Open Access Article
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Nitrate enhances TCE removal by enriching bifunctional denitrifying/aerobic co-metabolizing microbes in the joint H2/O2 system

Wenyi Huang a, Weiwei Ouyang a, Haonan Bian a and Hui Liu *ab
aHubei Key Laboratory of Yangtze Catchment Environmental Aquatic Science, School of Environmental Studies, China University of Geosciences, Wuhan, Hubei 430078, P R China. E-mail: hliu2009@cug.edu.cn; Fax: +(86) 27 87436235; Tel: +(86) 27 87436235
bState Key Laboratory of Geomicrobiology and Environmental Changes, China University of Geosciences, Wuhan, Hubei 430078, P R China

Received 14th January 2025 , Accepted 20th March 2025

First published on 21st March 2025


Abstract

Trichloroethylene (TCE) is a pervasive groundwater contaminant that poses significant health and ecological safety risks. The coexistence of hydrogen (H2) and oxygen (O2), resulting from electrochemical remediation technologies, has been shown to promote the degradation of TCE by fostering specific microbial communities. However, the role of nitrate (NO3), a common co-contaminant with TCE in groundwater, in this H2/O2 system remains poorly understood. This study revealed that increasing the nitrate concentrations (0–240 mg L−1) significantly enhanced TCE removal rate and efficiency, with the maximum removal rate increased by 1.84 times and removal efficiency by 19.79%. The variation in nitrate concentration could influence microbial diversity. In particular, denitrifying microorganisms, such as Pseudomonas, Hydrogenophaga, and Methyloversatilis, were enriched, which could reduce nitrate and nitrite using H2 as an electron donor and degrade TCE through aerobic co-metabolism. The increased presence of these microorganisms led to an abundance of the functional gene phe, which is responsible for TCE aerobic co-metabolic degradation, thereby enhancing TCE removal in the joint H2/O2 system. However, a high nitrate concentration of up to 240 mg L−1 inhibited the accumulation of Pseudomonas and Methyloversatilis. Meanwhile, it increased the abundance of Hydrogenophaga, which could use H2 and O2 to fix CO2 and provide organics for bacterial growth. These insights provide valuable technical guidance for the remediation of TCE and nitrate composites in groundwater environments, highlighting the potential of leveraging the interactive effects of H2, O2, and nitrate on microbial communities for effective bioremediation strategies.



Water impact

Trichloroethylene (TCE) is widely utilized in the chemical industry. Electrochemical synergistic microbial technology is an effective method to enhance the bioremediation of TCE in underground water. Electrochemistry generates hydrogen (H2) and oxygen (O2), which create a joint hydrogen–oxygen (H2/O2) region that is conducive to carbon cycling and the removal of TCE. This study explored the effects of different concentrations of nitrate on the degradation of TCE by in situ microorganisms in a combined H2/O2 system through an indoor batch experiment. This study elucidates the mechanisms by which nitrate influences microbial diversity, enriching denitrifying bacteria using H2 as an electron donor to degrade TCE through co-metabolism under aerobic conditions. These insights provide valuable technical guidance for the remediation of TCE and nitrate composite contaminants in groundwater environments, highlighting the potential of leveraging the interactive effects of H2, O2, and nitrate on microbial communities for effective bioremediation strategies.

1 Introduction

Trichloroethylene (TCE) is extensively employed as an essential organic solvent and chemical raw material.1 Owing to challenges in handling and disposing during its production, use and transportation, TCE is one of the most critical organic pollutants in the groundwater environment, posing severe ecological risks.2,3 Additionally, TCE is biotoxic and can enter the human body through inhalation and dermal absorption, potentially causing poisoning and damage to internal organs as well as neurological impairment.4 Given the global emphasis on groundwater safety, remediation of TCE contamination has emerged as a pivotal area of scientific inquiry.

