Results-project

This page is dedicated to the achievements of our experiments in the lab. We will focus on key results:

Card introduction

Evaluation of encapsulation beads for dual-strain water treatment

Context: Our bioremediation approach relies on two bacterial strains that cannot be co-cultured due to their different growth rates. To overcome this, each strain was encapsulated separately in activated carbon beads. This strategy allows us to combine the effects of both strains without co-culture, prevents the release of GMOs into the treated water, and leverages the PFAS adsorption capacity of activated carbon. These pilot experiments aim to evaluate the long-term viability of the bacteria within the beads, the potential release of encapsulated strains into water, and the adsorption of PFOA onto the beads.

Bacterial viability is ensured within the beads

Objective: We aimed at testing the viability of both strains over time within the beads to estimate the lifespan of our degradation process.

Method: The release and stability of bacteria were evaluated by incubating dried beads in sterile water (Figure 1), encapsulating either Pseudomonas putida with 10% or 20% activated carbon, or Labrys portucalensis with 20% activated carbon. Control beads without bacteria were also prepared using sterile water instead of bacterial culture.

Figure 1
Figure 1: Pictures of A) dried activated-carbon beads and B) beads in solution.
The production of this support matrix for our strains was carried out at our partner’s headquarter YpHen, in Grenoble (FR).

Supernatant samples were collected at different time points to measure bacterial release, and beads from dedicated tubes were dissolved with 1% tricitrate solution to assess bacterial viability within the beads. Bacterial counts were determined by serial dilutions, plating, and colony forming unit (CFU) enumeration.

Figure 2
Figure 2: Stability and release of encapsulated bacteria over time.
Time course of A) bacterial viability in encapsulated beads and B) bacterial release from encapsulated beads. Samples were incubated at room temperature (25°C) under shaking (200 rpm): Pseudomonas putida (10% and 20% activated carbon, AC), Labrys portucalensis (20% AC), and control beads without bacteria over 30 days.

Results: All strains remained viable and even showed growth for at least 10 days (Figure 2A). Pseudomonas putida in 10% activated carbon beads continued to grow for up to 30 days. Although the other conditions were not tested for the full 30-day period, similar trends are likely. No significant differences in bacterial viability were observed between beads containing 10% or 20% activated carbon, indicating that carbon content does not compromise survival.

Regarding bacterial release, Figure 2B shows that the number of bacteria released into water increases over time, at levels comparable to the bacteria remaining in the beads. This indicates that the current bead formulation is not optimized to retain bacteria. Major adjustments to the formulation will be discussed with YpHen to ensure bacterial confinement and comply with biosafety regulations.

Activated-carbon beads adsorb PFOA from aqueous solutions

Objective: We aimed at testing the efficiency of PFAS removal from aqueous solutions of activated-carbon beads.

Method: The adsorption of PFOA on beads (10% and 20% activated carbon, 10% and 20% talc, and a negative control without beads) was assessed by incubating 1.0 g of beads in a 50 µM PFOA solution.

Figure 3
Figure 3: Evolution of PFOA concentration in presence of beads.
Bacteria-free beads containing activated carbon or talc (● or ▲) at 10% or 20% loading (grey or dark) were incubated at room temperature (25°C) under shaking (200 rpm) in 20 mL of 50 µM PFOA solution. The no-bead negative control is shown in red.

Results: Figure 3 clearly shows a distinct difference in PFOA concentration over time between beads with or without activated carbon, as well as the negative control without beads. The results indicate that beads containing 20% activated carbon adsorbed 90.2% of PFOA within 120 minutes, while those with 10% activated carbon achieved 96.9% adsorption. In contrast, beads containing talc showed much lower adsorption efficiencies, 36.7% for 20% talc and 33.5% for 10% talc. The control exhibited a 26% decrease in PFOA concentration, likely due to adsorption onto the walls of the tubes used in the experiment.

These findings confirm that the presence of activated carbon in the beads is primarily responsible for PFOA adsorption and highlight the potential synergistic effect between adsorption and bacterial degradation. Interestingly, the 10% activated-carbon beads demonstrated slightly higher adsorption efficiency than the 20% beads. This suggests that similar or even better removal performance can be achieved with a lower activated carbon content, thereby reducing production costs while maintaining high adsorption capacity.

We then attempted to characterize PFOS degradation by L. portucalensis.

PFOS degradation by Labrys portucalensis

Context: As the first axis of PFAway, L. portucalensis is used to break down long-chain PFAS such as PFOS. This newly described strain needs further characterization before implementation in the PFAway process.

L. portucalensis and PFOS degradation

Objective: We aimed at following PFOS degradation by the strain as performed in Wijayahena et al., 2025, but this time by increasing 10 fold the starting concentration of bacteria to measure the impact on degradation efficiency.

Method: Degradation of 10 mg/L of PFOS as the sole carbon source was monitored in M9 minimal medium for 30 days by LC-MS/MS. L. portucalensis was inoculated at two different starting concentrations, OD600=0.1 and 1.

Results: Changes in optical density over time suggested different bacterial growth responses depending on the initial inoculum (Figure 4).

