Mariella Malefioudakia,
Archismita Misra
c,
Nadja Sbeityc,
Juan Zueco-Vincelle
a,
Miguel A. Laguna-Bercero
a,
Andrea Koerdt
*c,
Rafael Martín-Rapún
ab and
Scott G. Mitchell
*ab
aInstituto de Nanociencia y Materiales de Aragón (INMA-CSIC/UNIZAR), CSIC-Universidad de Zaragoza, C/Pedro Cerbuna 12, 50009 Zaragoza, Spain. E-mail: scott.mitchell@csic.es
bCIBER de Bioingeniería, Biomateriales y Nanomedicina, Instituto de Salud Carlos III, 28029 Madrid, Spain
cBundesanstalt für Materialforschung und -prüfung (BAM), Department of Materials and Environment, Unter den Eichen 87, 12205 Berlin, Germany
First published on 8th May 2025
Corrosion of metals and other materials in marine environments poses significant economic, operational, safety, and environmental challenges across the oil and gas industry, the renewable energy sector, and maritime infrastructure. Microbiologically influenced corrosion (MIC) accounts for a substantial portion of this corrosion, with sulfate-reducing bacteria (SRB) and methanogenic archaea (MA) being key contributors. Conventional methods such as cathodic polarization have proven insufficient in mitigating the colonization of corrosive microbial communities in real marine environments, requiring the development of alternative, broad-spectrum antimicrobial strategies to prevent such biofilm formation. Recently, molybdate has emerged as a potential alternative to traditional biocides and nitrate. Our hypothesis is polyoxometalate-ionic liquids (POM-ILs), which exhibit antimicrobial and anticorrosion properties, could have a broader spectrum of antimicrobial activity than demonstrated until now and could be capable of shielding and protecting sensitive metal surfaces from the extreme acidic environments produced by MIC microorganisms. Here we show how two prototype polyoxomolybdate-based POM-ILs, [(CH3(CH2)6)4N]2[Mo6O19] and [(CH3(CH2)6)4N]4[Mo8O26], demonstrated antimicrobial activity at microgram per millilitre concentrations, prevented biofilm formation on metal surfaces, and provided resistance to corrosive acidic environments. Furthermore, impedance measurements were commensurate with electron microscopy studies showing that POM-IL-coated brass coupons withstood extremely corrosive environments. These proof-of-concept results demonstrate how multi-functional POM-IL coatings represent promising MIC mitigation solutions by providing a hydrophobic acid-resistant and biocidal protective layer that prevents biocolonisation and acidic corrosion by MIC microorganisms.
New conceptsThis study reports the deployment of polyoxometalate-ionic liquids (POM-ILs) as novel multifunctional coatings to mitigate microbiologically influenced corrosion (MIC) of metal substrates. The results herein demonstrate how the cross-species antimicrobial activity of POM-ILs combined with their unique adaptable anticorrosive activity creates dual-action water-insoluble coatings that prevent microbial biofilm formation and protects metal surfaces from corrosion. Unlike traditional methods like cathodic polarization or chemical inhibitors which fail to address the complex interplay of microbial activity and corrosion in dynamic environments, POM-ILs offer robust corrosion protection in extreme highly acidic environments over several months. The exceptional protection they offer to metal surfaces is demonstrated by their ability to preserve brass alloy integrity under extreme corrosive conditions while preventing biofilm formation by sulfate-reducing bacteria and methanogenic archaea over a three-month period, as well as against real environmental samples. This research brings new insights into materials science by demonstrating the potential of POM-ILs to act as environmentally sustainable solutions that addresses the challenges interfacing corrosion and microbial activity. By expanding the utility of ionic liquid technologies and integrating them with molecular metal oxides, this work paves the way for next-generation coatings with applications across diverse industrial sectors. |
In general, two main types of MIC can be distinguished: (1) electronic MIC (E-MIC), in which microorganisms directly take up electrons from the metal surface and use them as electron donors (e.g. sulfate-reducing bacteria (SRB) facilitating cathodic depolarization); and (2) chemical MIC (C-MIC), where microorganisms produce or modulate chemical species that promote corrosion (e.g., production of organic acids, hydrogen sulfide, concentration of chloride ions or other reactive components), but not necessarily by altering electron transfer directly.
