Thermophilic and mesophilic bacteria in biofilms associated with corrosion in a heat exchanger

Biofilm development on AISI-1020 carbon steel coupons installed at the outlet of a heat exchanger was evaluated at the thirtieth and the sixtieth days of exposure. Water temperature varied between 41 and 60°C. The most probable number technique (MPN) was applied to quantify mesophilic and thermophilic species of aerobic, anaerobic, and sulphate-reducing bacteria (SRB) in planktonic and sessile phases. The results showed predominance of thermophilic aerobic bacteria in both phases, corresponding to 9.5±0.8×10⁶cells/ml in the planktonic phase. In biofilms, maximal aerobic cell concentration, 7.8±0.6×10⁸cells/cm2, was registered at the sixtieth day. An increase in the number of thermophilic anaerobic and SRB with elapsed time was also observed. The results obtained after 60 days were 5.8±0.4×10⁷ and 8.9±0.9×10⁴cells/cm² for anaerobic and sulphate-reducing bacteria, respectively. Scanning electron microscopy showed a varied composition of species in the biofilms and corrosion on the carbon steel surfaces after biofilm removal.     

Disturbance,starvation, and overfeeding stresses detected by microbial lipid biomarkers in high-solids high-yield methanogenic reactors

Summary Microbial biomass and community structure of methanogenic anaerobic biomass reactors can be quantitatively monitored by signature, lipid analysis. The eubacterial and eukaryotic polar lipid fatty acids and the methanogen polar lipid ethers are reliable measures of their respective biomasses. The pattern of polar lipid fatty acids yields information on the community structure and metabolic state of the eubacteria and eukaryotes. These biomarker methods were applied over a 2-day feeding cycle of a highly productive batch-fed high-solids anaerobic biomass reactor. It was sampled before feeding, 6 h after feeding (disturbed)., at maximum gas production (healthy, 24 h), and after feedstock utilization (starved, 48h). Relative to the healthy condition, the disturbance of feeding significantly decreased eubacterial biomass and the proportion of unsaturated fatty acids, and increased branched fatty acids and the eubacterial stress biomarker,trans/cis 16: 17. The starved condition was not significantly different from the healthy in biomass or proportions of fatty acids, but did show a significant increase in the proportion of the eubacterial stress biomarkertrans/cis 18: 17. This reactor was compared to a second of the same design which had been overfed and showed significantly less productivity. The overfed reactor had a significantly lower methanogenic biomass,iso-branched fatty acids, and higher eubacterial stress markers Cy17:0 andtrans/cis 18: 17 than the highly productive reactor.     

Scanning electron microscopy of biofilm development in anaerobic fixed-bed reactors: Influence of the inoculum

Summary Scanning electron microscopy was applied to evaluate the influence of inoculum on efficiency of initial biofilm formation and reactor performance. Five anaerobic fixed-bed reactors were inoculated with anaerobic sludges from different sources and operated in parallel under identical conditions with defined wastewater and acetate, propionate and butyrate as constituents In all sludges Methanothrix sp. was the predominant acetotroph. The reactors inoculated with anaerobic sludge adapted to the wastewater achieved the highest space loading with 21.0 g COD/l·d after 58 days. The inoculation with granular sludge from an upflow anaerobic sludge blanket (UASB) reactor resulted in significantly less reactor efficiency. Time course of biofilm formation and biofilm thickness (ranging from 20–200 m) depended on the type of inoculum.     

Modeling of an anoxic/methanogenic biofilm: effect of pH calculation within the biofilm

The models of anoxic/methanogenic processes in biofilm reactors published until now have supposed that pH does not change between the bulk liquid and biofilm. These assumptions are not necessarily valid for processes in reactors with biofilms. The present work studied an anoxic/methanogenic biofilm reactor incorporating the pH variation in both bulk and biofilm. Two dynamic models, one including the calculation of pH throughout the biofilm, were solved numerically and compared with each other. The results showed that the inclusion of a pH algorithm calculation produces different profiles and efficiencies on an anoxic/methanogenic biofilm system. Values of C/N ratio higher than 20 mg TOC/mg NO₃–N and values of HRT lower than 4.5 h produce differences of up to 46 % with a traditional model that does not include pH calculation inside the biofilm. Thus, the assumption of a constant pH within the biofilm when using the traditional model does not accurately describe the performance of the system under these conditions, and pH calculation inside the biofilm should be included.     