Figure 4
Figure 4: Growth curves of L. portucalensis during the PFOS degradation assays.
Growth in M9 minimal medium supplemented with 10 mg/L of PFOS as the sole carbon source was monitored in tubes. Replicates are shown as dashed lines, and the mean as a solid line (n=2).

At starting OD600=1.0, we observed a gradual decrease from 1.00 to 0.50 OD600 over time, indicating a decline in the bacterial population.

In contrast, at an initial OD600 of 0.1, a slight increase was observed, suggesting that a smaller starting population could better utilize PFOS as a carbon source, likely due to reduced competition.

Further experiments with intermediate inoculum densities may help identify the maximum threshold below OD600=1 that still allows growth, thereby clarifying the relationship between initial biomass, resource availability, and bacterial activity under PFOS exposure.

PFOS degradation assays turned out to be inconclusive. During sampling, the filtering step used to remove bacteria before LC-MS/MS analysis led to adsorption of PFOS to the filter, precluding quantification of PFOS concentration. For future experiments, we recommend substituting the filtration step with cell pelleting by centrifugation and removal of the supernatant containing PFOS for mass spectrometry quantitation.

Quantification of toxicity effects by NaF, TFA and PFPrA

Objective: Degradation of PFOS generates PFPrA, TFA, and fluoride. These products are toxic to cells and might determine the maximal PFOS concentration that our process will be able to treat. We therefore assayed the minimal inhibitory concentration (MIC) of PFPrA, TFA, and NaF on L. portucalensis.

Method: Growth curves were monitored in the presence of NaF, TFA, and PFPrA by monitoring OD600 kinetics in a 96-well microplate reader on glucose as the carbon source in M9 minimal medium.

Results: All the collected data are available via our Kinetic Viewer. This allows a complete and easy visual presentation of the kinetic data, and the corresponding R code is available on Contribution page. The most relevant data are presented here. L. portucalensis was able to grow until 40 mM of both TFA and PFPrA, (Figure 5A). However, MIC for NaF was not reached, and lies in a range over 40 mM (Figure 5B). Concentrations above 50 mM NaF were tested but the resulting growth curves could not be analyzed because the M9 medium crystallized at such high concentrations. Interestingly, this effect was not observed in toxicity assays with Pseudomonas putida (as shown later on this page).

Figure 5
Figure 5: Toxicity assays of NaF, PFPrA and TFA on Labrys portucalensis.
A) Growth curves of L. portucalensis for different NaF (top), PFPrA (middle) and TFA (bottom) concentrations. Technical and biological replicates (n=6) are shown as transparent lines and the mean as bold lines. Growth was monitored in M9 minimal medium supplemented with 15 mM glucose in a 96-well microplate at 30°C across different concentrations of fluorinated compounds. B) Minimal inhibitory concentrations (MIC) of NaF, PFPrA and TFA on L. portucalensis.

As shown in Figure 5A, we observed important variations between biological replicates. This variability is primarily due to the difficulty of synchronizing Labrys portucalensis cultures, as the strain exhibits a long lag phase in pre-cultures (2 days). This issue is evident for all molecules shown in the figure and across all experiments with L. portucalensis (see on the Kinetic Viewer). While this variability does not prevent the determination of MIC values, it makes it challenging to accurately define characteristic growth parameters such as growth rates (μ) and lag time. To address this, we decided to normalize the biological replicates against their control condition (0 mM) in order to highlight trends in the evolution of μ and lag time as a function of molecule concentration (Figure 6).

Figure 6
Figure 6: Kinetic parameters of Labrys portucalensis growth in presence of NaF, PFPrA, and TFA.
Kinetic parameters were normalized to the 0 mM control within each replicate to account for variability across replicates. Normalized A) growth rate and B) lag time of L. portucalensis in the presence of NaF, PFPrA, or TFA at the indicated concentrations. Data show the mean of three normalized replicates (n=3). Means are shown as bold points, replicates are shown as transparent points.

The maximum growth rate decreases as the concentration increases for the different fluorinated compounds. No clear trend could be detected for the lag time.

These findings indicate that, although growth inhibition by PFOS degradation products can be quantified, variability in the physiological state of the replicates limits the precise determination of kinetic growth parameters.

We next turned to the second axis of the project: directed evolution of DeHa2 for degradation of short-chain PFAS.

Engineering an orthogonal replication system in E. coli

Context: We designed an orthogonal replication system (ORep) in E. coli, to generate a library of genetic variants of DeHa2 (see our Design page). The system requires two components: the linear replicon containing the dehalogenase gene (dehH2) flanked by its ITRs, and the replication operon encoding the error-prone polymerase and associated proteins that replicate the linear replicon in continuous cycles.

The replication operon was successfully assembled and verified

Objective: We aimed to assemble the replication operon, which encodes a double-mutant error-prone DNA polymerase (ODNAP) and associated proteins (TP, DSB, and SSB) required for continuous replication of the linear replicon, with the goal of either integrating it into the chromosome of E. coli or cloning it into a single-copy plasmid.