Currently, microbial remediation is one of the predominant TCE remediation technologies, operating primarily through three distinct biological processes, namely, microbial aerobic co-metabolism, aerobic direct metabolism, and anaerobic reductive dichlorination.5 Aerobic co-metabolism of TCE involves a process where oxygen (O2) acts as an electron acceptor under aerobic conditions and microorganisms utilize TCE as an electron donor or an externally supplied carbon and energy source, facilitating the conversion of substrates that are not typically metabolized when they are growing.6 Direct aerobic metabolism of TCE involves microorganisms that utilize TCE as their exclusive carbon and energy source, leading to its direct degradation and metabolism under aerobic conditions.7 Anaerobic reductive dechlorination involves the degradation of TCE by microorganisms via respiration in an anaerobic environment, where TCE acts as an electron acceptor and hydrogen (H2) acts as an electron donor.8

In recent years, electrochemical technology has emerged as a novel approach for efficient remediation of organic pollutants in groundwater; it supplies H2 and O2 to the aquifer through water electrolysis, thereby promoting TCE degradation.9 Research works indicate that combining electrochemical and microbial remediation technologies can effectively promote the in situ microbial degradation of chlorinated hydrocarbons (CHCs) in groundwater.9–11 The cathodic electrode produces H2, enriching genes associated with the anaerobic degradation of pollutants. In contrast, the anode produces O2, which enhances the electron transfer activity within the microbial community and enriches functional genes related to phenol monooxygenase.12,13 Furthermore, the cathode-produced H2 and anode-produced O2 mix in the aquifer through groundwater flow, establishing a joint hydrogen–oxygen (H2/O2) zone. Compared to solely an H2 or O2 environment, the joint H2/O2 system effectively enhances denitrification and sulfate oxidation.12 The joint H2/O2 environment will promote the formation of microbial communities with specific structures and functions, increasing the relative abundance of the aerobic functional gene phe,14 encoding phenol monooxygenase and the TCE anaerobic dechlorination functional gene tceA.15,16 The joint H2/O2 system enables aerobic and anaerobic degradation of CHCs, thereby effectively enhancing the removal of CHCs like trichloroethane.15,17 However, the subsurface environment is inherently complex, and groundwater constituents such as SO42−, NO3, and Fe(III) can potentially impact the degradation of TCE.18,19 Consequently, additional research is required to elucidate the impact of these groundwater components on TCE biodegradation under the joint H2/O2 system.

Nitrate (NO3) has become a prevalent inorganic contaminant in groundwater. The nitrate concentration in groundwater ranges from 2 to 776 mg L−1.20,21 NO3 contaminant frequently co-exists with organochlorine pollutants in the subsurface environment.22 For instance, at a site in the U.S.A., groundwater was found to contain nitrate (up to 230 mg L−1) mixed with TCE (up to 300 μg L−1).23 The presence of NO3 can impact the degradation process of CHCs through denitrification.24,25 Studies have confirmed that NO3 inhibits reductive dechlorination under anaerobic conditions, with the inhibition effect intensifying as NO3 concentrations increase.26 The redox potentials for CHCs reductive dechlorination and denitrification are similar, leading to competition for electron donors such as H2 (ref. 24) and NO3 typically precedes TCE in reductive processes under H2-limited conditions.19 Furthermore, in the process of aerobic denitrification aimed at NO3 removal under aerobic conditions, microorganisms may simultaneously utilize either NO3 or O2 as an electron acceptor, followed by organic compounds serving as a carbon source and electron donor for reducing NO3.27 Leahy28 discovered that under hypoxic conditions, NO3 could act as an alternative electron acceptor, promoting the degradation of TCE. While numerous studies have explored the impact of NO3 on TCE degradation under anaerobic and aerobic conditions, the regulatory mechanism of NO3 on TCE degradation in environments where H2 and O2 coexist remains unclear. Therefore, it is crucial to investigate the influence of NO3 on TCE degradation within the joint H2/O2 system to understand the role of denitrification in this process.

This study was conducted on an indoor batch experiment to explore the impact and underlying mechanisms of different NO3 concentrations on the degradation of TCE by in situ microorganisms within the joint H2/O2 system. 16S rRNA gene sequencing coupled with quantitative PCR (qPCR) were utilized to monitor changes in microbial community structure and functional genes following the introduction of NO3, and to investigate the mechanism by which the denitrification process either enhances or impedes the oxidation or reduction of TCE. The results of this study are expected to offer valuable technical insights for the remediation of TCE and NO3 co-contamination in the joint H2/O2 system.