Testing the Efficiency of Biofilms Formed on Natural Substratum,Coyonoxtle (Opuntia Imbricata), for the Anaerobic Degradation of Aromatic Compounds

In this study, previously developed anaerobic microbial consortia capable of degrading aromatic compounds were used to develop biofilms on a natural material, coyonoxtle (Opuntia imbricata), which is abundantly available in North Mexico. The developed biofilms were evaluated for their efficiency in the biodegradation of different aromatic compounds, viz., phenol, catechol, 4‐aminobenzoic acid and p‐phenylenediamine in batch reactors. It was observed that in reactors with biofilms a more than 90 % COD removal and a concomitant production of methane could be obtained. But the rate of COD removal and methane production varied depending upon the type of biofilm used. Rumen‐derived biofilms demonstrated a lag phase of 7 to 14 days, whereas sludge‐derived biofilms exhibited a lag phase of more than three weeks. Between the biofilms from two sources, rumen‐derived biofilms showed a higher COD removal and methane production than sludge‐derived biofilms. When biofilm reactors were compared with reactors containing freely suspended consortia, it was evident that both rumen– and sludge‐derived biofilm reactors exhibited a two‐fold higher COD removal and methane production. Based on the results obtained, it can be concluded that coyonoxtle has the potential for use as a substratum.     

Biofilm development in laboratory methanogenic fluidized bed reactors

Biofilm development on sand with different heterogeneous inocula was studied in laboratory-scale methanogenic fluidized bed reactors. Both the course of biofilm formation during reactor start-up and the bacterial composition of newly developed biofilms at steady-state were found to be similar irrespective of the type of inoculum applied. Biofilm formation proceeded according to a fixed pattern that could be subdivided in three consecutive phases, designated as the lag phase, biofilm production phase, and steady-state phase. Methanogenic activity and biomass content of the fluidized bed granules were found to be accurate parameters of the course of biofilm formation. More indirect parameters monitored did not give unambiguous results in all instances. The composition of the newly developed biomass as assessed on the basis of potential methanogenic activities on different substrates and of the concentration of specific methanogenic cofactors was consistent with electron microscopic observations.     

Microbial characteristics of methanogenic sludge consortia developed in thermophilic U ASB reactors

The effect of temperature on granulation and microbial interaction of anaerobic sludges grown in thermophilic upflow anaerobic sludge bed (UASB) reactors was investigated at two different temperatures, 55°C (Run 1) and 65°C (Run 2). Each run consisted of two phases. Phase 1 was conducted by feeding acetate for a period of 200 days. In Phase 2, both reactors were fed a mixture of acetate and sucrose for a further 100 days. During Phase 1, no granulation occurred in the sludge of either run. Microscopic observation revealed that the predominant methanogen was Methanothrix in Run 1, whereas Methanobacterium-like bacteria existed to a significant extent in Run 2. The acetate-utilizing methanogenic activity of both sludges increased with increasing test temperature in the range 55–65°C. Since the acetate-grown sludges exhibited far higher H₂-utilizing methanogenic activity than acetate-utilizing methanogenic activity, it is suggested that a syntrophic association of acetate-oxidizing bacteria with hydrogenotrophic methanogens was responsible for a considerable portion of the overall acetate elimination in thermophilic anaerobic sludge. During Phase 2, granules coated with either filamentous bacteria or cocci-type bacteria (both presumably acid-forming bacteria) were successfully established in Run 1 and Run 2, respectively. Since the acetate-utilizing methanogenic activities of the granular sludges were four to five times higher than those of the acetate-grown sludges (Phase 1), the co-existence of these coating bacteria appeared to contribute to the enclosing of acetate consumers inside granules. Correspondence to: S. Uemura     