Method: The replication operon was initially synthesized into three gBlocks (A, B and C) by IDT. Each fragment contained 60 bp overlapping sequences to allow for Gibson assembly as well as homology regions for chromosomal integration in E. coli. The assembled operon was then amplified by PCR using KOD polymerase. To validate the good assembly of the operon, we performed agarose gel electrophoresis on the PCR performed on the assembled product and confirmed these results by linear amplicon sequencing using nanopore technology (Eurofins Genomics).

Results: Gel electrophoresis analysis showed a PCR product of the expected size (Figure 7). In addition, sequencing of the purified fragment confirmed the correct assembly of the replication operon (see part BBa_25HKSDJN). This validates the construct for transformation into a bacterial host, with the goal of generating a strain carrying the ORep system to enable continuous mutagenesis.

Figure 7
Figure 7: Agarose gel electrophoresis confirming the successful assembly of the replication operon by PCR amplification from the Gibson-assembled construct.

The main objective was to integrate the operon into E. coli chromosome to implement the ORep mutagenesis system, a modification made possible using two helper plasmids (pCas and pTarget) enabling CRISPR-assisted recombineering. However, this approach did not yield the expected results (see our Engineering page). We therefore sought for an alternative using a one-copy plasmid.

Construction of a one-copy plasmid carrying the replication operon

Objective: We aimed at inserting the replication operon into E. coli to generate the ORep strain, prior transformation with the linear replicon. The first strategy was chromosomal integration at the SS9 locus using CRISPR-assisted λ-Red recombination (see our Engineering page). As this was not achieved, an alternative strategy was designed based on assembling the operon into the one-copy plasmid pUD1387, which carries chloramphenicol resistance.

Method: The replication operon was amplified by PCR while excluding pre-existing SS9 sites within its sequence. The pUD1387 plasmid backbone was amplified by PCR to generate a linear fragment. Following Gibson assembly with both fragments, the product was transformed into competent E. coli cells and plated on LB agar supplemented with chloramphenicol for selection. Colonies were screened by colony PCR, and the presence of the operon was verified by PCR on purified plasmid and subsequent sequencing.

Results: PCR amplifications produced bands at the expected sizes: 3 804 bp for the operon and 6 945 bp for the linearized pUD1387 backbone (Figure 8).

Figure 8
Figure 8: Agarose gel electrophoresis showing the linear operon and backbone fragments generated by PCR.
Lane ABC: amplification of the operon at the expected size of 3 804 bp.
Lane OCP: amplification of the one-copy plasmid pUD1387 at the expected size of 6 945 bp.

Colonies grew on LB-chloramphenicol plates after transformation, confirming uptake of plasmid DNA. However, diagnostic PCR on miniprepped clones did not yield the expected amplicon size for the assembled plasmid; instead, smaller fragments were obtained (Figure 9).

Figure 9
Figure 9: Agarose gel electrophoresis of colony PCR from four independent clones.
Left side of the ladder: amplification product was expected at 5 572 bp, smaller bands were observed instead. Right side of the ladder: amplification product was expected at 5 243 bp, with bands matching the expected size. The discrepancy on the left suggests that a portion of gBlock A may be missing.

Sequencing confirmed incomplete assembly: only part of gBlock A was integrated, while gBlocks B and C were recovered intact in the plasmid (Figure 10).

Figure 10
Figure 10: Alignment of the expected one-copy plasmid carrying the replication operon (upper sequence) with the sequencing result (lower sequence).
A large missing region is highlighted in red, corresponding to most of gBlock A at the position where the DNA polymerase gene was expected.

Repeated attempts with purified PCR products and optimized assembly conditions yielded the same outcome. The incomplete recovery of the operon suggests instability of the construct in E. coli, possibly linked to the presence of foreign DNA polymerase genes. Future work will involve testing alternative cloning strategies to achieve stable maintenance of the complete operon.

The linear replicon was successfully assembled in pUC19 vector

Objective: We aimed to assemble the linear replicon designed to carry the dehalogenase gene (dehH2), the kanamycin-resistance gene (KanR) and flanked by ITRs, then to clone it into the pUC19 backbone, and validate the construction by sequencing.

Method: Linear replicon was first synthesized as two gBlocks (D and E) from IDT. Both fragments harboring dehH2, KanR and flanked by ITRs were cloned into the pUC19 vector by Gibson assembly to generate the replicon. The assembled construct was transformed into E. coli DH5α and plated on LB agar supplemented with kanamycin and ampicillin (KanR from gBlock D and AmpR from pUC19). Colonies were screened by restriction digestion. Plasmid DNA was extracted and subsequently sequenced by whole-plasmid sequencing using nanopore technology (Eurofins Genomics) to confirm the correct assembly and integrity of the linear replicon.

Results: Colonies were obtained on LB agar plates containing kanamycin and ampicillin, indicating successful transformation with the pUC19-containing linear replicon construct. Plasmid DNA from five selected clones was digested with BamHI, producing the expected band pattern (Figure 11). This result suggests correct assembly of the linear replicon within the pUC19 backbone.