The onset of MIC typically begins with the adhesion of microorganisms to a surface, followed by the development of a protective biofilm. This biofilm, composed of extracellular polymeric substances (EPS), acts as both a defensive barrier—shielding the microbial community from environmental stressors and toxic agents—and a selective filter that permits the diffusion of nutrients and metabolic byproducts. Within this microenvironment, microbial metabolic activity can dramatically alter local chemical conditions, accelerating metal dissolution and initiating corrosion processes.
Due to the highly localized nature of biofilm formation, MIC often leads to a non-uniform attack, resulting in damage that far exceeds that predicted by uniform corrosion models—sometimes reducing a structure's service life well below its original design parameters. When metals are the substrate, the situation becomes particularly critical. The electrochemical heterogeneity of the metal surface—where anodic and cathodic reactions occur at spatially separated sites—can promote pitting corrosion, a highly aggressive and localized form of attack. This can result in material failure far from the site of initial microbial activity. In critical infrastructure such as pipelines carrying flammable, toxic, or environmentally hazardous substances, such accelerated degradation can lead to catastrophic structural failures with severe safety and environmental consequences.4–6
Both aerobic and anaerobic microorganisms are involved in MIC, including sulfate-reducing bacteria (SRB), methanogenic archaea (MA), iron-oxidizer, iron-reducing microorganisms, and acetogenic microorganisms, among others.7 In anaerobic environments, SRB utilize sulfate as a terminal electron acceptor in place of oxygen, oxidizing organic substrates into organic acids and carbon dioxide while reducing sulfate to hydrogen sulfide (H2S). The generation of H2S poses serious challenges, as it readily reacts with various materials, often leading to corrosion. To date, research has primarily focused on metals—particularly iron—due to their critical role in infrastructure and industry. During MIC processes involving metals, metallic ions such as Fe2+ are released into the environment. These ions can react with biogenic sulfide to form poorly soluble ferrous sulfide (FeS) precipitates, which often accumulate as corrosive deposits on material surfaces.8 In the case of metals, MIC presents an additional challenge: ferrous sulfide (FeS), a common corrosion product formed by the reaction between Fe2+ and biogenic sulfide, is electrically conductive. This conductivity facilitates continued electron transfer at the metal surface, thereby sustaining and potentially accelerating the corrosion process. Another important group of MIC-associated microorganisms are methanogenic archaea (MA), which thrive on substrates associated with the terminal stages of the carbon cycle, including H2/CO2, acetate, methanol, and methylamines. Their metabolic end product is methane—a potent greenhouse gas with a significantly higher global warming potential than carbon dioxide. Notably, some methanogenic strains have evolved mechanisms to bypass conventional hydrogen metabolism. These electroactive methanogens are capable of directly accepting electrons from metallic surfaces and scavenging protons from the surrounding environment to generate hydrogen in situ. The locally produced hydrogen then fuels methanogenesis, further promoting MIC through a self-sustaining, bioelectrochemical feedback loop.9
Copper and its alloys are extensively used in various applications, including domestic and industrial pipeline systems, heat exchangers, fire sprinkler systems, and marine structures. This is due to their excellent machinability, thermal and electrical conductivity, ease of soldering, and corrosion resistance (as they are used even as a biocidal agent10–12). The formation of a protective patina on copper surfaces in the presence of oxygen enhances corrosion resistance by creating a passivating layer. Despite their long history as antibacterial and antimicrobial agents, copper – and particularly its alloys – are highly susceptible to microbial colonization and biodeterioration.10–12 Numerous cases of MIC have been reported for copper and its alloys, often resulting in significant infrastructure failures.12,13 Brass is a copper alloy composed primarily of copper and zinc, but one which often includes varying amounts of other metals like lead, tin, or iron to enhance its properties. Alpha (α) brass, characterized by a single-phase microstructure containing less than 37% zinc, is widely valued for its excellent cold-workability and inherent corrosion resistance. Despite these advantageous properties, α brass—like other copper-based alloys—is still susceptible to MIC, particularly in environments where microbial activity can alter local electrochemical conditions. Such corrosion can undermine the structural integrity of the material over time, limiting its long-term performance in critical applications.14,15