Interconversion of F430 derivatives of methanogenic bacteria

F₄₃₀ is the prosthetic group of the methylcoenzyme M reductase of methanogenic bacteria. The compound isolated from Methanosarcina barkeri appears to be identical to the one obtained from the only distinctly related Methanobacterium thermoautotrophicum. F₄₃₀ is thermolabile and in the presence of acetonitrile or C10 _in4 ^sup- two epimerization products are obtained upon heating; in the absence of these compounds F₄₃₀ is oxidized to 12, 13-didehydro-F₄₃₀. The latter is stereoselectively reduced under H₂ atmosphere to F₄₃₀ by cell-free extracts of M. barkeri or M. thermoautotrophicum. H₂ may be replaced by the reduced methanogenic electron carrier coenzyme F₄₂₀.Abbreviations CH₃S-CoM methylcoenzyme M, 2-methylthioethanesulfonic acid - HS-CoM coenzyme M, 2-mercaptoethanesulfonic acid - F₄₃₀ Ni(II) tetrahydro-(12, 13)-corphin with a uroporphinoid (III) ligand skeleton - 13-epi-F₄₃₀ and 12,13-di-epi-F₄₃₀ the 12, 13- and 12, 13-derivatives of F₄₃₀ - 12, 13-didehydro-F₄₃₀ F₄₃₀ oxidized at C-12 and C-13 - coenzyme F₄₂₀ 7,8-didemethyl-8-hydroxy-5-deazaflavin derivative - coenzyme F₄₂₀H₂ reduced coenzyme F₄₂₀ - MV⁺ methylviologen semiquinone - HPLC high-performance liquid chromatography     

Fe(III) Oxide Reduction by Anaerobic Biofilm Formation-DeficientS-Ribosylhomocysteine Lyase (LuxS) Mutant of Shewanella oneidensis

Shewanella oneidensis respires a variety of terminal electron acceptors, including solid phase Fe(III) oxides. S. oneidensis transfers electrons to Fe(III) oxides via direct (outer membrane- or nanowire-localized c-type cytochromes) and indirect (electron shuttling and Fe(III) solubilization) pathways. In the present study, the influence of anaerobic biofilm formation on Fe(III) oxide reduction by S. oneidensis was determined. The gene encoding the activated methyl cycle (AMC) enzyme S-ribosylhomocysteine lyase (LuxS) was deleted in-frame to generate the corresponding mutant ΔluxS. Conventional biofilm assays and visual inspection via confocal laser scanning microscopy indicated that the wild-type strain formed anaerobic biofilms on Fe(III) oxide-coated silica surfaces, while the ΔluxS mutant was severely impaired in anaerobic biofilm formation on such surfaces. Cell-hematite attachment isotherms demonstrated that the ΔluxS mutant was also severely impaired in attachment to hematite surfaces under anaerobic conditions. The S. oneidensis ΔluxS mutant, however, reduced Fe(III) at wild-type rates during anaerobic incubation with Fe(III) oxide-coated silica surfaces or in batch cultures with Fe(III) oxide or hematite as a terminal electron acceptor. Anaerobic biofilm formation by the ΔluxS mutant was restored to wild-type rates by providing a wild-type copy of luxS in trans or by the addition of AMC or transsulfurylation pathway metabolites involved in organic sulfur metabolism. LuxS is thus required for wild-type anaerobic biofilm formation on Fe(III) oxide surfaces, yet the inability to form wild-type anaerobic biofilms on Fe(III) oxide surfaces does not alter Fe(III) oxide reduction activity.     

Early stages in biofilm development in methanogenic fluidized-bed reactors

Summary Biofilm development in methanogenic fluidized-bed reactors with sand as the carrier was studied on a laboratory scale. The microorganisms present in consecutive layers of the biofilm of mature sludge granules were preliminarily characterized on the basis of their morphology, element composition and adhesion capacity and were compared to bacteria which take part in the initial colonization of sand. The early phase of biofilm development was monitored with reactors receiving waste-waters containing different mixtures of volatile fatty acids and inoculated with fluidized-bed reactor effluent for different lengths of time. The results obtained indicate that facultative anaerobic bacteria abundantly present in the outermost biofilm layers of mature sludge granules are probably the main primary colonizers of the sand. Methanothrix spp. or other methanogens were rarely observed among the primary colonizers. The course of biofilm formation was comparable under the various start-up conditions employed including variations in waste-water composition, inoculation and anaerobicity. However, omission of waste-water and thus of substrate resulted in rapid wash-out of the attached biomass. Offprint requests to: W. Heinen     