Figure 11
Figure 11: Agarose gel electrophoresis for validation of the pUC19-replicon biobrick by BamHI restriction digestion.
A) Predicted digestion profile. B) Digestion patterns obtained from five independent colonies.

Sequencing of the miniprepped plasmids confirmed the correct assembly of the biobrick (see pUC19-replicon sequence on Materials page).

The sequence-verified pUC19-replicon was subsequently employed for the expression of DeHa2 in the fluorescence assays using the FluorMango biosensor (see later on this page).

Production of linear replicon with ITRs from pUC19-replicon

Objective: We aimed at amplifying and purifying the linear replicon from the pUC19-replicon biobrick. This linear fragment will later be introduced into the DH10B host carrying the replication operon to enable continuous orthogonal replication of the encoded dehH2 gene.

Method: Two primers targeting the linear replicon were designed to amplify the ITR-flanked fragment from the pUC19-replicon biobrick by PCR using KOD One polymerase. The PCR product was verified by agarose gel electrophoresis, purified, and sent for sequencing by whole-plasmid sequencing using nanopore technology (Eurofins Genomics).

Results: Agarose gel electrophoresis of the PCR product showed a single band at the expected size (Figure 12), confirming successful amplification of the linear replicon from the biobrick.

Figure 12
Figure 12: Agarose gel electrophoresis of the linear replicon amplified by PCR from the pUC19-replicon biobrick.
The expected band at 2 214 bp, corresponding to the linear replicon, is observed.

Sequencing of the purified fragment confirmed the linear replicon had the correct sequence (see part BBa_25794BPU).

We conclude that the linear replicon is ready for transformation into the bacterial host, where it provides the template carrying the DeHa2 enzyme to be subjected to continued mutagenesis by the ORep machinery.

Creation of a dehalogenase-free linear replicon biobrick

Objective: We aimed at generating a version of the linear replicon biobrick lacking the dehH2 coding the DeHa2 enzyme. This modified biobrick serves as a versatile kit, allowing users to insert their own target gene for continuous orthogonal replication and directed evolution.

Method: Two PCRs were performed from the biobrick: one amplifying the left half of the biobrick and the other the right half, both excluding the dehH2 sequence. PCR products were purified and joined by Gibson assembly to reconstruct the biobrick lacking dehH2. The assembled construct was transformed into E. coli for amplification and extracted by miniprep from multiple clones. Colonies were screened by restriction digestion to verify the absence of the dehH2 sequence. Plasmids from selected clones were sequenced by whole-plasmid sequencing using nanopore technology (Eurofins Genomics) to confirm the correct deletion and integrity of the biobrick.

Results: Agarose gel analysis of the two PCR products showed single bands (an upper band of lower intensity is also observed in one PCR product) of the expected size (~ 2 000 bp each), confirming successful amplification (Figure 13).

Figure 13
Figure 13: Agarose gel electrophoresis showing PCR linearization of the pUC19-linear replicon construct into two fragments.
Amplification was designed to exclude the dehalogenase gene. The expected bands were obtained: 1 932 bp (left) and 1 838 bp (right).

Gibson assembly products were amplified in E. coli. Restriction digestion of miniprepped plasmids showed that only clones 3 and 4 had the expected digestion pattern corresponding to the biobrick without dehH2 (Figure 14). Comparison with the original biobrick containing dehH2 corroborated the deletion.

Figure 14
Figure 14: Removal of the dehalogenase was confirmed by restriction digestion.
A) Expected profile: Lane 1 is the biobrick with dehalogenase gene and lane 2 is the biobrick without the dehalogenase gene for the kit. B) Experimentally obtained profile.

Sequencing results of plasmids from clones 3 and 4 confirmed the removal of the dehH2 gene and the correct sequence of the remaining biobrick (see pReplicon_KIT sequence on Materials page).

We then aimed at developing a screening method to be combined with ORep: fluoride-sensitive biosensor integrated with droplet microfluidics.

Screening ORep strains with FluorMango and microfluidics

Measurement in microplates

Context: We aimed to establish a FluorMango biosensor-based microfluidic screening approach that will later be applied to select active DeHa2 variants (for more details, see our Design page). We first performed microplate-based tests to evaluate FluorMango’s sensitivity, specificity, and proof-of-concept performance. For more information on the FluorMango microplate assays, see our Best Measurement page.

FluorMango fluorescence is sensitive to NaF concentration variations

Objective: We aimed at quantifying the responsiveness of FluorMango to varying amounts of fluoride ions.

Method: FluorMango aptamer was incubated for 1 hour with TO1-biotin, 1X refolding buffer and increasing NaF concentrations, and fluorescence was measured in 384-well plates.

Results: Figure 15 clearly demonstrates that the fluorescence intensity increases with the fluoride concentration up to 3 mM NaF. Moreover, the aptamer is sensitive to 0.1 mM NaF.

