Abstract
The corrosion and degradation of materials, such as pipeline steel, have a strong effect on both the environment and the economy. The quantification of these processes can therefore provide important information needed to manage their impact. In this study, a concept for the characterization and quantification of corrosion is demonstrated on API X70 steel immersed in 3.5 wt.% NaCl solution. Due to the difficulty of quantifying corrosion rates, e.g., through single mean values, a unique system is applied that directly couples Raman spectroscopy with vertical scanning interferometry to assess the physical and chemical aspects of steel corrosion kinetics. Vertical scanning interferometry allows the quantification of the topographical evolution of corrosion product formation and material dissolution in combination with the direct measurements of the respective rates. The Raman spectroscopy provides additional information about the (mineral) phases. Rate variations ranging from uniform corrosion to areas of high pit densities are quantified and analyzed in rate maps and subsequently visualized in rate spectra. The rate distribution is classified into different domains and pitting rates. Thus, a comprehensive quantitative assessment of the characteristic corrosion behavior is discussed.
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Introduction
Modern industrial societies must invest a significant amount of the national gross product to maintain their infrastructure and fight its corrosion. The lifetime and velocity of degradation of solid material is a major concern to engineers, researchers, managers, and politicians. The corrosion of pipelines is a particularly important economical factor for the oil and gas industry where costs can easily exceed billions of dollars each year.1 Furthermore, material failure can result in pipeline leakages with substantial environmental impact. These facts are strong arguments for intense research efforts that have led to a wealth of information and knowledge about corrosion.2,3,4,5,6,7,8,9
In the field of geochemistry, Luttge and co-workers10,11,12 have demonstrated that mineral dissolution rates may vary significantly. This variation depends on specific characteristics related to intrinsic properties of solid materials, such as crystal lattice defects.10,11 In many cases, this work created some serious doubt about the validity of using simple mean values, i.e., rate constants. Alternatively, the reaction behavior of a dissolving mineral surface can be quantified by measuring topography changes.10 The surface normal retreat is obtained by measuring the local height development in a series of time frames and subtracting these from each other, hereby generating a material flux map.12 These surface normal retreat values are then converted into reaction rates that can be visualized in a rate map. Finally, the rate distribution is analyzed in a histogram, termed a rate spectrum.12 Through deconvolution of the rate spectra different rate contributing modes are revealed, providing a statistical approach to reaction rates and serving as a basis for mechanistic interpretion.10
In the case of steel, metal “dissolution” occurs as part of the corrosion process. Many different rate contributing factors have to be taken into consideration, as different compositional and microstructural properties can lead to significant corrosion rate variations (e.g., 0.8 mm year−1 to 3.2 mm year−1).13 Particularly pitting corrosion shows accelerated dissolution5 due to chemical or physical heterogeneities2 (Fig. 1).
Previous studies have utilized interferometry to assess corrosion behavior.14,15,16 These studies show the powerful capabilities of characterizing pitting corrosion, e.g., pit density and pit geometry14,16 as well as uniform corrosion.15 In this study, the characterization of uniform and localized corrosion is demonstrated, by quantifying the relationship between the corrosion products on the surface and the steel dissolution underneath. Methods of previous studies such as the measurements of surface topography after cleaning off the corrosion products are incorporated.15 This allows the generation of rate and corrosion product maps that are further quantified via the rate spectra concept.10,11,12
The corrosion kinetics are studied with a new surface sensitive measuring method, Raman spectroscopy-coupled vertical scanning interferometry (RC-VSI). This setup has the capacity of linking precise centimeter to nanometer scale surface topographic measurements with the mineral or material phases and alterations that occur at the reacting surface. This information adds significantly to a wide range of possibilities that allow a comprehensive quantitative description of corrosion behavior.
The RC-VSI system enables direct overlay of Raman spectroscopy maps and surface topography maps. Subsequently, rate maps are produced by subtracting consecutive topography maps. Finally, through data processing, rate maps are directly correlated with Raman spectroscopy maps. This procedure generates a direct correlation between surface reaction rates and composition. This work demonstrates a concept that can give insight into steel corrosion kinetics and provide quantification of corrosion rates via topography measurements with up to nanometer scale vertical resolution.
Below, the utilization of the previously outlined method is tested on API X70 pipeline steel undergoing corrosion in an NaCl solution.
