Multimodal biofilm control strategies for spacecraft water systems: Evaluating coatings, nutrient removal, and biocides for improved sustainability
Categoria dell'articolo: Research Note
Pubblicato online: 14 set 2025
Pagine: 75 - 89
DOI: https://doi.org/10.2478/gsr-2025-0005
Parole chiave
© 2025 Madelyn K. Mettler et al., published by Sciendo
This work is licensed under the Creative Commons Attribution-NonCommercial-NoDerivatives 3.0 License.
In space, as on Earth, water is necessary for human life. To achieve sustainable spaceflight and human presence in space, water must be recycled from urine, sweat, and humidity in the spacecraft. The systems responsible for recycling this water are especially vulnerable to damage and failure due to biofilm accumulation (Carter, 2010; Zea et al., 2020; Zea et al., 2018). As space exploration moves into a new era of commercial space stations and a government station to orbit the moon (Gateway), special considerations must be made regarding the design of water recycling systems and their susceptibility to biofilm-related issues.
Biofilms are microbial communities that are often associated with surfaces. They can be comprised of a multitude of organisms, extracellular polymeric substances (EPS), and environmental debris such as dirt (Donlan, 2002; Flemming et al., 2007; Wingender and Flemming, 2011). The biofilm morphology confers many advantages to microorganisms such as increased antimicrobial resistance, opportunities for horizontal gene transfer, and protection from environmental stresses like biocides, osmotic lysis, desiccation, UV radiation, and starvation (Elasri and Miller, 1999; Esbelin et al., 2018; Mah and O'Toole, 2001; Roberson and Firestone, 1992; Yin et al., 2019). These properties make biofilms particularly difficult to mitigate, especially in areas that are difficult to manually and mechanically clean, as those found in a spacecraft.
Many strategies have been proposed for controlling biofilm in spacecrafts, and specifically in spacecraft water systems including coated surfaces, predatory organisms, biocides, mechanical disaggregation, UV sterilization, thermal shock treatments, and nutrient removal (Azim et al., 2020; Velez Justiniano et al., 2020; Zea et al., 2020). Other researchers have investigated the use of coatings for biofilm control in spacecraft water systems (Demir et al., 2022; Flores et al., 2023; Li Sip et al., 2023; Mettler et al., 2022), but to our knowledge, none have explored the effects of coatings in combination with other biofilm control strategies. The experiments presented in this paper explore the use of a surface coating, biocide addition, and key nutrient removal, in combination and as individual methods to control biofilms composed of organisms from the ISS water system. The coating tested was Sher-Loxane® 800, a commercially available coating from Sherwin-Williams and it was tested in combination with silver fluoride dosing (biocide) and removal of phosphorus from the nutrient medium. Further, the research presented here uniquely features a multidomain consortium of organisms, all isolated from the International Space Station (ISS) water system. The previously published studies all used a singular organism,
The ISS serves as the test bed for future spacecraft and space stations. As such, all the methods used in this paper were developed with the National Aeronautics and Space Administration (NASA) portion of the ISS water system and recovery protocols in mind. While these experiments were designed to represent biofilms in the ISS, the results have broad implications for biofilm control on Earth as well. Researchers investigating biofilm control in Earth-based water systems have also explored coatings for biofilm reduction (Filice et al., 2022; Samuel et al., 2022; Si et al., 2015; Sójka et al., 2023). However, the published studies did not investigate the combined effects of coatings and biocides (or nutrient limitation) for biofilm control, despite the frequent use of biocides for water treatment and distribution (Hwang et al., 2012; Munavalli and Kumar, 2003; Pan et al., 2023). The research presented here suggests that incorporation of multiple methods of biofilm control leads to promising reduction of biofilm in an analogue to the ISS wastewater tank, which could be reproduced for Earth-based water systems.