2 Materials and methods

2.1 Sediment characterization

The sediment samples for the experiment were collected from a chemical plant site in Tianjin (China) at a depth of 3–5 m, which was contaminated by high concentrations of CHCs. The TCE concentration in the sediments was 171.41 mg kg−1, with NO3 concentrations varying from 17.48–23.16 mg kg−1 and total organic carbon (TOC) concentrations ranging from 650–940 mg kg−1.

2.2 TCE degradation experiment

The experimental device consisted of a 250 mL screw glass vial and a 300 mL Teflon bag connected by a Viton hose, as depicted in Fig. S1.17 The preparation was conducted in an anaerobic chamber (Coy Laboratory Products Inc., Michigan). Each experimental unit added 40 g of wet sediment and 200 mL of sterilized ultrapure water, along with 80 μM TCE. NO3 was introduced at 0, 30, 60, and 240 mg L−1 concentrations across different experimental groups. The gas bag was filled with 100 mL of H2 and 50 mL of O2 (H2 and O2 were obtained by water electrolysis). Sterilized sediments without additional NO3 supplementation served as controls. Microcosms were prepared in duplicate, and all experimental systems were cultured at 25 °C and 150 rpm. Soil samples were collected for subsequent microbial analysis on the 0th and 5th days of the reaction.

2.3 Analytical methods

The determination of TCE and possible intermediates in the samples was performed on an automatic purge and trap-gas chromatography-mass spectrometry (PT-GC-MS) (PT: Atomx, Teledyne Tekmar, USA; GC-MS: Thermo Fisher Scientific Inc., USA) with an Agilent DB-624 capillary column (30 m × 0.25 mm × 1.4 μm). The oven temperature was held at 35 °C for 2 min, heated at a rate of 5 °C min−1 to 120 °C, then heated at a rate of 10 °C min−1 to 220 °C and held for 2 min. The EI ion source was used with a temperature of 230 °C and the full scanning range was 35–270 amu. The quantification was done using the internal standard method.

Immediately after sampling, the oxidation–reduction potential (ORP) was measured using a redox potential tester (PHS-3C, Rex of Shanghai Co., Ltd. China). Dissolved hydrogen (DH) was measured with a hydrometer (DH200, CLEAN, USA) and dissolved oxygen (DO) was measured directly using a noninvasive oxygen sensor. The pH was determined using a pH meter. The concentrations of NO3 and NO2 in solution were determined by ultraviolet spectrophotometry.

2.4 Taxonomic and functional microbial composition analyses

Total DNA from sediments was extracted using a soil DNA extraction kit (Power Soil® DNA). Microbial gene sequencing was performed using an Illumina MiSeq instrument (MiSeq, Illumina, USA) at the Personal Biotechnology Company (Shanghai, China). Microbial community analysis was performed using QIIME 2 (2019.4), and microbial diversity and abundance were estimated using Mothur software (version 1.35.1, USA).

2.5 Quantification of functional genes by qPCR

The real-time quantitative polymerase chain reaction (qPCR) was performed on an ABI QuantStudio 3 (Version 1.4.1 software, Applied Biosystems, USA) to quantify microbial numbers and functional genes in the samples. The 16S rRNA gene was amplified using primers 341F and 515R. The abundance of genes related to bio-dechlorination (tceA), aerobic co-metabolic degradation (pmoA, phe), and NO3 reduction (narG, nirS, nosZ) were quantified by qPCR. Detailed information on the primer sequences is shown in Table S1. The 16S rRNA genes were normalized for each sample. The relative abundances of functional genes were calculated using the 2−ΔΔCT method, and the absolute abundances of functional genes were calculated by multiplying the number of 16S rRNA gene copies.29,30