Results
Topography observations
The initially polished surface was measured by vertical scanning interferometry (VSI). Minor scratches ranging from 1 to 3 µm in depth are observed (Fig. 2, A1−C1). The quantification of surface roughness was done by using two roughness parameters, i.e., the roughness average (Ra), which is the average mean height, and the root mean square (Rq), which describes the standard deviation from the mean height. All three samples initially show very low roughness values due to the polishing procedure, i.e., Ra = 63 nm and Rq = 87 nm (Table 1).
Conducting the corrosion experiment, after a time interval of 5 h in 3.5 wt.% NaCl solution, the topography data show that more than half of the initial surface is covered with a layer of corrosion products. These products have a grain-like texture (Fig. 2, A2−C2). The border between the corrosion products and the bare steel surface is visible (Fig. 2, A2−C2). As explained in the method section (Fig. 6 (2)) all height data reported are initially apparent height values because they are measured using the embedding material as a reference. Only after the corrosion products have been removed with Clarke’s solution the absolute corrosion product height and volume can be determined. The same applies for the quantification of surface-normal retreat rates.
After 5 h the apparent height of the corrosion products averages at around 10 µm, with a maximum of 25 µm. The border between the corrosion products and the steel surface has a curved shape, seen in sample C (Fig. 2, C2). Different morphologies of the corrosion products are observed: In sample A the corrosion products have formed an oval shape in the upper middle center (Fig. 2, A2), while products in sample B show smaller circular shapes with height values of 25 µm that are distributed across the surface (Fig. 2, B2).
The roughness analyses (Table 1) provide further quantification of the surface alteration. After 5 h of immersion the surface roughness values increase significantly to Ra = 6354 nm and Rq = 7828 nm due to the formation of the corrosion products.
After 72 h of immersion in the NaCl solution (Fig. 2, A3−C3), the corrosion products reside on the outer perimeters of the samples reaching heights of over 100 µm. Whereas in the center substantial lower height values and even negative height values are measured revealing the dissolution of the steel surface. Sample C (Fig. 2, C3) exhibits a different pattern as the height values are distributed rather homogenously across the surface reaching up to 140 µm and only two smaller areas of low and negative height values are present. The corrosion products formed after 72 h of immersion cause an increase in surface roughness values that are over 400 times higher than the initial polished surface’s roughness, with values of Rq = 24,697 nm and Ra = 29,210 nm (Table 1).
The circular formations observed after the first 5 h (Fig. 2, A2−C2) disappear largely after 72 h. Instead, pit areas with negative height values are now revealed (Fig. 2, A3−C3). The Raman spectrometer coupled with the VSI instrument is then used to analyze the corrosion products. As an example Fig. 2, B3 shows an area of a Raman measurement located at pit on the surface of sample B (Fig. 2, B3). These pits become even more pronounced after cleaning off all corrosion products (Fig. 2, A4−B4) and are documented in more detail in the rate maps section.
Raman spectroscopy-coupled vertical scanning interferometry—measurements (R-VSI)
Before cleaning off the corrosion products, Raman measurements (Fig. 3) of the area indicated in Fig. 2 (B3) were performed. A light optical microscope image (Fig. 3, (2)) shows the different coloring of corrosion products surrounding the pit ranging from red, orange to black. The corresponding Raman map shows the intensity of the 670 cm−1 vibrational band.
Strong Raman bands at 253, 380, 529, 658, and 1305 cm−1 are found surrounding the right side of the pit (Fig. 3, (3)) and are identified as lepidocrocite (see Methods for description of identification). Whereas a strong vibrational band at 673 cm−1 and small bands at 244, 314, and 543 cm−1, that correspond to magnetite, are located mainly in middle of the pit (Fig. 3, (4)). The rest of the area was identified as a mixture of Fe-hydroxides and oxides. The topography (Fig. 3, (5)) resembles the shape found in the Raman map as well as in the light microscope image. In close vicinity to the deep pit center an oval heightened hill gives the pit its characteristic shape. The majority of the pit is covered by corrosion products, only after cleaning them off two small pits are revealed (Fig. 3, (6)). Converting the surface normal retreat data into rates demonstrates the corrosive power of up to 2.5 mm year−1. Areas of low corrosion rates correspond to areas of high oxide/hydroxide heights. This resembles the typical anodic−cathodic electrochemical kinetics, which are discussed later on.