Several techniques are currently being used for the control, prevention, and inhibition of MIC. One of the most common techniques is cathodic polarization (CP). CP reduces the corrosion of a metal structure by making it the cathode of an electrochemical cell, using either a more active sacrificial anode or by impressing a current with an external direct current source. However, the effect of CP is still under discussion, since the current is not evenly distributed over the whole surface and the impact metabolic products (like acids) can have, is still unclear (especially in underground or sediment areas of a material).16–19
The effectiveness of the traditional techniques remains uncertain, particularly in complex dynamic environments, such as marine and wastewater systems where sampling and testing are difficult or even impossible. Recently, molybdate anions have demonstrated their effectiveness in inhibiting the growth of SRB and have been shown to reduce microbial souring in batch reactions.20 Furthermore, polyaniline–molybdate has been used to prevent corrosion on steel surfaces.21
Polyoxometalates (POMs) are a diverse class of nanoscale molecular metal oxides, with a wide and versatile range of physicochemical properties that can be tuned on the molecular level. POMs are composed of early transition metals from groups V and VI in their highest oxidation states, commonly VV, MoVI and WVI. The rich redox chemistry and diverse oxidation states of POMs means that they also display antimicrobial activity.22–24 Moreover, ionic liquids (ILs), which are salts with melting points below 100 °C have demonstrated excellent performance as anticorrosive agents through coating formation and lubrication.25–27 The greatest advantage of ILs is their modular design, which allows the cation and anion to be adjusted separately, thereby tailoring the formation of multifunctional materials that are appropriate for surface coatings.
Polyoxometalate-ionic liquids (POM-ILs), room-temperature ionic liquids formed from POM anions with bulky organic cations such as alkylammonium or -phosphonium,28 have gained significant attention in the area of surface-active IL coatings due to their exceptional chemical reactivity and versatility.29 Such POM-Ils have been used to great effect as coatings for natural stone, preventing corrosion and biodeterioration.30
Our hypothesis was that complex polyoxomolybdate-based POM-ILs could prove to be an innovative chemical solution for this emerging environmental and industrial problem. In this way, we demonstrate that the spectrum of activity and application of POM-ILs can be transferred to between sectors (e.g., heritage conservation and water purification) and materials (e.g., stone and metal surfaces). Furthermore, by doing so we demonstrate that POM-ILs have a broader “spectrum of action” than originally imagined. Here we report the synthesis and characterization of polyoxomolybdates transformed into POM-Ils using a tetraheptylammonium cation, which are used subsequently as hydrophobic, anticorrosive, and antimicrobial coatings (a cross-species effect) to prevent MIC of metal surfaces (Fig. 1).
Briefly, for the synthesis of Mo6, THEPA+ was added to an aqueous sodium molybdate solution adjusted to pH 5.5, under continuous stirring. This resulted in the formation of [(CH3(CH2)6)4N]2[Mo6O19], appearing as a dark green gel-like substance. The Mo6 Lindqvist structure is composed of four octahedrally coordinated [MoO6] units in a belt region, capped by Mo atoms on the top and bottom, yielding an overall octahedral symmetry. The synthesis of Mo8 followed an identical protocol, with the variation being the adjustment to pH 4, which yielded [(CH3(CH2)6)4N]4[Mo8O26] as a bright yellow gel-like substance. The [Mo8O26] structure features a six-membered ring of octahedral [MoO6] units, capped on both sides by two {MoO4} tetrahedra.31
The synthesized POM-Ils were characterized using Fourier transform infrared spectroscopy (FT-IR), Thermogravimetric analysis (TGA), and elemental analysis to confirm their composition and purity (Table S1, ESI†). The FT-IR spectra of the two POM-ILs exhibited characteristic absorption bands for the POM. Specifically, the bands at 954 and 795 cm−1 correspond to MoO and Mo–O–Mo, respectively. The presence of tetraheptylammonium was verified by the presence of the C–H stretching bands at 2957 and 2871 cm−1, which are assigned to ν(C–H) stretching vibrations in the aliphatic alkyl chains. The bending vibrations of CH2 and CH3 groups are observed in the range of 1400–1480 cm−1, corresponding to δ(CH2), δas(CH3), and δs(CH3) modes (Fig. 2).32,33 Thermogravimetric analysis (TGA) provided insights into the thermal stability and the distribution between the organic and inorganic components of the POM-ILs. Both materials were stable up to at least 190 °C. Subsequent weight losses were ascribed to the decomposition of THEPA+ cations, the organic part of the material. For Mo6 and Mo8, the weight losses of the organic portion of the POM-ILs at 400 °C of 50.68% and 59.35% aligned with the corresponding theoretical value of 48% and 58%, respectively (Fig. S1 and S2, ESI†).