3 Results and discussion

3.1 TCE removal under different NO3 concentrations in the joint H2/O2 system

The changes in TCE concentration under the joint H2/O2 system with different nitrate concentrations and sterilized control are shown in Fig. 1a. In the sterilized control, TCE concentrations gradually decreased over 15 days, likely due to volatilization and adsorption. In the unsterilized sediments, TCE concentrations dropped quickly during the initial 7 days and almost stopped declining afterwards. Nitrate concentration showed a significant impact on the TCE removal. Higher nitrate concentrations, such as 60 and 240 mg L−1, caused faster and more TCE removal.
image file: d5ew00046g-f1.tif
Fig. 1 TCE removal kinetics (a), fitting of TCE removal curves (b), nonlinear regression analysis of the relationship between TCE removal rate constants and nitrate concentrations (c), and TCE removal efficiencies (d) under different nitrate concentrations.

To quantitatively compare the effect of different nitrate concentrations on the TCE removal rate, the first-order kinetic model in eqn (1) was used to fit the TCE removal curves, as shown in Fig. 1b.

 
ln(C0/Ct) = kt(1)
where C0 and Ct denote the concentration of TCE at initial and time t, and k is the kinetic constant of the primary reaction.

As shown in Fig. 1b and c, the k values increased from 0.1115 to 0.3167, with nitrate concentrations elevating from 0 to 240 mg L−1, which followed a nonlinear eqn (2).

 
k = 0.3843C/(48.2138 + C)(2)
where C denotes different nitrate concentrations in the different groups.

This trend indicated that the TCE removal rate was more affected by lower nitrate concentrations. After 15-day experiments under different nitrate concentrations, the final TCE removal efficiencies were calculated using eqn (3) and shown in Fig. 1d.

 
TCE removal efficiency = [(C0Ct)/C0] × 100%(3)
where C0 and Ct denote the concentration of TCE at initial and time t.

During the 15-day experimental period, the TCE removal efficiencies under 0–30 mg L−1 nitrate were 64.60% to 67.25%, and those with 60 and 240 mg L−1 nitrate increased to 74.16% and 87.04%, respectively, indicating that a higher concentration of nitrate significantly promoted TCE removal efficiency in enough reaction time.

Prior research has found that NO3 inhibits the degradation of chlorinated olefins under anaerobic conditions.31 However, Yu32 demonstrated that low concentrations of NO3 could serve as a nitrogen source to enhance the biological reductive dechlorination of organic compounds. Our study is the first to report that nitrate enhances TCE removal in a joint H2/O2 system, which is common in the electrochemical remediation sites.

3.2 Denitrification during TCE removal in the joint H2/O2 system

Denitrification reactions were observed by detecting NO3, NO2, and NH4+ variations during 15-day experiments (Fig. 2a and b) to understand the TCE removal kinetics impacted by nitrate concentrations in the joint H2/O2 system. No NH4+ was detected in all the experiments. During the initial 7 days when TCE was quickly removed, nitrate concentrations dropped dramatically, accompanied by nitrite generation. Under 30 and 60 mg L−1 nitrate concentrations, nitrates were exhausted in 5 days, while the formed nitrite reached a maximum and declined afterwards, indicating further nitrite reductions. In contrast, under 240 mg L−1 nitrate, the nitrate removal efficiency reached 53.86% within 7 days, and then the nitrate reduction stopped. Meanwhile, nitrite was gradually produced in 7 days and then kept stable, suggesting that nitrate and nitrite reductions were limited after 7 days. This limitation should be attributed to the accumulation of toxic nitrite. It was discovered that nitrite accumulation inhibited the growth of Pseudomonas fluorescens.33 The free nitrite concentrations of 0.01–0.025 mg L−1 can reduce 40% nitrate reduction activity.34
image file: d5ew00046g-f2.tif
Fig. 2 Variations in aqueous-nitrate (a) and -nitrite (b) and Δnitrate/ΔTCE molar ratios (c) during the experiments at different nitrate concentrations.