Rate maps and rate spectra
After 72 h of experimental runtime all corrosion products were cleaned off with Clarke’s solution, revealing the material damage through the corrosion process. Large areas of the surface have been dissolved causing a surface normal retreat (Table 1) ranging from 0 to 25 µm. This measured surface normal retreat is converted into corrosion rates of up to 3.5 mm year−1 (e.g., see ref. 17). The outer edges of the samples, where the majority of the corrosion products were found (Fig. 2, A3−C3), have nearly no surface normal retreat (~2 µm (0.25 mm year−1)). Whereas majority of the region in the middle of the samples have around 9 µm retreat (=1.2 mm year−1). The characteristic appearance of the rate maps is seen more clearly in the histogram of the rate distribution, known as rate spectrum. The spectra of all three samples show two major peaks (Fig. 4, (4)). Therefore, the deconvolution of the rate spectrum results in two Gaussian curves which quantify two characteristic corrosion domains, one at relatively low and one at relatively high corrosion rates. The centers of the Gaussian curves and their half width at half maximum (HWHM) are listed in Table 1. These values quantify the rate behavior seen in the rate maps.
Sample A (Fig. 4, (1)) has a region with high corrosion rates in the upper area. The cross-section of this region (Fig. 4, (5)) exposes three pits forming the rectangular shape with a dominant deep pit reaching a surface normal retreat of 29 µm (=3.94 mm year−1).
Likewise, sample B exhibits pits, yet these are rather dispersed throughout the surface. The pits can be linked to the circular corrosion product shapes found in Fig. 2 (B3). Their corrosion reaches surface normal retreat values of up to 21 µm (=2.94 mm year−1). Sample C shows no pits and has a rather uniform corrosion behavior with a retreat of 14 µm (=2 mm year−1) covering a large part of the sample surface. This results in a more flattened rate distribution of domain 2 (Fig. 4, (4)) leading to a high HWHM of 0.52 mm year−1 (Table 1).
The mean rate of 0.79 mm year−1 is found between the two domains.
In addition, the pitting impact can be determined by the ratio of pitting corrosion rate to total corrosion rate across the entire sample (Table 1). The highest pitting impact has sample A with 2.44%. The amount of steel material loss can be quantified via the cleaned topography and can then be calculated into material loss per area showing an average of 11.01E-3 mm3mm−2 (see Table 1 for more information).
Corrosion product topography maps and height distribution
Figure 5 (1)−(3) display the maps of the absolute height distribution. These data determine the distance between the corroded steel surface and the corrosion products after 72 h of immersion in NaCl (see Methods) and allow the quantification of the volume. Sample C has a volume of 10.17E-2 mm3mm−2 while the average is only 8.37E-2 mm3mm−2.
Similar to the corrosion rate distribution, the absolute heights can be visualized in a corrosion product histogram. This shows a different shape than the rate spectra and resembles a rather continuous decrease as the absolute height increases. The deconvolution by Gaussian curves delivers no proper quantification; further research is here necessary. In correlation to the observed uniform corrosion in sample C the absolute height distribution shows a high frequency between 60 and 100 µm, following an exponential decrease till 140 µm. Whereas the other two samples A and B reach a maximum at 100−120 µm (Fig. 5, (4))).
Strong metal dissolution tends to occur at locations of low absolute heights. This demonstrates the spatial electrochemical behavior of steel corrosion.
Discussion
The lifetime of a material is difficult to predict as lab experiments cannot consider all environmental factors, yet even relatively simple experiments are of a complex nature as seen here. The quantification of these processes results in a heterogeneous distribution of values. Taking a simple mean may give a broad overview, yet often fails to describe important details and may even present a rate result that does not exist (see Fig. 4). For example, the mean surface roughness parameters taken from the entire steel surface illustrate the alteration of steel corrosion by increasing its surface roughness from initially Rq = 64 nm to Rq = 4947 nm (for sample C cleaned with Clarke’s solution, Table 1). While samples A and B show a similar increase in surface roughness, the deep pits of up to 28.76 µm (Table 1) are not described by these mean roughness values. A convergence analysis could assess representable roughness values.18
Mean values require a normal distribution; however, this normal distribution is often not realized. Our alternative concept considers the entire rate spectrum, i.e., the spatial distribution of all rates measured on a representative section of the corroding steel surface. The principle of our approach and measurement techniques are demonstrated in this paper by conducting a 72 h long experiment. For real corrosion systems the run duration may be significantly longer depending on system parameters such as temperature, pH, steel material and solution composition.19
Due to the rate distribution a mean value may overlook the damaging effect of locally constrained high corrosion rates. Consider a pipeline wall thickness of 17.5 mm,20 using the maximum pitting rate of 3.94 mm year−1 observed here, a pipeline failure could occur already after ~4−5 years. The mean rate (0.79 mm year−1) would suggest a lifetime of ~21 years.