The experimental protocol involved using a 96-well plate assay. Bacteria were cultured in appropriate media (E. coli in Luria-Bertani and B. subtilis and S. epidermidis in Nutrient Broth) and exposed to serial dilutions of POM-ILs in 2% dimethylsulfoxide (DMSO) (Fig. S6, ESI†). Bacterial viability was evaluated using a resazurin-based colorimetric assay, where resazurin (blue) is reduced to resorufin (pink) by metabolically active cells.34 The concentration of POM-ILs inhibiting bacterial growth was determined by the absence of color change (Fig. S7, ESI†).
Table 1 presents the corresponding minimum bactericidal concentrations (MBCs) of the POM-ILs against three model bacterial strains, E. coli, B. subtilis, and S. epidermidis. The higher MBC values for E. coli are due to structural differences between Gram-negative and Gram-positive bacteria. Gram-negative bacteria have approx. 2.5–4 nm peptidoglycan cell wall and an outer membrane, while Gram-positive bacteria have thicker (approx. 30–100 nm) layers of peptidoglycan.35 POM-ILs exert antimicrobial effects primarily through electrostatic interactions with negatively charged bacterial cell surfaces. These interactions likely disrupt membrane integrity, leading to cell death. Gram-positive bacteria, with their porous peptidoglycan walls, are generally more susceptible, whereas Gram-negative bacteria require higher concentrations due to their protective outer membrane.36
Minimum bactericidal concentration (MBC) (μg mL−1) | |||
---|---|---|---|
Bacteria | E. coli | B. subtilis | S. epidermidis |
a Resazurin cell viability assays were confirmed by colony counting of aliquots seeded on agar plates (refer to Experimental section). | |||
Mo6 | 3.5 | 0.6 | 0.4 |
Mo8 | 4.0 | 0.4 | 0.4 |
To determine the extent of bacterial reduction, the number of bacterial colonies on the metal samples coated with POM-ILs was compared to the number of colonies on uncoated samples. The metal surfaces were coated with 80 μL of 40 mg mL−1 concentration for Mo6 and Mo8. The results showed that at these concentrations there was a 100% reduction of bacterial growth on all metal surfaces for both bacteria strains (Table S3, ESI†).
Further analysis using scanning electron microscopy (SEM) was conducted to observe the effect of POM-ILs on the metal surfaces. The SEM images of the uncoated brass samples (Fig. 3a) showed significant biofilm formation on the surface after 48 hours. In contrast, the brass samples coated with POM-ILs (Fig. 3b) displayed non-viable bacterial cells and cell components dispersed on the surface, indicating an effective prevention of biofilm formation.
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Fig. 3 SEM images of an E. coli biofilm growth in LB medium for 48 hours on: (a) the uncoated brass coupon; (b) brass coupon coated with 40 mg mL−1 of Mo8. |
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Fig. 4 SEM (10![]() |
EIS data were fitted using two different electrical equivalent circuit (EEC) models: one for uncoated samples and coated samples measured after exposure and cleaning (Fig. 5a), and another for non-exposed coated samples, which retained the coating for the EIS measurements (Fig. 5b). For exposed and cleaned samples, a model with three parallel RCPE (resistance-constant phase element) components was used. The first RCPE at high frequency attributed to the natural brass patina, the second to charge transfer resistance, and the third to the diffusion of corrosion products (Fig. 5a and Table 2). For coated samples (Fig. 5b and Table 3), additional elements were included to represent coating resistance (Rcoating) and capacitance (CPEcoating), as well as charge transfer resistance (Rct) and double-layer capacitance (CPEdl), with the Warburg element describing diffusion through the coating.41,42
Metal sample | Rpatina (Ω cm2) (f–kHz) | Rct (Ω cm2) (f–Hz) | Rdiff (Ω cm2) (f–mHz) |
---|---|---|---|