To further elucidate the relationship between nitrate denitrification and TCE removal in the joint H2/O2 system, the quantitative relationship was determined by calculating the molar ratio of consumed nitrate to removed TCE (Δnitrate/ΔTCE) in 15 days (Fig. 2c). It showed that the Δnitrate/ΔTCE varied with time and nitrate concentrations. Under lower nitrate concentrations such as 30 mg L−1, the Δnitrate/ΔTCE values were about 20 on the first day, increased to 35 on the second day, and then decreased to and kept stable around 10 after 3 days. The Δnitrate/ΔTCE values when the nitrate concentration was 60 mg L−1 showed a similar trend with 30 mg L−1 nitrate. In contrast, the high nitrate concentration of 240 mg L−1 nitrate showed a high Δnitrate/ΔTCE value of 87 and gradually decreased to around 22. These results indicated that increased nitrate concentration enhanced denitrification more than TCE removal, especially during the first several days of the fast reaction stage.

3.3 Variation of environmental factors during TCE removal in the joint H2/O2 system

DH, DO, ORP, and pH are crucial parameters affecting CHC degradation.30,35,36 Their variations were monitored during the experiment further to analyze the mechanism of nitrate effects on TCE removal. The results are shown in Fig. 3. DH and DO values were 0–0.6 mg L−1 and 0–6 mg L−1, respectively, in all the treatments, while ORP values fluctuated from −300 mV to 30 mV in the pH range of 8 to 9.
image file: d5ew00046g-f3.tif
Fig. 3 Variations in DH (a), DO (b), ORP (c) and pH (d) during the experiments at different nitrate concentrations.

The significant variations of these parameters happened in 7 days. The increased DH and DO in two days was due to mixing the gases in the experimental solutions. The decrease in DH and DO should be attributed to their consumption in the systems. DH showed more vigorous fluctuations than DO, which also caused significant variations in ORP. Compared to other treatments, the sterilized control and nitrate-free microcosms consumed less DH and DO, while their ORP values stayed relatively stable between −200 mV and −300 mV. The presence of 30 and 60 mg L−1 nitrate significantly increased the consumption of DH and DO, causing an increased ORP. The high nitrate concentration of 240 mg L−1 consumed the most DH, but less DO than lower nitrate concentrations, which induced the highest ORP above zero. Overall, ORP in the sterilized control group was maintained between −300 mV and −200 mV, indicating an anaerobic state. In contrast, the ORP in the nitrate-free group rapidly decreased from −100 mV to −250 mV, also reflecting an anaerobic condition. In the 30 and 60 mg L−1 nitrate groups, the ORP fluctuated between anaerobic and aerobic states. In the 240 mg L−1 nitrate group, the ORP gradually increased from −300 mV to 10 mV within 4 days, indicating a transition from an anaerobic to an aerobic state. It has been demonstrated that the rate of anaerobic dechlorination of TCE is optimal at a redox potential of −260 mV,37 while aerobic metabolism of TCE occurs at potentials above 50 mV.38 As shown in Fig. 1a, the ORP in the experimental group varied from −300 mV to 30 mV, indicating that the alternation between anaerobic and aerobic states in the system is more favourable for TCE removal. In particular, the removal of TCE was more significant during the transition from anaerobic to aerobic conditions. The pH of all experimental groups was slightly alkaline, and nitrate addition caused a slight increase in pH.

The variations of DH and DO in the nitrate-containing groups demonstrated that DH and DO were simultaneously consumed in the joint H2/O2 system. Nitrate concentrations adjusted the consumption balance between DH and DO. Consequently, ORP and pH were changed by the DH and DO consumption. These critical environmental parameters can change the microbial compositions reversibly, especially some functional microbes, thereby impacting TCE removal.