Gene expression in<Emphasis Type="Italic"> Escherichia coli</Emphasis> biofilms

DNA microarrays were used to study the gene expression profile of Escherichia coli JM109 and K12 biofilms. Both glass wool in shake flasks and mild steel 1010 plates in continuous reactors were used to create the biofilms. For the biofilms grown on glass wool, 22 genes were induced significantly (p0.05) compared to suspension cells, including several genes for the stress response (hslS, hslT, hha, and soxS), type I fimbriae (fimG), metabolism (metK), and 11 genes of unknown function (ybaJ, ychM, yefM, ygfA, b1060, b1112, b2377, b3022, b1373, b1601, and b0836). The DNA microarray results were corroborated with RNA dot blotting. For the biofilm grown on mild steel plates, the DNA microarray data showed that, at a specific growth rate of 0.05/h, the mature biofilm after 5 days in the continuous reactors did not exhibit differential gene expression compared to suspension cells although genes were induced at 0.03/h. The present study suggests that biofilm gene expression is strongly associated with environmental conditions and that stress genes are involved in E. coli JM109 biofilm formation.     

Genomically and biochemically accurate metabolic reconstruction of Methanosarcina barkeri Fusaro,iMG746

Methanosarcina barkeri is an Archaeon that produces methane anaerobically as the primary byproduct of its metabolism. M. barkeri can utilize several substrates for ATP and biomass production including methanol, acetate, methyl amines, and a combination of hydrogen and carbon dioxide. In 2006, a metabolic reconstruction of M. barkeri, iAF692, was generated based on a draft genome annotation. The iAF692 reconstruction enabled the first genome-Scale simulations for Archaea. Since the publication of the first metabolic reconstruction of M. barkeri, additional genomic, biochemical, and phenotypic data have clarified several metabolic pathways. We have used this newly available data to improve the M. barkeri metabolic reconstruction. Modeling simulations using the updated model, iMG746, have led to increased accuracy in predicting gene knockout phenotypes and simulations of batch growth behavior. We used the model to examine knockout lethality data and make predictions about metabolic regulation under different growth conditions. Thus, the updated metabolic reconstruction of M. barkeri metabolism is a useful tool for predicting cellular behavior, studying the methanogenic lifestyle, guiding experimental studies, and making predictions relevant to metabolic engineering applications.     

Relation of coenzyme F420 to the activity of methanogenic microorganisms

Summary The relationship between the coenzyme F₄₂₀ content and the activity of methanogenic microorganisms was investigated under different cultivation conditions in anaerobic reactors. The coenzyme F₄₂₀ concentration depends on the substrate used and the cultivation conditions. Coenzyme F₄₂₀ appears not to be a measure of the total methanogenic activity but rather a measure of the amount of methanogenic microorganisms in mixed anaerobic cultures.     

The Use of Drip Flow and Rotating Disk Reactors for Staphylococcus aureus Biofilm Analysis

Most microbes in nature are thought to exist as surface-associated communities in biofilms.¹ Bacterial biofilms are encased within a matrix and attached to a surface.² Biofilm formation and development are commonly studied in the laboratory using batch systems such as microtiter plates or flow systems, such as flow-cells. These methodologies are useful for screening mutant and chemical libraries (microtiter plates)³ or growing biofilms for visualization (flow cells)⁴. Here we present detailed protocols for growing Staphylococcus aureus in two additional types of flow system biofilms: the drip flow biofilm reactor and the rotating disk biofilm reactor.Drip flow biofilm reactors are designed for the study of biofilms grown under low shear conditions.⁵ The drip flow reactor consists of four parallel test channels, each capable of holding one standard glass microscope slide sized coupon, or a length of catheter or stint. The drip flow reactor is ideal for microsensor monitoring, general biofilm studies, biofilm cryosectioning samples, high biomass production, medical material evaluations, and indwelling medical device testing.^6,7,8,9The rotating disk reactor consists of a teflon disk containing recesses for removable coupons.¹⁰ The removable coupons can by made from any machinable material. The bottom of the rotating disk contains a bar magnet to allow disk rotation to create liquid surface shear across surface-flush coupons. The entire disk containing 18 coupons is placed in a 1000 mL glass side-arm reactor vessel. A liquid growth media is circulated through the vessel while the disk is rotated by a magnetic stirrer. The coupons are removed from the reactor vessel and then scraped to collect the biofilm sample for further study or microscopy imaging. Rotating disc reactors are designed for laboratory evaluations of biocide efficacy, biofilm removal, and performance of anti-fouling materials.^9,11,12,13Download video file.^{(49M, mov)}     

Estimation of the biofilm formation ability of Pseudomonas putida in discrete samples from continuous culture