Figure 15
Figure 15: FluorMango/TO1-biotin complex response to fluoride ions.
FluorMango (400 nM) aptamer was incubated for 1 hour with TO1-biotin (700 nM), 1X refolding buffer and increasing NaF concentrations. Fluorescence of FluorMango/TO1-biotin complex was directly measured at 𝜆excitation=510 nm and 𝜆emission=550 nm. The x-axis represents NaF concentration and is displayed on a logarithmic scale. Grey points represent individual measurements (n=6), and black symbols indicate the mean values. The shaded area represents the confidence interval at 95%.

The next step was to show if this response is specific to fluoride ions.

FluorMango responds specifically to fluoride ions

Objective: We assessed the specificity of FluorMango fluorescence. To this end, we exposed the aptamer to a variety of molecules relevant to our experiments and measured its fluorescence.

Method: FluorMango aptamer was incubated for 1 hour with TO1-biotin (400 nM), 1X refolding buffer and NaF, NaCl, TFA or fluorinated microfluidic oil. Fluorescence was measured in 384-well plates.

Results: A strong fluorescence signal, up to 14-fold, was observed exclusively in the presence of fluoride ions, whereas fluorescence remained low in the presence of NaCl, TFA, or the fluorinated oil used in microfluidics (Figure 16). This remarkable specificity, together with its quantitative responsiveness, validates FluorMango as a reliable biosensor for fluoride ions.

Figure 16
Figure 16: Fluorescence of FluorMango/TO1-biotin complex in presence of different compounds.
FluorMango aptamer (400 nM) was incubated for 1 hour with TO1-biotin (700 nM), 1X refolding buffer and 1 mM of NaF, NaCl, TFA or fluorinated microfluidics oil (Fluo-oil 135) with or without surfactant (FluoroSurf O at 2%). Fluorescence of FluorMango/TO1-biotin complex was directly measured at 𝜆excitation=510 nm and 𝜆emission=550 nm. Values are the mean of three independent experiments (n=3), and errors bars correspond to standard deviation. The individual data points are also displayed in grey.

We then tested whether the biosensor could detect fluoride released during bacterial defluorination of a fluorinated substrate.

FluorMango detects fluoride released from enzymatic defluorination

Objective: We investigated if FluorMango is compatible with the detection of fluoride in the presence of bacteria, i.e., under conditions close to the screening of DeHa2 variants with ORep E. coli cells.

Method: FluorMango was incubated with TO1-biotin, 2-fluoropropionate (2-FP) as the monofluorinated substrate for DeHa2, and E. coli cells expressing recombinant DeHa2 (from pUC19-replicon plasmid). Substrate degradation kinetics were monitored over 4 hours in 384-well plates by directly measuring the fluorescence of the FluorMango/TO1-biotin complex.

Results: We found that the defluorination of 2-FP and the accompanying production of F- by DeHa2 (with IPTG) could successfully be detected by FluorMango (upper curve in Figure 17), while the fluorescence signal remained low in the control samples (no IPTG induction, only bacteria, only 2-FP). Summarizing, we provided a detailed characterization of FluorMango responsiveness, establishing this biosensor as a quantitative tool for the directed evolution of DeHa2.

Figure 17
Figure 17: Real-time monitoring of fluoride (F⁻) release during IPTG-induced DeHa2 expression in E. coli DH5α.
Cultures were grown overnight in LB at 37 °C, washed in PBS, and incubated in a microplate reader at 25°C with IPTG (0.1 mM), 2-FP (50 mM), FluorMango (400 nM), TO1-biotin (700 nM) and 1X refolding buffer. Fluorescence was recorded with λexcitation=510 nm and λemission=550 nm. Values are the mean of two independent experiments (n=2), and errors bars correspond to the standard deviation.

Having validated FluorMango as a sensitive and specific biosensor in microplate assays and even in the presence of living bacteria, the next step was to test whether this technology could be translated into a droplet-based format. Microfluidic encapsulation not only provides the high-throughput capacity required for directed evolution but also allows linking enzymatic activity to individual genetic variants. We therefore explored whether FluorMango retains its functionality inside droplets and whether it can support the sorting of active versus inactive variants in a pooled screening setup.

Measurement in droplet-microfluidics

Context: Pooled genetic screens of DeHa2 variants require a method to efficiently link the gene sequence to enzymatic activity. During hypermutagenesis in the ORep E. coli strain, a large diversity of the dehH2 gene is created within the bacterial population. Isolation of genetic variants and their phenotypic outputs is then essential for directed evolution.

Our strategy consisted in compartmentalizing individual ORep cells along with FluorMango inside water-in-oil emulsion droplets generated by microfluidics. To find out more about the microfluidic assays, see our Best Measurement page.

FluorMango enables fluorescence detection of fluoride in microfluidic droplets

Objective: We aimed at detecting fluoride ions in microfluidic droplets using FluorMango.

Method: FluorMango was incubated with TO1-biotin, 1X refolding buffer and either NaF (1 mM, for positive-fluorescent droplets) or RNAse-free water (for negative droplets). Droplets were generated using two approaches: in the first one, FluorMango activation occurred only after encapsulation, whereas in the second one, FluorMango was pre-activated by fluoride prior encapsulation. Fluorescence of FluorMango/ TO1-biotin in droplets was measured by fluorescence microscopy.