The organisms used in the experiments are direct and frequent isolates from the ISS water system (Zea et al., 2020), and are a subset of the organisms selected by Velez Justiniano et al. for their previous monoculture work (2021). Three bacteria and one fungus were used in co-culture for all experiments conducted and include the bacteria
Inconel® 718 (a nickel-chromium alloy) and TeflonTM (polytetrafluoroethylene) cylindrical coupons (12.7 mm diameter, 3.8 mm thickness) were procured (BioSurface Technologies; Bozeman, MT). Prior to coating or use in the reactor, coupons were washed by soaking and sonication in soapy water for approx. 5 min followed by a rinse step and additional sonication of approx. 5 min in Milli-Q water (resistivity 18.2 MΩ·cm). The coating tested was provided by The Sherwin-Williams Company (Cleveland, OH) and is a commercially available product known as Sher-Loxane® 800, product numbers B80W501 (extra white) and B80V500 (standard temperature hardener). The coating was applied with a paintbrush such that a homogenous thickness of coating was present on the flat surface of the coupon (Figure 1). After at least 48 h of drying at room temperature, the coupon was flipped over so the other flat surface could be coated with the freshly mixed coating. The round edges of the coupons were not coated, but the painted coating dripped over the side in some areas. No additional wash step was completed after coating. Contact angles were measured for uncoated and coated surfaces with a VCA 2500 XE system and surface topography was measured with a Bruker Dektak stylus profilometer (Chi et al., 2015) (Supplemental Table 2).

Coupons for sampling biofilm accumulation in the CDC reactor.
CDC biofilm reactors (BioSurface Technologies) were assembled and sterilized empty in an autoclave at 121 C and 21 PSI for at least 30 minutes. Uncoated coupons were loaded before the reactor was autoclaved (8 rods loaded with 3 coupons per rod). For experiments that utilized coated coupons, the reactor was autoclaved without coupons. After autoclaving, coated coupons were loaded and sterilized using the same method outlined previously (Mettler et al., 2022). In summary, the reactor was placed in a Labconco class II biosafety cabinet, coupon holder rods were removed, coated coupons were loaded, and then rods were submerged in 99% isopropanol for at least 30 s before air drying and replacement into the reactor.
The medium used in the experiments was developed by researchers at the Center for Biofilm Engineering (CBE) in collaboration with MSFC (Table 1). The medium was designed to mimic the ISS wastewater tank nutrient levels and chemical composition (50% influent from humidity condensate and 50% influent from urine distillate) during a biofouling event. An early version of the recipe was published by Velez-Justiniano et al. (2021). Slight modifications were made to the formulation, including the addition of minor/trace nutrients (MTN), removal of KCl, and reduction of KI concentrations (Sandvik et al., 2022). The new version of the medium was termed microbial ersatz MTN. To prepare the medium, Milli-Q water was autoclaved for 3 h in 20 L glass carboys. After autoclaving, filter sterilized stock solutions were added to the carboy. A 10 mL aliquot of medium was removed from the carboy with a sterile serological pipette for measuring pH. The pH was adjusted on the aliquot to 5.55 ± 0.05 with hydrochloric acid (1 M) or sodium hydroxide (1 M) and scaled to adjust the medium in the carboy. Sterile HCl or NaOH was added to the carboy and the pH was checked again. The iterations tested in the experiments here include a full-strength version of microbial ersatz MTN and a no phosphorus version which excluded the phosphate stock. The no phosphorus medium was prepared in carboys that had not held full strength medium, or if they had, they were acid washed with 10% HCl and rinsed thoroughly with Milli-Q water.
Recipe for microbial ersatz MTN featuring final component concentrations.