Uncoated + non-exposed | 1.99 × 104 (13.9) | 5.50 × 104 (0.4) | 6.31 × 104 (19.5) |
Uncoated + exposed | 2.11 × 104 (14.9) | 3.63 × 103 (3.2) | 1.62 × 104 (32.7) |
Mo6-coated + exposed | 1.95 × 104 (13.7) | 8.90 × 103 (1.6) | 3.04 × 104 (23.0) |
Mo8-coated + exposed | 1.91 × 104 (14.1) | 1.06 × 104 (1.4) | 3.27 × 104 (20.9) |
Samples | Rcoating (Ω cm2) (f–kHz) | Rct (Ω cm2) (f–Hz) | WoR (Ω cm2) (T–s) |
---|---|---|---|
Mo6-coated + non-exposed | 1.68 × 104 (34.2) | 1.88 × 104 (0.70) | 9.98 × 103 (78.15) |
Mo8-coated + non-exposed | 1.80 × 104 (32.7) | 1.04 × 104 (0.74) | 5.62 × 103 (68.80) |
In the first model (Fig. 5a and Table 2), as corrosion of brass is mainly associated with zinc depletion, no significant change was observed in the first contribution (patina), which is related to the copper carbonate surface layer. However, a clear decrease in the Rct value was observed when going from non-exposed to exposed samples, indicating increased corrosion activity after exposure. This decrease was less pronounced in coated samples, demonstrating the protective effect of the coatings. Moreover, coated samples also exhibited higher diffusion resistance (third element) than the uncoated ones, though still lower than under non-exposed conditions.42
The second model was used to fit the results for coated samples which were neither exposed to acidic environment nor cleaned, that is, the coating was present during the EIS measurements (Fig. 5b and Table 3). Similar Warburg resistance (WoR) and T-parameters were obtained across coated samples, suggesting that the diffusion of corrosion products through the coating pores is comparable. These results are summarized in Tables 2 and 3.
Bode plots (Fig. 5c and d) complemented this analysis, showing low conductivity at lower frequencies for coated samples after the exposure, a sign of effective corrosion protection.41,42 Overall, the EIS analysis confirmed that both Mo6 and Mo8 coatings offered substantial protection, with Mo8-coated samples showing particularly strong resistance to the corrosive environment.
Experimental Conditions | Experiment 1 (E1) | Experiment 2 (E2) |
---|---|---|
Media | Artificial sea water supplemented with 1 M sulfate | Artificial sea water supplemented with 1 M lactate and 1 M sulfate |
Microorganism | Desulfovibrio ferrophilus IS5 | Methanococcus maripaludis (Mic1c10) and Oleidesulfovibrio alaskensis 16109 |
Incubation period | Thirteen weeks | Eight weeks |
Two experiments were carried out to evaluate the effectiveness of POM-IL as a protective coating against MIC on brass coupons. In Experiment 1, sulfate-supplemented artificial seawater was inoculated with D. ferrophilus IS5 and six samples were prepared: three with POM-IL coating and three without used as controls. In Experiment 2, artificial seawater was supplemented with lactate (10 mL, 1 M) and sulfate (15 mL, 1 M) and inoculated with a mixture of 2.5 mL of the SRB Oleidesulfovibrio alaskensis 16109 preculture and 2.5 mL of the MA Methanococcus maripaludis Mic1c10 preculture in a similar setup as described before. All experiments were conducted under anaerobic, sterile conditions in which all equipment was sterilized and headspaces were flushed with N2/CO2 to maintain an oxygen-free environment and avoid contamination.
Visual inspection revealed a distinct contrast between the POM-IL coated and uncoated coupons in both experiments. The surface of the POM-IL-coated coupons (Fig. 6c and g) almost retained their original appearance in terms of color, surface integrity and brightness, whereas the uncoated ones (Fig. 6b and f) exhibited evident surface attack and deterioration. Upon closer examination of the sample surfaces, for the coupons coated with POM-IL maintained a consistent surface, similar in smoothness to the initial state. In contrast, the uncoated coupons exhibited substantial disparities in color, surface structure, and observable rough features on the surface.