Results: We visualized the positive and negative droplets collected from the microfluidic chip by fluorescence microscopy. With both sample preparation and droplet generation methods, no fluorescence was detected in negative control droplets, whereas positive control droplets consistently exhibited strong fluorescence (Figure 18). These results demonstrate the successful detection of fluoride ions by FluorMango in microfluidic droplets.

Figure 18
Figure 18: Fluorescence detection of fluoride (F⁻) in microfluidic droplets using the FluorMango biosensor
Bright-field (top) and fluorescence (bottom) microscopy images of negative (+RNAse-free water) and positive (+NaF) droplets generated with A) method 1 where FluorMango activation occurred after encapsulation, B) method 2 where FluorMango activation occurred prior encapsulation. Fluorescence was recorded with 𝜆excitation=480/40 nm and 𝜆emission=527/30 nm.

We conclude that its implementation in microfluidics does not impair biosensor functionality.

FluorMango allows for fluorescence-based sorting in microfluidics

Objective: We aimed at sorting active droplets based on fluorescence intensity thresholding from a mixed population of positive (with fluoride → fluorescent) and negative (no fluoride → nonfluorescent) droplets. This ‘mock library’ assay would validate the method for the prospective screening and selection of DeHa2 variants.

Method: Positive droplets and negative droplets generated using Method 2 (described above) were mixed at a 2:8 ratio (v/v) to create a mock library of active and inactive variants. Droplets were screened using the integrated fluorescence detector with 𝜆excitation=488 nm and 𝜆emission=525 nm and pre-sort and sort population analyzed using fluorescence microscopy.

Figure 19 shows a droplet sorting experiment which was performed under an oil pressure of 500 mbar and a sample pressure of 360 mbar to ensure efficient separation of droplets. When a droplet passing the detector exceeds the fluorescence threshold, the electrode is activated, deflecting the droplet toward the lower outlet for collection of the fluorescent droplets. Droplets with fluorescence below the threshold are directed to the upper outlet as waste.

Figure 19
Figure 19: Bright-field microscopy images of the sorting area of R-Sort100.
The flow direction and position of the fluorescence detector are indicated. Droplets are directed to one of the two outlets depending on their fluorescence intensity.

Video 1: Droplets sorting

Results: Fluorescence-based sorting of the mixed droplet population (‘mock library’) yielded time-resolved events of screened positive droplets (Figure 20). These detection hits activated the sorting of droplets that were collected in an Eppendorf tube. We assessed the sorting efficiency by imaging the collected droplets under a fluorescence microscope. The images (bright field and fluorescence) revealed an enrichment of the positive droplets from 20% (pre-sort) to 80% after sorting (Figure 21).

Figure 20
Figure 20: Fluorescence detection of hits during droplet sorting.
Events above threshold are represented as red lines on top of the graph.
Figure 21
Figure 21: Microscopy images of pre-sort and sort populations showing enrichment of positive droplets.
All the droplets are visualized with the bright-field mode (top), while active droplets (+NaF) are observed in the fluorescence channel (bottom). Fluorescence measured at 𝜆excitation=480/40 nm and 𝜆emission=527/30 nm.

We conclude that FluorMango, combined with fluorescence-based droplet microfluidic sorting, enables successful enrichment of positive droplets in a mock library containing an excess of inactive droplets. The ‘mock library’ validates this method for the prospective screening and selection of DeHa2 variants.

We then turned to enhancing the fluoride resistance of our chassis Pseudomonas putida, which will be bearing the expression of DeHa2 for short-chain PFAS defluorination.

Enhancing the resistance of P. putida to fluoride ions with FluC

Context: In the PFAway process, L. portucalensis degrades long-chain PFAS, releasing PFPrA and TFA, whose subsequent defluorination by the evolved DeHa2 produces large amounts of fluoride ions. These ions, as well as short-chain PFAS, can inhibit essential metabolic enzymes, compromising the expression of the evolved DeHa2 by Pseudomonas putida KT2440 and more generally the cell’s viability. We therefore wanted to characterize and enhance the resistance to fluoride ions of our modified P. putida strain which will bear the expression of the evolved DeHa2.

Successful construction of the pSEVA438-fluC plasmid

Objective: The fluoride-specific transmembrane transporter FluC endogenously expressed under the control of fluoride-responsive mechanisms was overexpressed in P. putida KT2440.

Method: The gene encoding for FluC was cloned into the expression plasmid pSEVA438 under the control of the strong xylS/Pm transcription promoter. P. putida was transformed with the resulting construct, pSEVA438-fluC. Following induction with m-toluic acid, the growth of the recombinant strain KT2440-pSEVA438-fluC was assessed in the presence or absence of 50 mM NaF by monitoring OD600 kinetics in 96-well microplates in LB medium. Whole-plasmid sequencing was performed using nanopore technology at Eurofins Genomics.

Results: After cloning and transformation of P. putida, plasmid extraction, and purification, pSEVA438-fluC was sent for sequencing. The alignment shows that fluC has successfully been cloned in pSEVA438. See the complete sequencing of pSEVA438-fluC in the Materials page.