Summary Test systems were set up in order to evaluate the ability of biomass from a continuous culture to form biofilms. A film-forming strain of Pseudomonas putida was used as the test organism. The adsorption of resting cells onto glass surfaces was measured in specially designed chambers containing 1 ml of cell suspension. Both the quantity and the physiological activity of the adsorbed cells, in terms of optical density after detachment and pH change of a substrate exposed to the adsorbed cells, were measured. The analysis of biomass from continuous cultures of Pseudomonas putida verified the suitability of the methods. Furthermore, other properties of importance to biofilm formation such as hydrophobicity and flocculation capacity of the cells were investigated.It was shown for samples deriving from different dilution rates that the cell adsorption rate drastically increased at dilution rates higher than the _max of the culture. Simultaneously, higher values of hydrophobicity and flocculation capacity were observed.It was also shown that the age and thickness of the biofilm subsequently produced in the continuous culture influenced the metabolic activity per unit of biomass attached to the surface. The methods described in this investigation may facilitate the study of parameters important to biofilm formation as well as the metabolic activity of the attached biomass.     

Regulation of methylamine and formaldehyde metabolism in Arthrobacter P1

The regulation of methylamine and formaldehyde metabolism in Arthrobacter P1 was investigated in carbonlimited continuous cultures. To avoid toxic effects of higher formaldehyde concentrations, formaldehyde-limited cultures were established in smooth substrate transitions from choline-limitation. Evidence was obtained that the synthesis of enzymes involved in the conversion of methylamine into formaldehyde and in formaldehyde fixation is induced sequentially in this organism. Compared to growth with methylamine the molar growth yield on formaldehyde was approximately 30% higher. This difference is mainly due to the expenditure of energy for the uptake of methylamine from the medium.The addition of a pulse of a heterotrophic substrate, glucose or acetate, to C₁ substrate-limited continuous cultures resulted in relief of carbon limitation and transient synthesis of increasing amounts of cell material. Concomitantly, a significant decrease in the specific activities of hexulose phosphate synthase was observed. However, the total activity of hexulose phosphate synthase in these cultures remained clearly in excess of that required to fix the formaldehyde that became available in time. The observed strong decrease in the specific activities of this RuMP cycle enzyme strongly suggests that its synthesis is controlled via catabolite repression exerted by the metabolism of heterotrophic substrates.Abbreviations HPS 3-Hexulose-6-phosphate synthase - HPI 3-hexulose-6-phosphate isomerase - RuMP ribulose monophosphate     

Physiology of biofilms of thermophilic bacilli—potential consequences for cleaning

Thermophilic Bacillus species readily attached and grew on stainless steel surfaces, forming mature biofilms of >10^6.0 cells/cm² in 6 h on a surface inoculated with the bacteria. Clean stainless steel exposed only to pasteurized skim milk at 55 °C developed a mature biofilm of >10^6.0 cells/cm² within 18 h. When bacilli were inoculated onto the steel coupons, 18-h biofilms were 30 m thick. Biofilm growth followed a repeatable pattern, with a reduction in the numbers of bacteria on the surface occurring after 30 h, followed by a recovery. This reduction in numbers was associated with the production of a substance that inhibited the growth of the bacteria. Variations in the environment, including pH and molarity, affected the viability of the cells. Chemicals that attack the polysaccharide matrix of the biofilm were particularly effective in killing and removing cells from the biofilm, demonstrating the importance of polysaccharides in the persistence of these biofilms. Treatment of either the biofilm or a clean stainless steel surface with lysozyme killed biofilm cells and prevented the attachment of any bacteria exposed to the surface. This suggests that lysozyme may have potential as an alternative control method for biofilms of these bacteria.     

Evaluation of a model for the effects of substrate interactions on the kinetics of reductive dehalogenation

The effects of primary electron-donor and electron-acceptor substrates on the kinetics of TCA biodegradation in sulfate-reducing and methanogenic biofilm reactors are presented. Of the common anaerobic electron-donor substrates that were tested, only formate stimulated the TCA biodegradation rate in both reactors. In the sulfate-reducing reactor, glucose also stimulated the reaction rate. The effects of formate and sulfate on TCA biodegradation kinetics were analyzed using a model for primary substrate effects on reductive dehalogenation. Although some differences between the model and the data are evident, the observed responses of the TCA degradation rate to formate and sulfate were consistent with the model. Formate stimulated the TCA degradation rate in both reactors over the entire range of TCA concentrations that were studied (from 50 g TCA/L to 100 mg TCA/L). The largest effects occurred at high TCA concentrations, where the dehalogenation kinetics were zero order. Sulfate inhibited the first-order TCA degradation rate in the sulfate-reducing reactor, but not in the methanogenic reactor. Molybdate, which is a selective inhibitor of sulfate reduction, stimulated the TCA removal rate in the sulfate-reducing reactor, but had no effect in the methanogenic reactor.     