3.4 Microbial community evolution under different nitrate concentrations in the joint H2/O2 system

16S rRNA high-throughput sequencing was used to analyze the microbial community structure impacted by nitrate concentrations in the joint H2/O2 system. In all the experimental microcosms, the total microorganism counts ranged from 109–1010 copies per g (Fig. 4a). A total of 4765 amplicon sequence variants (ASVs) were obtained based on gene sequencing analysis. The core ASVs were analyzed and demonstrated using a Venn diagram in Fig. 5a. There were 539 core ASVs in the original sediment before the experiment, which increased to 705 upon introducing the joint H2/O2 system. However, adding nitrate at 30, 60, and 240 mg L−1 concentrations decreased the core ASV to 316, 380, and 281, respectively. Only 133 ASVs were common across all groups, indicating that adding different nitrate concentrations altered the microbial community structure in the joint H2/O2 system.
image file: d5ew00046g-f4.tif
Fig. 4 Variation in the number of microorganisms (a), TCE aerobic co-metabolizing (b), TCE anaerobic dechlorinating (c) and denitrifying microbes (d) in the sediments before and after 5th day of experiment at different nitrate concentrations.

image file: d5ew00046g-f5.tif
Fig. 5 Venn diagram of microbial community core ASV (a) and PCoA changes of microbial communities in microcosms (b) at different nitrate concentrations.

Chao1 and observed species indices were utilized to indicate microbial community richness, while Shannon and Simpson's indices were employed to characterize microbial community diversity, as detailed in Table S2. Following a 5-day experimentation period in the joint H2/O2 system, richness and diversity were highest in the nitrate-free group compared to the start point. However, the addition of nitrate led to a decrease in richness and diversity across all supplemented groups. Notably, as nitrate concentration increased, there was a corresponding decline in community richness and diversity. These results further demonstrate that nitrate concentration is a key determinant for changes in microbial community structure in the joint H2/O2 system.

Clustering and principal coordinate analysis (PCoA) using Bray–Curtis distance revealed the evolutionary pathways of microbial communities between the different nitrate concentrations, as depicted in Fig. 5b. The horizontal and vertical axes accounted for 70.1% and 14.9% of the variance in microbial community structure, respectively. The microbial communities within each group exhibited variation in the direction opposite to PCo1. In contrast to the nitrate-free group, introducing nitrate induced more pronounced changes in community structure, with more significant divergence observed in the direction opposite to PCo2.

The microbial community composition focusing on the top 50 abundances in each nitrate concentration is depicted in Fig. 6. In the original sediments, Pseudomonas (39.63%) was the dominant genus, which reduced to 36.46% after the 5-day introduction of the joint H2/O2 system, and to 32.79–33.21% after the introduction of nitrate. Geobacter (21.75%) was the second dominant genus; its relative abundance was reduced to 7.96% after introducing H2/O2 and decreased to 0.69–1.32% after adding 30–240 mg L−1 nitrate. Hydrogenophaga gradually increased from 0.99% to 30.31% in relative abundance and emerged as the dominant genus in the mixed H2/O2 and nitrate systems. Methyloversatilis had a low relative abundance in the original sediments, which rapidly increased to 19.46% upon adding 30 mg L−1 nitrate, after which its abundance decreased with increasing nitrate concentrations.


image file: d5ew00046g-f6.tif
Fig. 6 Variations in relative abundance of microbial community composition in the sediments before and after 5th day of experiment at different nitrate concentrations.

Pseudomonas is frequently recognized as a fundamental component of the bacterial community capable of degrading TCE through co-metabolism, utilizing substrates such as phenol and toluene.5,16Pseudomonas is also capable of aerobic denitrification, with certain Pseudomonas strains carrying the narG gene, which encodes an enzyme that reduces NO3 to NO2.5,39,40Hydrogenophaga has been identified as a hydrogen-oxidizing bacteria,41 capable of fixing CO2 using H2 acting as an electron donor and O2 as an electron acceptor.42,43Hydrogenophaga was found to synthesize enzymes for the aerobic metabolism of TCE, contributing to its biodegradation.17,44,45 Additionally, the genus can utilize nitrate as the sole nitrogen source to support its growth and remove nitrate under aerobic conditions,46 and it is also capable of denitrifying nitrate using H2 as an electron donor.47Methyloversatilis can produce enzymes that facilitate aerobic co-metabolic degradation of TCE.9 It has also been identified as a denitrifying bacterium, with Methyloversatilis universalis FAM5 being able to reduce nitrate to nitrite.48,49Geobacter is an organohalide-respiring bacterium that mediates TCE reductive dechlorination to cis-dichloroethylene (cDCE), playing a significant role in anaerobic dechlorination processes.30,50,51 No reports show that Geobacter is related to denitrification.