Propylene Glycol | 8.971 | μL/L | Benzyl Alcohol | 6.075 | μL/L |
Ethanol | 44.946 | μL/L | Diethylphthalate | 2.01 | μL/L |
Acetone | 25.799 | μL/L | Trimethyl Silanol | 0.635 | μL/L |
2-(2-butoxyethoxy) Ethanol | 2.356 | μL/L | Benzothiazole | 0.21 | μL/L |
N, N-Dimethylformamide | 1.486 | μL/L | 2-Ethyl-1-Hexanol | 0.48 | μL/L |
2-Ethoxyethanol | 1.303 | μL/L | Decamethylcyclopentasiloxane | 1.03 | μL/L |
1-Methyl-2-Pyrrolidinone | 0.782 | μL/L | Dodecamethylcyclohexasiloxane | 10 | μL/L |
2-Propanol | 0.896 | μL/L | Octamethylcyclotetrasiloxane | 1.02 | μL/L |
1-Propanol | 0.876 | μL/L | Dimethoxydimethylsilane | 35.1 | μL/L |
4-Ethylmorpholine | 2.265 | μL/L | Calcium Sulfate | 1.885 | mg/L |
Formic Acid | 27.489 | μL/L | Dimethyl Sulfone | 0.205 | mg/L |
Lactic Acid | 8.55 | μL/L | Hexamethylcyclotrisiloxane | 1.02 | mg/L |
Benzoic Acid | 3.015 | mg/L | Monobasic Potassium phosphate | 0.835 | mg/L |
Caprolactam | 1.111 | mg/L | Magnesium chloride hexahydrate | 0.397 | mg/L |
Urea | 1.899 | mg/L | Manganese chloride tetrahydrate | 0.319 | mg/L |
Zinc (II) Acetate dihydrate | 1.425 | mg/L | Ferric chloride | 0.129 | mg/L |
Nickel (II) Acetate tetrahydrate | 0.518 | mg/L | Boric acid | 0.268 | mg/L |
Acetic Acid | 32.088 | μL/L | Cobalt chloride hexahydrate | 0.004 | mg/L |
Ammonium Bicarbonate | 101.457 | mg/L | Sodium molybdate dihydrate | 0.016 | mg/L |
Sodium Fluoride | 0.88 | mg/L | |||
Potassium Iodide | 0.021 | mg/L |
Silver (I) fluoride (99+%, Thermo Scientific) was used in experiments featuring biocide dosing. The biocide was prepared at a concentration of 216.66 mg/L so that when it was added to the reactor, it was present at a concentration of 2 ppm. The silver (I) fluoride was added to Milli-Q water and filter sterilized into a sterile container with tubing connected to the reactor.
The CDC reactor experiments were conducted to evaluate control strategies alone and in combination with one or two other control strategies. Three biological replicates of each experiment were completed. Figure 2 presents a schematic to visualize the iterations of each experiment. The format of Figure 2 is carried through the data and microscopy figures that present the results of the experiments.

Biofilm control methods used in each of the eight iterations of experiments. The empty section in the upper left represents the base condition of unmitigated biofilm growth. This layout is used throughout the results to present data for each experiment.
Sterile reactors loaded with coupons were filled to the effluent port with fresh, sterile medium (approx. 325 mL). For inoculation, 100 μL of each washed culture was added to the reactor and the stir bar was set to 125 ±10 rpm. The full consortium was used for each experiment and computational fluid dynamics models indicate the stir rate resulted in shear stresses of 0.365 +/− 0.074 Pa across the surfaces of all 24 coupons (Johnson et al., 2021). Experiments took place at room temperature and with ambient oxygen concentrations. About 5–10 min after inoculation, a sample of bulk fluid was taken from the reactors to validate the cell concentrations at the start of the experiments via viable plate counts.
After 24 h batch operation, continuous flow was initiated. Fresh, sterile medium was pumped (Masterflex L/S, Cole Parmer) into the reactor at 2 mL/min, creating a residence time of about 162 min. The medium used for continuous flow was the same as that used for the batch phase operation. For reactors receiving biocide, the first dose corresponded with the initiation of continuous flow, and silver fluoride was dosed every 24 h at 3 mL/min for 1 min.
The first sampling point took place at the completion of 24 h batch conditions, just prior to the start of continuous flow. Sampling consisted of removing a reactor rod and gently dipping it into 30 mL of sterile 1M phosphate buffered saline (PBS). After rinsing, the coupons were removed and put into sterile 50 mL Falcon tubes containing 10 mL sterile PBS. The biofilm was removed from the coupon surface and disaggregated via a vortex mixing and sonication series of 30 s each for a total of 2 min 30 s (vortex, sonicate, vortex, sonicate, vortex). For Days 1, 3, and 5, three coupons were sampled for viable plate counts of attached biofilm. For Day 7, two coupons were sampled for plate counts and one was sampled for microscopy. Planktonic samples were taken with a sterile serological pipette from the open port on the CDC reactor where the rod was removed. The rod was then replaced with a sterile dummy rod to maintain similar fluid dynamics in the reactor. Bulk reactor fluid was also sampled 6 h after the biocide dose in experiments that received silver fluoride to monitor effects of the silver fluoride dose on planktonic populations. Planktonic samples were vortex mixed for 30 s to disaggregate potential biofilm aggregates. Disaggregated biofilm and planktonic samples were plated on selective agar for enumeration (see Table 2 for the agar used). Agar plates were allowed to dry at room temperature before placing them into a 30 C incubator. Enumeration took place after the formation of visible colonies, typically after 2 days for general counts,
Selective agar used for microbial enumeration of planktonic and biofilm samples.