In this study a concept derived from mineralogical applications10,11 that assesses the rate distribution via rate maps and rate spectra is presented, thus, providing an extensive description of the complex corrosion behavior. The rate distribution ranges from two major rate contributing domains 0.25 ± 0.21 and 1.21 ± 0.32 mm year−1 (Fig. 4, (4)) to a maximum pitting rate of 3.44 mm year−1 (Table 1). This provides a more comprehensive description than a single mean corrosion rate of 0.79 mm year−1 (Table 1).
The rates are derived from a short-term exposure time of 72 h. Therefore, the calculated rates mainly demonstrate the principles of this new concept. In any case, they are relevant for the initial corrosion behavior of the system. In order to determine the actual long-term behavior of a material, longer immersion times may be advised because corrosion kinetics may be subject to change as a function of time.9,19,21,22 Pit stability is hereby an important aspect since pitting does not occur at a linear constant rate2 and tends to have a maximum lifetime.23 Corrosion product formation is also a dynamic process. In accordance with other studies24 after 5 h immersion a significant corrosion product layer is found on the pits (Fig. 2, (A2−C2)). After 72 h the majority has dissolved at these locations (Fig. 2, (A3−C3)).
The corrosion products on the surface influence the steel dissolution underneath.25,26 The RC-VSI is capable of delivering insight into the relationship between metal dissolution and corrosion product formation. The findings represented here are in agreement with other studies27 as Fe-oxides, e.g., magnetite, are found in close vicinity to the dissolving pit center, whereas Fe-hydroxides, e.g., lepidocrocite are found only in a distance from the pits (e.g., Fig. 3).
Pits can take on irregular localized behavior5,6,28 where e.g. micro pits join up to form macro pits,29 as seen in sample A (Fig. 4, (1), (5)). The occurrence of high reactive sites in close proximity present a potential weakness in the material, which can lead to degradation faster than predicted by the overall mean rate. This is particularly true in the perspective of real-world applications, where pressure, mechanical forces,30 and microbial corrosion31,32 can have an additional negative effect. The direct combination of rate maps with Raman spectroscopy maps is a powerful tool in future applications giving the possibility of precisely quantifying such heterogeneously distributed surface reactions.
The RC-VSI measurements and data processing provides a wealth of information about the corrosion process, yet limitations exist. The orthogonal white light beam of the VSI allows only surface normal pit depth measurements. If the pit grows under the surface, as seen in crevice corrosion, this method would not be able to detect the underlying dissolution. Further evaluation with e.g. µ-CT would be necessary to determine the true pit shape.
The corrosion product volume method presented here measures only the surface topography. Therefore, it is not possible to evaluate the density of the corrosion products and possible voids or air bubbles that may exist beneath the surface. This might explain the low ratio of steel material lost to corrosion product volume determined here (Table 1).
When cleaning off the corrosion products with Clarke’s solution, due to the HCl, small amounts of steel are dissolved.33,34 This can lead to a slight increase in the rate provided in domain 1. Using the presented method additional research is necessary to assess the effect of Clarke’s solution on the corrosion rates.
The introduction of RC-VSI enables the quantification of corrosion rates and analyses of corrosion products. Specifically, the method provides spatially resolved steel corrosion maps (rate maps), corrosion product maps, and Raman spectroscopy maps. The combination of these data generates insight in reaction mechanism(s) and kinetics in this way. Here, the surface of the corroding steel shows an inhomogeneous distribution of the corrosion processes. Therefore, simple mean values, rate constants, derived for the bulk material are not an adequate representation of the spectrum of corrosion rates. Instead, a concept is proposed and tested that is based on the measuring of the corroding surface topographies and the subsequent generation of rate maps leading finally to the desired rate spectra. This method provides a comprehensive quantification of reaction kinetics, i.e., corrosion behavior. In contrast to the conventional rate constant, rate spectra represent a new tool for an overall material characteristic quantification: the classification of the frequencies of corrosion rate occurrence with the potential of analyzing the individual rate modes and their contributions to the overall rate.