In Experiment 1, SEM images of uncoated coupons exposed to Desulfovibrio ferrophilus IS5 (Fig. 6a) revealed a complex biofilm development, characterized by a heterogeneous surface with elevated regions and flaky corrosion byproducts, potentially metal oxides originating from artificial seawater (ASW) medium. In contrast, coated samples (Fig. 6d) exhibited a relatively homogeneous surface with occasional cracks and sparse corrosion byproducts near these cracks, suggesting the formation of a protective passivation layer by the POM-IL coating, which limited microbial attachment and surface degradation. Quantitatively, uncoated samples showed a weight loss of 0.087% and a corrosion rate of 0.003 mm year−1, compared to the coated samples with a significantly reduced weight loss of 0.009% and a corrosion rate of 0.0003 mm year−1, indicating nearly 10 times of reduction in corrosion (Table 5).
Sample | Initial weight (g) | Final weight (g) | Weight loss (%) | Corrosion rate (mm year−1) |
---|---|---|---|---|
E1 Uncoated | 2.0536 | 2.0518 | 0.087 | 0.003 |
E1 Coated | 2.0630 | 2.0628 | 0.009 | 0.0003 |
E2 Uncoated | 2.0985 | 2.0920 | 0.309 | 0.0167 |
E2 Coated | 2.0969 | 2.0959 | 0.047 | 0.0026 |
In Experiment 2, SEM imaging of uncoated coupons exposed to a mixture of Methanococcus maripaludis and Desulfovibrio alaskensis (Fig. 5e) showed flaky corrosion products, cylindrical bacterial cells, and a visibly uneven surface, all indicative of biofilm formation and extensive surface damage. Coated samples (Fig. 5h) displayed a protective layer, however, with small surface cracks, where corrosion byproducts such as copper and zinc oxides (confirmed by EDX spot analyses) were localized at the edges of these cracks rather than uniformly distributed. Additionally, dispersed non-viable bacterial cells and cellular components were observed, suggesting a reduced ability for biofilm formation on the coated surfaces. Weight-loss measurements showed that uncoated samples suffered 0.309% weight loss and a corrosion rate of 0.017 mm year−1, while coated samples had significantly lower values of 0.047% and 0.003 mm year−1, respectively, demonstrating a six-times reduction in corrosion (Table 5).
The corrosion rates of four commonly used biocidal treatments in the oil and gas industry, specifically against Desulfovibrio ferrophilus IS5, are illustrated in (Fig. S13, ESI†), derived from previously published literature.48 Among these, POM-IL exhibited the lowest corrosion rate, at 0.003 mm year−1. Tetrakis(hydroxymethyl)phosphonium sulfate (THPS) followed with a corrosion rate of 0.025 mm year−1. A combination of glutaraldehyde (GLUT) and benzalkonium chloride (BAC) demonstrated a higher corrosion rate of 0.15 mm year−1, while glutaraldehyde (GLUT) alone resulted in the highest corrosion rate of 0.44 mm year−1. These data highlight the efficacy of POM-IL in comparison to more traditional biocidal treatments.
Such sediments are expected to host diverse microorganisms, including SRB and methanogens. The sediment samples were introduced into controlled environments alongside brass coupons, coated and uncoated with POM-IL. Results revealed a stark contrast between biotic (microorganism-containing) and abiotic (sterilized) sediment samples. Uncoated coupons displayed significant surface degradation, with biotic samples exhibiting higher corrosion rates than their abiotic counterparts. Notably, sediment with active microbial communities produced higher concentrations of dissolved sulfide, corroborating the metabolic activity of SRB within these environments.
In the biotic samples, high sulfide concentrations were observed due to SRB activity, with uncoated samples exhibiting sulfide levels of up to 0.106 mM (Table S4, ESI†). This directly correlated with elevated corrosion rates in the uncoated coupons (Table S5, ESI†). For example, the uncoated biotic brass samples showed corrosion rates exceeding 3.47 × 10−3 mm year−1, demonstrating significant material degradation within just 13 weeks of exposure. In contrast, POM-IL-coated coupons significantly mitigated these effects. Coated biotic samples displayed reduced sulfide concentrations (as low as 0.087 mM) and halved corrosion rates (1.58 × 10−3 mm year−1), highlighting the ability of the coating to inhibit microbial activity and protect the underlying metal surface. Further experiments along this line are already planned to optimize and establish the efficacy of POM-IL coatings in the context of environmental samples.