Sabouraud dextrose agar, pH lowered to 3 | |
R2A with chloramphenicol (20 μg/mL) and amphotericin B (7.5 μg/mL) | |
No isolation, general counts | R2A |
During Day 7 sampling, coupons were stained for confocal analysis. After gently rinsing in PBS, coupons were placed into sterile 24-well plates. The well was then flooded with freshly prepared LIVE/DEADTM BacLightTM stain and incubated in the dark for 15 min at room temperature. The stain was removed from the well and the coupons were washed three times with filter-sterilized Milli-Q water. Next, the well was flooded with a 50/50 solution of sterile 1X PBS and Calcofluor White and incubated in the dark for 10 min at room temperature to stain fungal cells. After the incubation period, the stain was removed, and the coupons were washed with filter-sterilized Milli-Q water three times. The wells were then flooded with a solution of 4% paraformaldehyde and 2.5% glutaraldehyde. The 24-well plate was covered with a foiled lid and wrapped several times with parafilm. The wrapped plate was then placed into a closed plastic bag and stored at 4 C until confocal microscopic imaging at excitation wavelengths of 405 nm, 483 nm, and 568 nm on a Leica DM6 Multiphoton Upright Confocal Microscope. At least four random positions on each coupon were imaged from each biological replicate. The published images are a single field of view representative of all biological replicates.
The effects of Sher-Loxane® 800, phosphorus removal, and silver fluoride dosing were evaluated on a species-by-species basis. To investigate the effects on the entire biofilm and planktonic community, the viable plate counts on the non-selective R2A plates were used. Mixed effects ANOVA models and statistical comparisons were generated using MiniTab (version 21.1).
The viable biofilm densities are presented in Figure 3. The average of the three biological replicates is presented in the graphs and consisted of three technical replicates each for Days 1, 3, and 5 (n=9 coupons total), and two technical replicates each for Day 7 (n=6 coupons total).

Viable biofilm density for each of the eight iterations of biofilm control combinations. Continuous flow was initiated on Day 1 after the sample was taken. The grey dashed line represents the limit of detection, y=1.69. Error bars are standard deviation.
The experiments featuring unmitigated biofilm growth (no coating, full strength medium, and no biocide; Figure 3A) fostered the highest viable biofilm density of all the experiments.
In experiments featuring the no phosphorous medium as the only method of biofilm control (Figure 3B), the general trend is a reduction in viable biofilm density by 0.5–1 log10CFU/cm2. The experiments with silver fluoride dosing as the sole method of biofilm control (Figure 3C) featured a reduction in viable biofilm density from Day 1 to Day 3 (biocide was dosed on Day 1 immediately after sampling).
The experiments on uncoated coupons with nutrient limitation and biocide as the biofilm control methods (Figure 3D) featured a reduction of about 0.5 log10CFU/cm2 in
The coated coupons effectively delayed viable biofilm accumulation by several orders of magnitude for at least three days after inoculation (Figure 3E vs 3A). This delay presented an excellent opportunity for additional control methods to further suppress biofilm accumulation. The final viable biofilm density was similar to the unmitigated case, reaching approx. 8.0 log10CFU/cm2 for
Mirroring the comparison between Figure 3A and 3B, the inclusion of nutrient limitation as a biofilm mitigation method on coated coupons (Figure 3F) reduced viable biofilm accumulation by approx. one order of magnitude compared to biofilms with the coating as the only method of biofilm control (Figure 3E).
The greatest reduction in biofilm accumulation occurred when silver fluoride dosing was incorporated as a biofilm control method with the coating (Figure 3G) and when all three strategies were implemented together (Figure 3H). In these experiments, the biofilm density was significantly reduced on Day 1 compared to the unmitigated case (Figure 3A) and the density was generally highest on Day 1. Throughout the experiments, the biofilm density remained low, aside from
Mixed effects statistical analysis was fit to the log-transformed CFU data to investigate the resulting viable biofilm density in each treatment method more definitively. The species were evaluated individually, and the biofilm was evaluated as a whole, using counts from the R2A agar plates. The ANOVA models used the experiment replicate as a random factor, and medium, biocide, coating, material, and day all as fixed factors. The p-values associated with the mixed effects F-tests for most individual factors are presented in Table 3, see Supplementary Table 3 for all remaining p-values.