On the biosynthesis of 5-hydroxybenzimidazolylcobamide (vitamin B12-factor III) in Methanosarcina barkeri

Exogenous 5-hydroxy-[2-¹⁴C]benzimidazole was transformed by Methanosarcina barkeri into 5-hydroxy-[2-¹⁴C]benzimidazolylcobamide. Thereby the endogenous biosynthesis of 5-hydroxybenzimidazole was completely blocked.Benzimidazole and 5,6-dimethylbenzimidazole were used by M. barkeri to form benzimidazolylcobamide respectively 5,6-dimethylbenzimidazolylcobamide (vitamin B₁₂), but in these cases the endogenous biosynthesis of factor III was not completely suppressed.With [2-¹⁴C]benzimidazole it was demonstrated that this base as well as the benzimidazolylcobamide formed thereof are no precursors in the biosynthesis of 5-hydroxybenzimidazolylcobamide.Glycine instead was found to be a building block for the biosynthesis of 5-hydroxybenzimidazole, since radioactivity from [1-¹⁴C] and [2-¹⁴C]glycine was incorporated, into the base moiety of factor III, but not into its corrin moiety. With [1-¹³C]glycine and ¹³C-NMR-spectroscopy it was shown that C-1 of glycine gets C-3a of 5-hydroxybenzimidazole.[1-¹³C]glycine also led to a single prominent signal in the ¹³C-NMR-spectrum of coenzyme F₄₂₀, this was assigned to C-10a.Thus C-1 of glycine was incorporated into the hydroxybenzene part of 5-hydroxybenzimidazole, whereas it was not incorporated into this part of coenzyme F₄₂₀, indicating that the hydroxybenzene part of these two compounds is not formed from a common intermediate. L-[U-¹⁴C]glutamate led to the exclusive labeling of the corrin ring of factor III, showing that the corrin precursor 5-aminolevulinic acid is formed by the C-5 pathway in M. barkeri.These experiments indicate that the biosynthesis of factor III in the archaebacterium M. barkeri is similar to the corrinoid biosynthesis in the anaerobic eubacteria Eubacterium limosum, Clostridium barkeri, and Clostridium thermoaceticum.     

In vitro antibiofilm and anti‐adhesion effects of magnesium oxide nanoparticles against antibiotic resistant bacteria

The aim of the current investigation was to determine the antibacterial and antibiofilm potential of MgO nanoparticles (NPs) against antibiotic‐resistant clinical strains of bacteria. MgO NPs were synthesized by a wet chemical method and further characterized by scanning electron microscopy and energy dispersive X‐ray. Antibacterial activity was determined by broth microdilution and agar diffusion methods. The Bradford method was used to assess cellular protein leakage as a result of loss of membrane integrity. Microtiter plate assay following crystal violet staining was employed to determine the effect of MgO NPs on biofilm formation and removal of established biofilms. MIC values ranged between 125 and 500 μg/mL. Moreover, treatment with MgO NPs accelerated rate of membrane disruption, measured as a function of leakage of cellular proteins. Leakage of cellular protein content was greater among gram‐negative bacteria. Cell adherence assay indicated 25.3–49.8% inhibition of bacterial attachment to plastic surfaces. According to a static biofilm method, MgO NPs reduced biofilm formation potential from 31% to 82.9% in a time‐dependent manner. Moreover, NPs also significantly reduced the biomass of 48, 72, 96 and 120 hr old biofilms (P < 0.05). Cytotoxicity experiments using a neutral red assay revealed that MgO NPs are non‐toxic to HeLa cells at concentrations of 15–120 μg/mL. These data provide in vitro scientific evidence that MgO NPs are effective and safe antibiofilm agents that inhibit adhesion, biofilm formation and removal of established biofilms of multidrug‐resistant bacteria.