SEM analysis revealed distinct differences between biotic and abiotic samples, both coated and uncoated. In the biotic, uncoated sample (Fig. 7a), dense biofilm structures and extensive surface pitting were observed, accompanied by visible corrosion byproducts such as sulfides, indicating aggressive microbial activity. The presence of repetitive cylindrical structures, resembling microorganisms, and high sulfur concentrations further suggested the involvement of SRB in the corrosion process. In contrast, the biotic, coated sample (Fig. 7d) showed a more homogeneous surface with minimal biofilm formation and reduced pitting.
In the abiotic, uncoated sample (Fig. 7e), cloudy corrosion products were evident, likely the result of chemical corrosion or mineral precipitation, with no signs of biological activity. On the other hand, the abiotic, coated sample (Fig. 7h) displayed copper/zinc oxides in the form of white round shapes, confirming the protective role of the coatings against oxidation. While some cracking of the POM-IL layer was noted, it did not significantly compromise the protection, and the surface showed far less corrosion compared to the uncoated sample, demonstrating the efficacy of the coating in mitigating chemical degradation.
These results demonstrate the dual functionality of POM-IL coatings in mitigating MIC: (1) reducing microbial colonization and sulfide production, and (2) providing a physical barrier that inhibits chemical and microbial-induced surface degradation. This is especially significant in environments rich in sediments where microbial activity is highly concentrated, such as marine or freshwater systems.
Although laboratory MIC systems cannot fully replicate the unpredictable and multifactorial nature of real environmental settings, they provide a robust platform for assessing protective materials under representative conditions. The current endeavors simulate different biocorrosive environments using environmental samples and mixed microbial consortia to evaluate the efficacy of POM-IL nanocoatings on metal surfaces. The findings serve as a scientifically relevant foundation for future studies aiming to incorporate broader and more dynamic and even codependent environmental variables.
Our findings indicate that POM-IL coatings effectively protect brass coupons exposed to acidic environments for one month and embedded in environmental sediment over a three-month period. Coated samples exhibited significantly less surface damage and maintained their integrity compared to uncoated samples, demonstrating the ability of POM-IL coatings to inhibit corrosion and microbial colonization. SEM analysis showed that POM-IL coatings reduced surface irregularities and the formation of corrosion products, further underscoring their protective capabilities. Additionally, POM-IL coatings were effective at inhibiting sulfate-reducing bacteria activity, as evidenced by lower sulfide concentrations in coated samples, indicating cross-species biocidal activity. Despite these promising results, we also identified some limitations, SEM images revealed occasional cracking post-exposure. These cracks likely stem from mechanical stress during the drying process, as well as fluctuations in temperature and humidity during storage or testing. Since POM-ILs are applied as relatively soft films that evaporate solvents, they can develop internal tension when the solvent (acetone) evaporates quickly, leading to shrinkage and minor fissures. In environments where temperature or humidity varies, the differences in thermal expansion between the brass substrate and the POM-IL layer might also play a role in crack formation.
Although these cracks did not significantly affect the short-term performance of the coating (as confirmed through corrosion data and SEM analysis), they could potentially allow corrosive agents or microorganisms to penetrate over time, which might reduce the long-term protective effectiveness of the POM-IL layer. As such, our on-going research efforts are currently focused on optimizing the protective properties of POM-IL coatings and validating their applicability in real-world scenarios, for instance, by incorporating POM-ILs into polymeric supports to improve their long-term performance and durability. This mixed strategy aims to merge the antimicrobial and anticorrosive benefits of POM-ILs with the mechanical strength of traditional polymers. We believe that overcoming such practical obstacles could enable POM-IL coatings to become a robust and reliable solution for corrosion mitigation in various industrial and cultural contexts.
In an Erlenmeyer flask, 10 g (0.04 mol) of sodium molybdate dihydrate (Na2MoO4·2H2O) was dissolved in 40 mL of water. The solution was acidified by adding 11.6 mL of 6 N hydrochloric acid (HCl) and stirred vigorously for 1 min at room temperature. To the acidified sodium molybdate solution, a separate solution of 7.30 g (0.01 mol) of tetraheptylammonium bromide [CH3(CH2)6]4NBr in 8 mL of water was added with vigorous stirring. The addition resulted in the formation of a white precipitate. The resulting slurry was heated to a temperature range of 75 to 85 °C and stirred for 45 min. During this process, the white solid changed to a green color. The light green particles were separated from the solution through filtration, and subsequent washing was performed with water to remove any residual impurities. The washed particles were then dried under vacuum conditions to ensure complete solvent removal. The dried light green particles were dissolved in 30 mL of toluene. The toluene was evaporated on a rotary evaporator and the resulting dark green complex was collected as the total product. Yield: 10.6 g, 90% (based on Mo). FT-IR (cm−1): 2957 and 2871 cm−1 (ν(C–H)), 1400–1480 cm−1 (δ(CH2), δas(CH3), δs(CH3)), 954 cm−1 (MoO), and 795 cm−1 (Mo–O–Mo). TGA expt. (calc.): 50.68% (48%). CHN expt. (calc.)%: C: 41.9 (39.5), H 6.9 (7.1), N 1.7 (1.6).