P-values for statistical significance of individual factors comparing viable cell densities of the accumulated biofilms. Bolded values represent those less than 0.05, indicating the factor had a significant impact on viable biofilm accumulation of the organism. Table key: No P: no phosphorus medium; FS: full strength medium; AgF: silver fluoride biocide; Inc: Inconel; Tef: Teflon; SL: Sher-Loxane 800 coating; and Unc: uncoated.
Medium (No P < FS) | 0.0556 | ||||
Biocide (AgF < No biocide) | |||||
Material (Inc < Tef) | 0.9930 | ||||
Coating (SL < Unc) |
Additionally, follow-up Tukey pairwise comparisons were performed for the three-way interactions of medium, biocide, and coating. These specific comparisons were performed as they were the biofilm control methods investigated. The Tukey pairwise comparisons for biofilm densities are presented in Supplementary Table 4. The comparisons indicate that for
In addition to biofilm measurements, bulk fluid samples from the reactors were taken to monitor the reactor planktonic populations. The averages of the three biological replicates are presented in Figure 4. The planktonic populations generally mirror the trends observed in the viable biofilm accumulation (Figure 3) in all reactors aside from those treated with silver fluoride. In the reactors receiving biocide (3 mL in 60s every 24 h), the planktonic population was significantly reduced and there was a cyclical suppression and rebound of viable planktonic (detached biofilm) cells. Mixed effects statistical analysis was fit to the log-transformed CFU data to more definitively investigate the resulting viable planktonic cell density in each treatment method. The models used the experiment replicate as a random factor, and medium, biocide, coating, and day were all fixed factors. The material type was not included as a factor in planktonic analysis because both Teflon and Inconel were present in the same reactor. The p-values associated with the F-tests for all individual factors are presented in Table 4, see Supplementary Table 5 for all remaining p-values.

Viable planktonic cell density for each of the eight iterations of biofilm control combinations. Continuous flow began on Day 1 after the sample was taken. The grey dashed line represents the limit of detection, y=1.3. Error bars represent standard deviation.
P-values for statistical significance of individual fixed factors comparing viable cell densities of the planktonic cells in the reactor fluid. Bolded values are less than 0.05, indicating the factor had a significant impact on the viable planktonic density of the organism. Table key: No P: no phosphorus medium; FS: full strength medium; AgF: silver fluoride biocide; SL: Sher-Loxane 800 coating; and Unc: uncoated.
Medium (No P < FS) | 0.9320 | ||||
Biocide (AgF < No biocide) | |||||
Coating (SL < Unc) | 0.2827 |
Tukey pairwise comparisons were also performed for the three-way interaction of media, biocide, and coating presence in the reactor. The comparisons are present in Supplementary Table 6. Results indicate that the biofilm control methods had minimal effect on the planktonic densities of
Confocal microscopy images were generated for biofilms that had accumulated on the coupons after seven days in the reactors. Figures 5 and 6 present 3D projections of these images for Inconel and Teflon surfaces, respectively. The greatest reduction in biofilm accumulation can be seen when comparing panels C and D to G and H in Figures 5 and 6. Panel E in each figure presents biofilms on Sher-Loxane 800® coating grown in full strength medium without biocide dosing. The biofilms appear much denser than those grown on uncoated coupons (panel A), however, some of the fluorescence in the Sher-Loxane 800® images is due to the coating itself. The coating became highly fluorescent in the wavelengths used to image the biofilm (excitation wavelengths of 405 nm (blue), 483 nm (green), and 568 nm (red)) and appears in different false colors due to image processing to improve visibility of the cells on the surface. The microbial cells present on the coating have more intense fluorescence than the coating, so the cells remain distinguishable from the surface.

Confocal images of biofilms accumulated on Inconel CDC coupons seven days after inoculation. Viable bacterial cells are in green, non-viable bacterial cells are in red, and fungal cells are in blue. The fluorescence of the coating can be seen in the three images on the lower right. The scale bar for each image is 30 μm.