The variations in the numbers of aerobic co-metabolizing-, anaerobic dechlorinating-, and denitrifying functional bacteria are shown in Fig. 4(b–d). The bacteria with bi-functions of TCE aerobic co-metabolic degradation and denitrification, i.e., Pseudomonas, Hydrogenophaga, and Methyloversatilis, were dominant in the potential TCE aerobic co-metabolizing and denitrifying microbial communities. Among them, under a high nitrate concentration of 240 mg L−1, Pseudomonas and Hydrogenophaga declined, and Hydrogenophaga remained high due to the different resistance to nitrite. Geobacter numbers decreased significantly with the addition of H2/O2 and nitrate due to the negative effect of O2.52

3.5 Changes in functional genes under different nitrate concentrations in the joint H2/O2 system

The functional genes associated with biological dechlorination (tceA),16 aerobic co-metabolism (pmoA, phe)45,53 and denitrification (narG, nirS, nosZ)54 were quantified using qPCR to verify the effect of denitrification on the enrichment of anaerobic dechlorination and aerobic co-metabolism genes in the joint H2/O2 system. Fig. 7a illustrates the relative changes in three TCE degradation functional genes across different nitrate concentrations. The abundances of tceA and pmoA genes were lower than 2.4 × 104 copies per g, whereas that of phe was high up to 107 copies per g. Compared with the initial sediment group, the expression of tceA and pmoA genes decreased in joint H2/O2 in the presence of nitrate. In contrast, the phe genes in the nitrate-free group with joint H2/O2 (4.12 × 107 copies per g) increased relative to the original sediment (2.83 × 107 copies per g). This number significantly rose to 8.95 × 107 copies per g when nitrate increased to 240 mg L−1. These results proved that nitrate enhanced aerobic co-metabolism in the joint H2/O2 system.
image file: d5ew00046g-f7.tif
Fig. 7 Variation in gene abundances of tceA, pmoA, and phe (a) and narG, nirS, and nosZ (b) in the sediments before and after 5th day of experiment at different NO3 concentrations.

The denitrification functional gene changes are shown in Fig. 7b. Introducing H2/O2 increased the abundance of narG, nirS, and nosZ compared to the original sediment. The narG, nirS and nosZ genes encode enzymes that drives the conversion of nitrate to nitrite, nitrite to nitrous oxide, and nitrous oxide to nitrogen, respectively.55 Our previous research indicated that the abundance of functional genes related to denitrification could increase under the joint H2/O2 system.12 This study demonstrated that introducing nitrate increased the abundance of narG, nirS, and nosZ genes, favoring the denitrification process to the nitrite and nitrous oxide conversion stages. However, the high nitrate concentration of 240 mg L−1 showed lower denitrification functional genes than 60 mg L−1, consistent with the trend of denitrification functional microbes due to nitrite accumulation.

3.6 Mechanism of the nitrate effect on TCE removal in the joint H2/O2 system

The experimental results showed that increased nitrate concentration from 0 mg L−1 to 240 mg L−1 enhanced the TCE removal rate, efficiency, and denitrification, while more DH and DO were consumed, which induced a higher ORP. It also caused evolution of microbial communities to accumulate microbes such as Pseudomonas, Hydrogenophaga, and Methyloversatilis with bi-functions of denitrifying and aerobic co-metabolizing TCE, which was further demonstrated by the increased gene abundance of phe and narG, nirS, and nosZ. The highest nitrate concentration of 240 mg L−1 inhibited denitrification.