Methods
Three API X70 steel samples were embedded into one sample holder with polymethylmethacrylate (PMMA) and polished with a 3 µm diamond suspension. The ex situ immersion experiments were performed at room temperature (21 °C) for 72 h, in a 1 L NaCl (3.5 wt.%) solution with pH of 6. After immersion, the corrosion products were cleaned off with Clarke’s solution (100 ml HCl, 2 g Sb2O3 and 5 g SnCl2), uncovering the corroded steel surface. To minimize further corrosion, the immersion time in the Clarke’s solution was only 3 min and done in an ultra-sonic bath34.
In order to evaluate the corrosion behavior as a function of time, two measurement periods of 5 and 72 h were taken. The corrosion products were cleaned off after 72 h with Clarke’s solution and then measured with the VSI. All topography measurements were performed by a Bruker GT vertical scanning interferometer (VSI) in white light mode with a vertical resolution up to the Ångstrom level. This method has been described in detail.10,17,35,36 The measurements were performed with a ×5 objective, with a measurement area of x = 952.4 µm, y = 714.3 µm and a lateral sampling of 0.744 µm. The measurements were stitched together (also known as tiling). The initial roughness (before corrosion) of the samples was calculated using SPIP classic parameters (subtraction from mean). The roughness average Ra and root mean square Rq represent the mean surface roughness of the entire steel surface.
The interferometer is coupled to a Raman spectrometer from Renishaw and is equipped with a 532 nm laser (Fig. 6, (1)). The coordinates of the VSI measurements are calculated into the Raman coordinates thereby linking the spatially resolved height distribution directly to the chemical information of the corrosion products. The laser power for the measurements was 1.2 mW. The Renishaw database was used for identification of the spectra; further confirmation was achieved by the RRUFF database and other studies.27 The topography data were evaluated with SPIP (Imagemet) software. Surface normal retreat is calculated by subtracting the topography maps of the initial and corroded steel surface (Fig. 6, (2)) thereby generating a material flux map. Hereby, the PMMA is set to a constant height of zero and serves as a reference height and is also used as a baseline for the maximum pitting depth measurements (Fig. 6, (2)). The alignment of the individual measurements was done by characteristic surface features found on the PMMA. The subtraction of different topographies delivers various quantification (Fig. 6 (2)). The material flux maps, that show the surface normal retreat, can then be calculated into rate maps by taking the reaction time into consideration. These rate maps visualize the rate distribution10,11 across the surface. Furthermore, the frequency of surface normal retreat rate occurrences can be shown in a histogram, i.e., in a frequency spectrum. Rate domains and mechanisms are distinguished by deconvoluting the histogram into different normal type curves. This final histogram is termed as rate spectrum.11
The absolute corrosion product volume can be obtained adding up all the absolute height values. In the same procedure the surface normal retreat values yield the volume of steel material lost.
Data availability
The raw data presented in this study are available from the PANGAEA database. Processed data can also be obtained from the corresponding author upon reasonable request.
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Acknowledgements
Hereby we would like to thank Ricarda D. Rohlfs, Elisabete Trindade Pedrosa, Malte Bahro, Inna Kurganskaya, Till Bollermann, and Mohammad Khalid Bin Mahbub for fruitful discussions and advice. A special thanks to our technician Marcos Toro assisting the measurements. We gratefully acknowledge support from sponsors that have funded our work: The Deutsche Forschungsgemeinschaft (DFG) INST 144/378-1, and INST 144/388-1
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J.H. and A.L. designed the research; J.H. performed the research; J.H. analyzed the data; and J.H. and A.L. wrote the paper.
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Heuer, J., Luttge, A. Kinetics of pipeline steel corrosion studied by Raman spectroscopy-coupled vertical scanning interferometry. npj Mater Degrad 2, 40 (2018). https://doi.org/10.1038/s41529-018-0061-2
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DOI: https://doi.org/10.1038/s41529-018-0061-2