Confocal images of biofilms accumulated on Teflon CDC coupons seven days after inoculation. Viable bacterial cells are in green, non-viable bacterial cells are in red, and fungal cells are in blue. The fluorescence of the coating can be seen in the three images on the lower right. The scale bar for each image is 30 μm.
Side views of the tallest portion of the biofilm presented in Figures 5 and 6 are provided for biofilms grown in full strength medium without biocide dosing to provide additional context regarding biofilm structure that may be lost in the 3D projections (Figure 7). It can be seen that the biofilms on the uncoated coupons (panels A and C) had a much larger maximum thickness than those on the Sher-Loxane 800® coated coupons (panels B and D).

Side views of tallest segments of biofilms on A) uncoated Inconel, B) coated Inconel, C) uncoated Teflon, and D) coated Teflon grown in full strength medium without biocide dosing. Scale bar in each image is 30 μm.
Coatings have previously been investigated for biofilm control for use in spacecraft water systems by Mettler et al. (2022), Flores et al. (2023), Demir et al. (2022), and Li Sip et al. (2023). These previous investigations, while limited in scope and relevance to the ISS water system, confirmed that coatings can decrease unwanted biofilm accumulation. The results presented in this paper build on previously published results (Mettler et al., 2022) with key methodology changes to improve model accuracy to conditions in the ISS wastewater tank. Here, the use of a multi-organism consortia, including a fungus, is a characteristic that has not been addressed in previous research using coatings for biofilm control in spacecraft water systems. Further, these experiments aim to improve accuracy of modeling the ISS water system by utilizing the microbial ersatz MTN medium designed to mimic nutrient availability and chemical composition of the wastewater tank that may lead to a biofouling event (Sandvik et al., 2022). These changes are more realistic and significantly improve upon the use of tryptic soy broth and potato dextrose broth tested in previous experiments (Mettler et al., 2022). One characteristic that remained constant between the early experiments and the ones described here is the use of materials found in the ISS water system (Callahan et al., 2007), though here the materials were reduced to only Teflon and Inconel (the material that composes the wastewater tank). The final improvement made to the experiments is the extension of the duration from 3 days to 7 days. Within that time frame, the biofilms within the CDC reactor generally seem to achieve steady state.
While not reflective of the low shear environments found in the ISS (generally lower than 1 mPa), the CDC reactor offers a relatively high-throughput method of evaluating biofilm control strategies. As shear tends to induce biofilm formation (Peyton and Characklis, 1993; Tsagkari et al., 2022), the higher shear environment of the CDC reactor allows for biofilm formation and evaluation on shorter timescales, facilitating the investigation of many experimental iterations. Further, the CDC reactor offers experimental flexibility, with all three methods of biofilm control being implemented with minimal alteration to the reactor and its operating method. The CDC reactor was operated with a batch phase followed by a continuous flow phase as is typical according to the American Society for Testing and Materials' standard method (ASTM, 2021). The flow rate during continuous flow phase for a reactor like the CDC should be fast enough to prevent replication of the organisms in the planktonic phase (i.e., residence time shorter than doubling time), inducing biofilm formation. The residence time here was 2.7 h, and the doubling time of the organisms in monoculture was determined to be approx. 1.9–11 h. However, the doubling times in the CDC reactor were likely longer due to the organisms being present in consortium and the lower nutrient concentrations associated with continuous flow operation. As such, any replication of the organisms in the bulk fluid of the reactor was likely minimal, effectively selecting for biofilm formation.
The coating tested in these experiments was Sherwin-Williams Sher-Loxane® 800. It is an “epoxy siloxane hybrid designed for corrosion control and weatherability.” There are no specific agents added to the coating to make it antimicrobial or biocidal. It was chosen in these experiments based on its performance in preliminary screening of multiple antimicrobial coatings (data not shown) and as a general antifouling coating with the basic mechanism of action of reducing microbial adhesion. As an epoxy-based coating, there may be concerns regarding the safety of the water that passes through the system for crew consumption. Additional downstream processing steps could be necessary to remove potential contaminants. Further testing of the coating for human compatibility or the creation of a new coating that produces similar results is necessary.