We then aimed to verify that FluC was successfully overexpressed by comparing the growth curve of the recombinant strain to that of wild-type P. putida in the presence of NaF, both with or without induction with m-toluic acid (Figure 22).

Figure 22
Figure 22: Growth curves and kinetics of Pseudomonas putida KT2440 (WT) and P. putida KT2440-pSEVA438-fluC.
Strains were cultivated in LB medium at 30°C with 50 mM of NaF. Technical replicates (transparent circles or dashed lines) and means (solid circles or lines) are represented (n=3). A) Growth curves in the presence or absence of 500 µM m-toluic acid (induced or not induced). B) Specific growth rates and C) lag time for both strains, in the presence or absence of 500 µM m-toluic acid (induced or not induced).

Figure 22A shows that for the WT strain, there is no significant difference in fluoride resistance with or without the inducer. This suggests that the presence of m-toluic does not affect bacterial growth. For P. putida KT2440-pSEVA438-fluC, the lag time is reduced by 2-fold compared to the WT strain in the presence of the inducer, while the growth rate is unchanged (Figure 22 B and C). These results suggest a positive effect on fluoride stress adaptation. Further investigation to characterize these effects were pursued.

Overexpression of fluC accelerates cellular adaptation to fluoride stress

Objective: We further investigated the effect of fluC overexpression on P. putida’s response to fluoride stress. Additional experiments were conducted in M9 minimal medium to better mimic the conditions encountered during water treatment.

Method: Growth of the recombinant strain P. putida KT2440-pSEVA438-fluC in M9 minimal medium was monitored in the presence of m-toluic acid inducer, across different NaF concentrations. Two individual carbon sources were used, acetate and propionate, as they are the expected degradation products of TFA and PFPrA. Lag time, specific growth rate, and Minimal Inhibitory Concentrations (MIC) were evaluated.

Results: The complete dataset and results are provided on the Kinetic Viewer. The growth kinetics of the recombinant strain on both carbon sources were compared, as shown in Figure 23.

Figure 23
Figure 23: Growth curves and kinetics of P. putida KT2440-pSEVA438-fluC on propionate or acetate as carbon source, in the presence of fluoride ions.
Biological replicates (transparent circles and dashed lines) and means (solid circles and lines) are represented (n=3). A) Growth curves on M9 minimal medium supplemented with 30 mM and 45 mM of propionate or acetate respectively, in the presence of different NaF concentrations. OD600 was monitored in 96-well microplates at 30°C. B) Specific growth rates and C) lag time on both carbon sources, for different NaF concentrations. D) Comparative table of MIC of NaF on the recombinant strain.

In the absence of fluoride ions, P. putida pSEVA438-fluC grows similarly on propionate or acetate (Figure 23A). In fact, specific growth rates are equivalent with values of 0.58 h-1 on acetate and 0.63 h-1 on propionate (Figure 23B). When increasing the NaF concentration, the specific growth rates follow the same trend, and carbon source does show any influence. However, lag times for acetate are clearly reduced compared to that on propionate (Figure 23C). Overall, the MIC for NaF on acetate is clearly higher (over 100 mM) than the MIC on propionate (75 mM) (Figure 23D).

To further characterize the effect of the overexpression of fluC on growth, we then compared growth of the wild-type strain and the recombinant strain on acetate in the presence of different NaF concentrations (Figure 24).

Figure 24
Figure 24: Growth curves and kinetics of the WT and recombinant P. putida KT2440 strain in minimal M9 acetate medium in the presence of NaF.
Biological replicates (transparent circles and dashed lines) and means (solid circles and lines) are represented (n=3). A) Growth curves of Pseudomonas putida KT2440 (WT) and P. putida KT2440-pSEVA438-fluC in M9 minimal medium supplemented with 45 mM acetate, recorded in a 96-well microplate at 30°C under different NaF concentrations. B) Growth rate and C) lag time of P. putida KT2440 (WT) and P. putida KT2440-pSEVA438-fluC as a function of NaF concentration under the same growth conditions. D) Comparative table of MIC of NaF for the recombinant and WT strain.

We found that higher concentrations of NaF led to reduced growth rates (µ) and increased lag times for both strains (Figure 24). This confirms that the toxic effect of fluoride ions on bacterial growth is not confined to a threshold concentration leading to cell death, but encompasses a progressive impairment of metabolic activity (Qin et al., 2006).

Interestingly, the recombinant strain was less affected than the WT strain at a given NaF concentration. P. putida KT2440-pSEVA438-fluC was able to grow at NaF concentrations up to 100 mM, whereas the WT strain only grew up to 60 mM (Figure 24A). The resulting MIC for P. putida WT is congruent with the MIC found in literature in M9 minimal medium supplemented with glucose, which lies in the range of 75 mM (Calero et al., 2022) (Figure 24D). A difference of 25 mM is then observed in the MIC analysis, showing that the overexpression of the FluC transporter enables growth in the presence of higher fluoride concentrations.

