However, experimental results obtained by atom probe tomography and transmission electron microscopy revealed an atomically sharp interface between the glass and the SAL14,17,18, which contradicts a diffusion-controlled process. In addition, new results of isotope tracer experiments are not consistent with a leaching model19,20. Instead, such observations can be explained by the interface-coupled dissolution-precipitation (ICDP) model that is based on a stoichiometric dissolution of the glass spatially and temporally coupled to the precipitation of amorphous silica once a solution boundary layer at the glass surface is supersaturated with respect to silica 5,21,22. Recently, the ICDP model has been expanded to include an ion exchange zone that may evolve ahead of an ICDP front if the dissolution-precipitation rate slows down dramatically23 (Figure 1B). For a more detailed review of further models considering the formation of SAL, refer to the PhD thesis of M. Fritzsche24.
Commonly performed corrosion experiments follow a multi-step workflow, including the alteration experiment itself, quenching (rapid cooling), drying, sawing, and polishing of the altered glass sample for postmortem analysis15,19. This, however, is critical as it may change the structural and chemical properties of the main corrosion product, i.e., the hydrous amorphous silica-based SAL, due to condensation and/or polymerization, loss of water (dehydration) and/or cracking and flacking15,19,25. In chemically complex systems (multicomponent glasses and solutions), quenching and drying of the sample may also induce the precipitation of secondary minerals that are not involved in the reaction itself. Besides this, a quenched sample represents only one point in time of the glass corrosion process, requiring a high effort to derive glass dissolution rates and information about the reaction mechanism(s) from multiple quench experiments26. Therefore, most glass corrosion kinetic data obtained during glass corrosion experiments from aliquot analyses of the bulk solution are less informative for studying the reaction mechanisms and accompanying transport processes during silicate glass corrosion.
To overcome the disadvantages of ex situ experiments, including sample preparation and post mortem analysis, in situ techniques have gained increasing interest over the past years27,28. For instance, atomic force microscopy (AFM) and vertical scanning interferometry (VSI) became vital tools to study mineral surfaces that are in direct contact with aqueous solution27,29. However, both approaches are limited to studying the very first steps of a corrosion process, i.e., until a secondary layer has formed that impedes the investigation of the glass/SAL interface28,30. Fluid-cell Raman spectroscopy (FCRS) overcomes the aforementioned shortcomings by providing real-time and space-resolved (operando) observations of reaction and transport processes at solid/solution interfaces at a microscopic scale and at elevated temperatures if the parent and product phase(s) are transparent to visible light (Figure 2). First FCRS studies were conducted by Geisler et al.5, who investigated the aqueous corrosion behavior of ternary borosilicate glass (TBG) in a 0.5 M NaHCO3 solution, i.e., under near-neutral pH conditions at 85 °C. The formation of a water-rich zone between the SAL and pristine glass was observed, an intrinsic feature of the ICDP model. By using a bicarbonate solution, pH gradients at the glass surface and within the SAL could also be detected by estimating the local pH from the intensity ratio of the carbonate and bicarbonate band (c.f.5). Moreover, without disturbing the ongoing corrosion process, an exchange with a deuterated solution showed that the transport of water through the SAL was not a rate-limiting step for the corrosion process. In summary, this work showcased the strength of FCRS to identify key reaction mechanisms and feedback on transport phenomena within a single experiment under well-controlled conditions.
Subsequent FCRS experiments have further demonstrated that this method is suitable for routine use, producing consistent and reproducible results24,31,32. For instance, FCRS was applied to study the effect of heavy ion irradiation on the forward dissolution rate of borosilicate glasses, showing a significant increase in the forward dissolution rate by a factor of 3.7 ± 0.531. Moreover, FCRS experiments conducted with a Ba-bearing, soda-lime boroaluminosilicate glass in a hyperalkaline solution documented operando the direct transformation of the glass into Mg-clay, zeolite, and carbonates. These authors found a decrease in the initial glass dissolution rate, the magnitude of which appears to be related to the composition and structure of the alteration layer33. Moreover, changes in the shape of the convoluted water band were used to monitor ionic strength operando, revealing rhythmic fluctuations32. Sulzbach and Geisler34 performed FCRS experiments to study the replacement of celestine (SrSO4) by strontianite (SrCO3), both transparent to visible light, in a carbonate solution, which provided new details about an ICDP mechanism and gave the first evidence for three kinetic regimes. Recently, as part of a doctoral thesis24, the experimental setup was extended to include an external heating station, facilitating long-term studies over several months with glasses of higher durability, such as the six-component International Simple Glass (ISG)14,24. For this, the fluid cell was stored on the heating station between consecutive Raman measurements to avoid blocking the Raman spectrometer for several months. In addition, flow-through experiments were conducted by connecting the fluid cell to a syringe pump. This approach effectively prevented the precipitation of silica, which allowed the measurement of forward dissolution rates under turbulent flow conditions (Fritzsche24).
In general, FCRS provides a novel approach for studying coupled mechanisms of reactions and mass transfer occurring at solid-water interfaces, overcoming the shortcomings of commonly applied ex situ experiments. It is readily expandable to accommodate a wide range of samples and conditions. The aim of this article is to share the technical and experimental details of Fluid-cell Raman spectroscopy, exemplified by a corrosion experiment with a ternary borosilicate glass (TBG) and a 0.5 M NaHCO3 solution at a nominal temperature of 90 °C. The protocol will cover the sample preparation, the assembly of the fluid cell, and the setting of the measurement conditions at the Raman spectrometer. For determining the glass retreat rate, potential pH gradient, and the local temperature the authors refer to the study of Geisler et al.5 and Sulzbach and Geisler34 plus supplementary material and the doctoral thesis of Dohmen35 and Fritzsche24. Critical steps in setting up the experiment, such as filling and closing the cell, will be covered with additional advice on how to avoid repeating the pitfalls of previous work. This article provides a comprehensive overview of the technique, facilitating its implementation by newcomers to the field and contributing to the advancement of research in solid-fluid interaction.