Phosphorus was identified as a major limiting nutrient during the development of the microbial ersatz MTN medium (Sandvik et al., 2022) and has been reported as a limiting nutrient in the ISS water processing assembly (WPA) (Diaz et al., 2021). Phosphorus is pervasive in biomolecular processes, lending to its capacity as a limiting nutrient (Elser, 2012). In spacecraft, phosphorus may be removed using nutrient filters, resins, or biological methods such as plant growth—all of which would need external validation for incorporation into the water system. As can be seen in Figure 3, the removal of phosphorus generally tended to reduce viable biofilm accumulation by a half a logarithm to a full order of magnitude with the planktonic densities mirroring that trend (Figure 4).
Silver has long been used to control microorganisms, whether in textiles (Radetić, 2013), material coatings (Knetsch and Koole, 2011; Schierholz et al., 1998), or as a biocide (Sim et al., 2018). It has broad antimicrobial effects including interaction with membrane proteins, disruptions of electron transfer and respiration, interactions with DNA and proteins, and generation of reactive oxygen species (Li et al., 2018). Many experiments investigating silver compatibility in spacecraft systems have been conducted (Adam, 2009; Beringer et al., 2014; Callahan et al., 2007; Petala et al., 2016; Petala et al., 2017; Roberts et al., 2007; Wallace et al., 2016; Wallace et al., 2017), and NASA has expressed interest in moving away from iodine treatment towards silver treatment for potable water (Li et al., 2018). The use of silver fluoride at 2 ppm was determined based on unpublished results from the CBE investigating a wide range of biocides for use in spacecraft water systems. The daily dosing of silver fluoride to the reactors effectively suppressed additional biofilm accumulation during the continuous flow phase. In the ISS water system, reducing planktonic cell density is a key goal in addition to reducing biofilm density because planktonic cells (and/or detached biofilm clumps) can cause clogging issues downstream in the water recovery process. Also, planktonic cells can serve to inoculate surfaces within the wastewater tank (represented by the CDC reactor) or further downstream, leading to additional biofilm formation.
Combining the coating, a daily silver fluoride dosing, and phosphorus removal resulted in the lowest viable biofilm accumulation, ultimately leading to a biofilm total cell density of 1.74 log10CFU/cm2 (Inconel) and 1.77 log10CFU/cm2 (Teflon) at seven days, which is just above the limit of detection of 1.69 log10CFU/cm2. None of the control methods alone came anywhere near this level of biofilm reduction. Testing all three biofilm control methods alone and in combination with each other was important to show that under the conditions tested, good biofilm control will almost certainly not be achieved by one method alone.
In spacecraft water systems, the goals of biofilm control extend beyond logarithmic reduction of viable microbial cells. The accumulation of biofilm and biofilm detachment (even dead cells) contributes to the potential clogging of valves and pipes. As such, it is important to evaluate the biofilm thickness and morphology in addition to the viable cells within. To investigate the biomass and overall clogging potential of the biofilms in various states of control, confocal imaging provides important insight.
Figures 5 and 6 feature representative confocal images of the biofilms after seven days in CDC reactors for each of the eight iterations of experiments conducted. The uncoated Inconel coupons (Figure 5) seemed to foster thinner, near monolayer, biofilms with fewer large aggregates than the uncoated Teflon coupons (Figure 6), which aligns with the viable biofilm density data (Figure 3). However, when the coating was utilized, there were minimal differences in biofilm morphology (or density) between Inconel and Teflon, which is also supported by the CFU data (Figure 3). Figure 7 shows the differences in thickness for all the biofilms grown in full strength microbial ersatz MTN and without biocide dosing. This figure was generated by finding the x-slice of the confocal images in Figures 5 and 6 with the tallest segment of biofilm. Despite the general monolayer biofilm morphology on uncoated Inconel (Figure 7A), the clump of biofilm in the image results in a biofilm with a larger maximum thickness than the biofilms on Sher-Loxane® 800 coated coupons. These tall clumps of biofilm are concerning for their potential for sloughing off and clogging pipes. The clogging potential is even more drastic with the uncoated Teflon biofilm (Figure 7C).