The overexpression of fluC also accelerated the adaptation of P. putida to high fluoride concentrations. Specific growth rates were less affected by NaF for the recombinant strain, and lag times were significantly reduced compared to that of the WT strain (Figure 24B and C). For example at 40 mM NaF, the lag time of KT2440-pSEVA438-fluC was 12 h compared to 25 h for the WT, and the growth rate was 0.32 h-1 versus 0.25 h-1, respectively. Similar trends were observed in M9 medium supplemented with propionate: data are provided in the supplementary Figure S1. The complete dataset and results are provided on the Kinetic Viewer.

Process limits were assessed by PFPrA and TFA toxicity on P. putida

Objective: Since PFAS are toxic to cells and might determine the maximal PFOS concentration that our process will be able to treat, we assayed the minimal inhibitory concentration (MIC) of PFPrA and TFA on the fluoride resistant strain P. putida KT2440-pSEVA438-fluC. Two individual carbon sources were used, acetate and propionate, as they are the expected degradation products of TFA and PFPrA.

Method: The growth of the recombinant strain was assessed in the presence of TFA and PFPrA by monitoring OD600 kinetics in 96-well microplate reader in M9 minimal medium supplemented with acetate and propionate as carbon sources. Lag time, specific growth rate, and Minimal Inhibitory Concentrations (MIC) were evaluated.

Results: As shown in Figure 26A, Pseudomonas putida KT2440-pSEVA438-fluC was able to grow at TFA and PFPrA concentrations up to 30 mM.

Figure 26
Figure 26: Growth curves and kinetics of the recombinant P. putida strain in minimal M9 acetate medium in the presence of TFA and PFPrA.
Biological replicates (transparent circles and lines) and means (solid circles and lines) are represented (n=3). A) Growth curves of P. putida KT2440-pSEVA438-fluC cultivated in M9 minimal medium supplemented with 45 mM acetate and measured in a 96-well microplate at 30°C across different TFA and PFPrA concentrations. B) Growth rate and C) lag time of P. putida KT2440-pSEVA438-fluC as a function of TFA and PFPrA concentration. D) Determined MIC for TFA and PFPrA for P. putida KT2440-pSEVA438-fluC.

Increasing TFA and PFPrA concentrations caused a drop of the specific growth rate at 30 mM, while the lag time increased. For instance, lag time ranged from 5 h without TFA to 12 h at 30 mM TFA. (Figure 26C). The MIC of TFA and PFPrA for P. putida KT2440-pSEVA438-fluC were determined to be 40 mM (Figure 26D). Similar behaviors were observed under other conditions, such as growth in M9 medium supplemented with propionate for which the MIC also lies in the range of 40 mM (see supplementary Figure S2). A link to the complete dataset and results is provided on the Kinetic Viewer.

Discussion and perspectives

Our team aimed at implementing a degradation process of PFAS using two complementary bacterial strains embedded in activated carbon beads.

We first determined key parameters for the full process development as detailed in Entrepreneurship page:
• The viability of L. portucalensis and P. putida was ensured for at least 30 days in the encapsulation beads. This indicates the lifespan of the beads before recycling, and thus the lifespan of the degradation process.
• Activated carbon showed efficient adsorption of 96.9% of PFOA when used at 10% concentration in the beads. Its presence did not compromise bacterial viability.

We also determined the maximum concentration of degradation products of PFOS (PFPrA, TFA and fluoride ions) that could tolerate the recombinant P. putida strain and L. portucalensis. Minimal inhibitory concentrations (MICs) were deduced:

Table 1: Experimental MIC determined for L. portucalensis, P. putida KT2440 Wild Type and P. putida KT2440-pSEVA438-fluC. These were estimated in M9 medium supplemented with acetate or glucose as carbon source for P. putida or L. portucalensis respectively.

Table 1

In addition, we found that overexpression of the fluoride transporter FluC in P. putida KT2440 significantly increased the strain’s tolerance to fluoride ions, raising the MIC from 75 mM in the wild-type to >100 mM in the recombinant strain. Knowing that PFOS complete defluorination releases 17 fluoride ions, the maximum PFOS concentration that can be fully defluorinated before growth inhibition rises from 4.4 mM for the WT to 5.9 mM for the recombinant strain, representing a 34% improvement. This enhanced resistance directly extends the operational range for complete PFOS degradation, demonstrating the importance of engineering fluoride tolerance to optimize bioremediation of PFAS.

Moreover, at a 1:1 stoichiometric ratio, PFPrA and TFA are formed at concentrations up to 5.9 mM, which remain far below the MIC values for P. putida KT2440-pSEVA438-fluC (40 mM) and L. portucalensis (50 mM). Consequently, the accumulation of these intermediates should not hinder PFOS biodegradation under the tested conditions.

Although such high PFOS concentrations are unlikely to occur in natural environments, the increased fluoride tolerance conferred by FluC is still highly relevant. In real applications, it provides an additional safety margin against growth inhibition, ensuring robust strain performance even under conditions of accumulation of PFOS in the activated carbon beads, transient concentration peaks, or scale-up processes where fluorinated compounds may accumulate.

Further perspectives are to be explored:

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