The denitrification process necessitates reducing highly oxidized nitrate using organic or inorganic electrons; for instance, organic matter commonly serves as an electron donor in natural environments.56 Studies have shown that aerobic denitrifying microorganisms (Pseudomonas, Hydrogenophaga, etc.) can use organic matter as a carbon and energy source to perform aerobic denitrification, a process in which oxygen and nitrate act as the electron acceptors and the carbon source is the electron donor.57,58Hydrogenophaga can fix CO2 using H2 as an electron donor and O2 as an electron acceptor.42,43 Additionally, it can reduce nitrate using H2 as an electron donor.47 Heterotrophic denitrifying bacteria such as Methyloversatilis can also perform denitrification using carbon compounds as carbon sources.58 Certain autotrophic denitrifying bacteria within Pseudomonas can employ H2 as an electron donor for denitrification.59 Meanwhile, Pseudomonas, Hydrogenophaga, and Methyloversatilis can synthesize co-metabolizing degradative enzymes that facilitate the aerobic metabolism of TCE under aerobic conditions.9,16,17 It is also reported that in the presence of O2, TCE can serve as a growth substrate, providing a carbon and energy source for microbial cells.7

Therefore, the mechanism for the effect of nitrate on TCE removal in the joint H2/O2 system is proposed. Nitrate induces accumulation of denitrifying bacteria, such as Pseudomonas, Hydrogenophaga and Methyloversatilis, which possess denitrifying genes of narG, nirS, and nosZ. These bacteria reduce nitrate and nitrite using H2 as an electron donor and aerobically co-metabolize TCE or use TCE as a carbon source. Hydrogenophaga uses H2 as an electron donor and O2 as an electron acceptor to fix CO2 and produce organic compounds for the growth of the bacteria. However, a nitrate concentration of 240 mg L−1 can inhibit the accumulation of Pseudomonas and Methyloversatilis due to the remaining nitrite.

4 Conclusion

This study proves that introducing nitrate into the joint H2/O2 system significantly enhances TCE removal. The enhancement effect is pronounced with increasing nitrate concentrations, indicating a positive correlation between nitrate levels and TCE removal efficiency. Adding nitrate enriches denitrifying bacteria, such as Pseudomonas, Hydrogenophaga, and Methyloversatilis, capable of denitrification using H2 as an electron donor and aerobic TCE co-metabolism. This dual functionality of the microbes and the increased abundance of the aerobic co-metabolic gene phe suggest a synergistic mechanism by which nitrate promotes TCE removal in the joint H2/O2 system. However, a high nitrate concentration of up to 240 mg L−1 inhibits the accumulation of Pseudomonas and Methyloversatilis. Alternatively, it increases the abundance of Hydrogenophaga, which could use H2 and O2 to fix CO2 and provide organics for bacterial growth. The coexistence of H2 and O2 altered the redox state of the system, favouring aerobic co-metabolizing microorganisms and thereby enhancing aerobic co-metabolism processes. This observation suggests that organic pollutants amenable to aerobic co-metabolism may also undergo more efficient degradation in systems where nitrate, H2 and O2 co-exist.

The findings of this research underscore the importance of nitrate, along with H2 and O2, in influencing the microbial-mediated degradation of TCE. The results suggest that manipulating these electron donors and acceptors could be a viable strategy to enhance bioremediation outcomes. In areas with high concentrations of nitrate and TCE contamination, remediation can be achieved by introducing H2 and O2 systems. Conversely, remediation can be done in TCE-contaminated sites with low nitrate concentrations by supplementing the joint H2/O2 system with up to 60 mg L−1 of nitrate. This study provides technical guidance for the remediation of TCE and nitrate co-contamination in groundwater environments, offering a promising avenue for developing more effective environmental remediation technologies that leverage the interactive effects of H2, O2, and nitrate on microbial communities.

Data availability

Microbiological data for this article are available from the NCBI website at https://dataview.ncbi.nlm.nih.gov/object/PRJNA1206323?reviewer=jhknm0tverjns8r9vv6iv5orel.

Author contributions

Wenyi Huang: conceptualization, methodology, validation, formal analysis, software, writing – original draft and editing. Weiwei Ouyang: writing – review & editing. Haonan Bian: writing – review & editing. Hui Liu: supervision, project administration, funding acquisition, conceptualization, writing – review & editing.

Conflicts of interest

All authors declare no conflict of interest.

Acknowledgements

This work was supported by the National Key Research and Development Program of China (No. 2022YFC3702401) and the National Natural Science Foundation of China (No. 42277051).

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