A key morphological difference between biofilms on the uncoated and coated coupons was the presence and absence of fungal hyphae, respectively. On the uncoated coupons, especially on Teflon, fungi were present in the hyphal (filamentous) morphology. The hyphae add significant height to the biofilm, sometimes upwards of 200 μm as can be seen in Figure 7C and add additional surface area for bacterial colonization. Both viable and non-viable bacteria (green and red, respectively) appear to have colonized the fungal hyphae (blue) in Figure 7C. The increased height further enhances clogging potential in small diameter pipes and valves like those found in spacecraft water systems. The additional surface area provided by the hyphae for bacterial colonization means that any treatment present at the substratum (such as a coating) would not be effective against bacteria colonizing the hyphae. For this reason, it is especially encouraging that this coating fostered minimal fungal cell attachment, and that the fungal cells present were in the conidial morphology (Figures 5 and 6, lower right corner).
Some methods used in this study are similar to those reported by Velez Justiniano et al. (2021), such as a subset of the organisms investigated and a modified version of the medium used in their experiments (Sandvik et al., 2022; Velez Justiniano et al., 2021). There has been extensive collaboration between the authors, additional researchers at the CBE, and researchers at MSFC. The results that have been reported by Velez Justiniano et al. (2021) examine relevant organisms (including similar organisms to those used here) as single-species cultures in the planktonic phase. As such, this is the first time to our knowledge, that results of experiments featuring an ISS relevant selection of organisms grown as biofilms in consortium using a relevant medium have been published.
Each of the approaches for biofilm control evaluated in this research have been explored individually by other researchers for spacecraft applications. Four peer-reviewed studies on coatings for use in spacecraft water systems have been published (Demir et al., 2022; Flores et al., 2023; Li Sip et al., 2023; Mettler et al., 2022). All four studies featured
One published study evaluated numerical models of nutrient limitation in the WPA. The researchers evaluated the effects of carbon and phosphorus limitation to understand biofilm accumulation in the WPA during typical operation and potential dormancy conditions (Diaz et al., 2021). The models also investigated the effects oxygen availability would have on open and closed systems. Though the study discusses bacterial metabolism, no specific organisms were listed as the basis of the model and fungal microorganisms were not included, which as reported in the results here, contribute greatly to biomass and biofilm thickness. While the study was an interesting mathematical evaluation, no biological tests were completed to support the reported results.
Several studies examining biocide use for biofilm reduction in spacecraft water distribution systems have been published. A long-term study (3 years) found that iodine dosing showed promising reduction of biofilm as long as concentrations were maintained between 1–3 mg/L (Schultz et al., 1992). The researchers used stainless steel, a relevant material (Callahan et al., 2007), and used non-sterile Milli-Q water as the medium and inoculum. They frequently isolated organisms in the resulting biofilm included
One paper describes a combination of nutrient limitation and biocide dosing for evaluation of dormancy conditions in spacecraft water systems (Beitle et al., 2024). The consortium used in the experiments was very similar to the one used here, but with the addition of
Approaches used in this research could also be used to evaluate biofilm control in Earth-based water systems. It is likely that using organisms relevant to drinking water distribution systems, industrial water systems, or wastewater systems and the use of a medium relevant to the target system could result in similar biofilm reduction when multiple control strategies are combined. Space research can sometimes help inform or inspire applications on Earth, as may be the case here.
These experimental results represent the first time, to our knowledge, a multidomain biofilm has been used in evaluating coatings as a control method in spacecraft water systems. It also represents the first time results have been published using a relevant medium and consortium, and an experiment duration longer than 72 h. Further, this is the first time (to our knowledge) that additional biofilm control methods were tested in combination with coatings for biofilm control in water systems. The results indicate that with these organisms and conditions, a combination of control methods was necessary for effective biofilm mitigation. Each control method—Sher-Loxane® 800 coating, phosphorus removal, and silver fluoride dosing—had individual effects on reducing biofilm accumulation, but the presence of the coated surface was the key to reducing accumulated biofilm to the limit of detection.
While this research was framed within the context of the ISS water recovery system, and more specifically the wastewater tank, the results may extend to water systems on Earth as well. The combined effects of multiple biofilm control methods are under-investigated despite the general understanding of the difficulty of controlling biofilm accumulation.
Building upon this research further, it will be important to extend experiments past 7 days and to incorporate reinoculation of the organisms at regular intervals during the experiment. Further improvements include the incorporation of simulated microgravity as the goal of these biofilm control methods is to reduce biofilm associated risks in spacecraft water systems.