In a 100 mL beaker, 10 g (0.04 mol) of commercial sodium molybdate dihydrate was dissolved in 24 mL of water. The solution was then acidified by adding 10.4 mL of 6 N aqueous HCl, and vigorous stirring was maintained over a period of 2 min at room temperature. A solution of 10.16 g (0.02 mol) of tetraheptylammonium bromide in 30 mL of toluene was prepared in a separate container. The tetraheptylammonium bromide solution was added to the acidified sodium molybdate solution with vigorous stirring, and the mixture was stirred for 25 min resulting in a yellow solution, which was then transferred to a vacuum rotary evaporator in order to remove the remaining toluene solvent, leaving the final yellow product. Yield: 10.8 g, 76% (based on Mo). FT-IR (cm−1): 2957 and 2871 cm−1 (ν(C–H)), 1400–1480 cm−1 (δ(CH2), δas(CH3), δs(CH3)), 954 cm−1 (MoO), and 795 cm−1 (Mo–O–Mo). TGA expt. (calc.): 59.35% (58%). CHN expt. (calc.)%: C 51.6 (47.6), H 8.5 (8.6), N 2.1 (2.0).
Seawater media were prepared for experiments 1 and 2 (Table 4). To prepare 1L ASW a sterile container was filled with 1L Milli-Q water. The media was supplemented with the following salts: 0.45 mol (26.37 g) of NaCl, 0.12 mol (11.20 g) of MgCl2, 0.01 mol (1.48 g) of CaCl2 and 0.008 mol (0.60 g) KCl under stirring conditions to dissolve completely. After complete dissolution of all the salts, the pH was adjusted with Na2CO3 to 7.2. Subsequently, the medium was sterilized by autoclaving at 121 °C for 15 min. After cooling down the media to room temperature other minerals and other heat sensitive components e.g. vitamins, were added to create a well-balanced and nutrient-rich environment that supports the growth and metabolic activities of specific microorganisms in the media.
Ammonium chloride (NH4Cl, 3.74 M, 1.25 mL) and potassium dihydrogen phosphate (KH2PO4, 1.10 M, 1.33 mL) were added to enhance the salinity and phosphate content. To support microbial metabolism, sodium bicarbonate (NaHCO3) at 1 M concentration (60 mL) was included as a carbon source. Additionally, trace elements without EDTA from FMU (1 mL), Se-Wo (1 mL), and 5-vitamins from FMU (1 mL) were added to provide essential micronutrients. For cofactor and vitamin supplementation, lipoic acid + folic acid (1 mL), thiamine at a concentration of 0.1 mg mL−1 (1 mL), riboflavin at a concentration of 0.025 g mL−1 (1 mL), and vitamin B12 at a concentration of 0.05 mg mL−1 (1 mL) were added. To create reducing conditions in the media, sodium sulfide (Na2S) at 1 M concentration (1 mL) and cysteine (1 mL) were included. Lastly, acetate (1 mL) was incorporated to serve as an additional carbon and energy source for microbial growth. These supplements collectively contribute to the optimal nutritional environment for the targeted microorganisms within the media. For experiment 1:
15 mL of Na2SO4 (1 M) was added. For the experiment 2
:
10 mL lactate (1 M) and 15 mL Na2SO4 (1 M) were added. Lactate was supplemented to act as an electron donor. Sulfate was added to act as an electron acceptor in anaerobic respiration of SRB, where they reduce sulfate to sulfide.
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Footnote |
† Electronic supplementary information (ESI) available: Additional experimental details, data, figures and tables. See DOI: https://doi.org/10.1039/d5mh00373c |
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