| Literature DB >> 31635215 |
Pierre Albina1,2, Nadège Durban3,4, Alexandra Bertron5, Achim Albrecht6, Jean-Charles Robinet7, Benjamin Erable8.
Abstract
Bacterial respiration of nitrate is a natural process of nitrate reduction, which has been industrialized to treat anthropic nitrate pollution. This process, also known as "microbial denitrification", is widely documented from the fundamental and engineering points of view for the enhancement of the removal of nitrate in wastewater. For this purpose, experiments are generally conducted with heterotrophic microbial metabolism, neutral pH and moderate nitrate concentrations (<50 mM). The present review focuses on a different approach as it aims to understand the effects of hydrogenotrophy, alkaline pH and high nitrate concentration on microbial denitrification. Hydrogen has a high energy content but its low solubility, 0.74 mM (1 atm, 30 °C), in aqueous medium limits its bioavailability, putting it at a kinetic disadvantage compared to more soluble organic compounds. For most bacteria, the optimal pH varies between 7.5 and 9.5. Outside this range, denitrification is slowed down and nitrite (NO2-) accumulates. Some alkaliphilic bacteria are able to express denitrifying activity at pH levels close to 12 thanks to specific adaptation and resistance mechanisms detailed in this manuscript, and some bacterial populations support nitrate concentrations in the range of several hundred mM to 1 M. A high concentration of nitrate generally leads to an accumulation of nitrite. Nitrite accumulation can inhibit bacterial activity and may be a cause of cell death.Entities:
Keywords: acclimation; denitrifying bacteria; high nitrate concentration; high pH; hydrogenotrophic denitrification; mineral carbon; nitrite accumulation
Mesh:
Substances:
Year: 2019 PMID: 31635215 PMCID: PMC6834205 DOI: 10.3390/ijms20205163
Source DB: PubMed Journal: Int J Mol Sci ISSN: 1422-0067 Impact factor: 5.923
Figure 1Overview of the four steps of microbial denitrification.
Figure 2Schematic representation of the canonical respiratory chain of denitrification after [29,30,31].
Figure 3Schematic representation of the transcriptional regulation of the expression of genes encoding the different enzymes involved in denitrification in P. denitrificans [31,37].
Experiments with activated sludge cultures highly concentrated in nitrate, acclimation procedure and nitrite accumulation.
| Experimental Protocol | Acclimation Procedure | Nitrate (In Culture) | Nitrite Build-Up | Ref. |
|---|---|---|---|---|
| Ca increase from 50 to 550 g/L at 45 mM nitrate, pH 8.5 | Medium diluted x2 during 2 weeks | 45 mM | max 2.5 mM | [ |
| Nitrate increase to 580 mM and ionic strength from 0.8 to 3.0 in SBR, pH 9 | Stepwise nitrate increase from 100 mM to 580 mM in about 6 weeks | 100 mM | 70 mM | [ |
| Test at 140 mM nitrate in a batch reactor, pH 9/ Nitrate increase to 1000 mM in a continuous reactor | Stepwise nitrate increase | 140 mM | 50 mM 1 | [ |
| Nitrate increase to 640 mM in SBR | Step-wise nitrate increase in the medium from 120 mM to 640 mM in 8 weeks | 430 mM | 420 mM | [ |
| NaCl stress decrease from 11 to 0 % at 430 mM, in continuous reactor | Stepwise nitrate increase from 140 mM to 430 in 3 weeks | 430 mM (influent) | 70–360 mM (effluent) | [ |
| pH increase from pH 7.5 to 12 in SBR | Step-wise pH increase from 7.5 to 11.5 in 8 weeks | 60 mM | 30–55 mM (high pH) | [ |
1 Results of the batch culture.
Figure 4Proportions of nitrite reduced and accumulated according to the initial nitrate concentration in bacterial cultures after [6,59,63,64,65].
Figure 5The regulatory [NiFe] hydrogenase and membrane-bound [NiFe] hydrogenase in Ralstonia eutropha after [69,71].
Phyla producing [NiFe], [FeFe] and [Fe] hydrogenase, with examples of strains.
| Phylum | Specie, Genus | Hydrogenase | Ref. |
|---|---|---|---|
| Crenarchaeota (Archaea) |
| [NiFe] | [ |
| Euryarchaeota (Archaea) |
| [Fe], [NiFe] | [ |
| Actinobacteria |
| [NiFe] | [ |
| Aquificae |
| [NiFe] | [ |
| Chloroflexi |
| [NiFe], [FeFe] | [ |
| Cyanobacteria |
| [NiFe] | [ |
| Firmicutes |
| [NiFe],[FeFe] | [ |
| Proteobacteria |
| [NiFe], [FeFe] | [ |
| Thermotogae |
| [FeFe] | [ |
| Spirochaetes |
| [FeFe] | [ |
Overview of nitrate maximal reduction rates in hydrogenotrophic cultures testing different pH and nitrate concentrations ranges.
| Inoculum | Experimental Set-Up | pH | Nitrate | Nitrate Maximal Reduction Rate | Ref. |
|---|---|---|---|---|---|
| Activated sludge | Continuous reactor, heterotrophy or hydrogenotrophy | 6.5–8.7 | 0.8–2.3 | ND | [ |
| Consortium | Pressured Batch reactor | 7.1 | 0.07–0.7 | 356.4 mM/d | [ |
|
| Continuous and batch reactors | 7.1–9 | 1.8–3.2 | 50.0 mM/d | [ |
|
| Semi-batch reactors | 6.5–9.5 | 40 | 8.4 mM/gDW/d 1 | [ |
| Activated sludge | Batch reactors | 6.4–7 | 0.5–14.3 | 5.5 mM/d | [ |
| Activated sludge | Batch and continuous reactors | ND | 14 | 1.3 mM/d | [ |
| Activated sludge | Continuous reactor | 7–9.5 | 1 | 31 mM/d | [ |
| Activated sludge | Sequencing batch reactors | 7–9.5 | 1.4 | 27.4 mM/d | [ |
1 Expressed in terms of dry weight.
Calculation of pH in a culture buffered with carbonate and fed with acetate according to the reduced nitrate concentration.
| Equivalents | [HCO3−]produced ⇔ 7/8 [NO3−]reduced [CO32−] produced ⇔ 3/8 [NO3−]reduced |
| Final carbonate concentrations | [CO32−]final = [CO32−]initial + [CO32−]produced = [CO32−]initial + 3/8 [NO3−]reduced [HCO3−]final = [HCO3−]initial + [HCO3−]produced = [HCO3−]initial + 7/8 [NO3−]reduced |
| Henderson-Hasselbalch equation |
|
| Final equation |
|
Calculation of pH in culture buffered with carbonate and fed with hydrogen according to the reduced nitrate concentration.
| Equivalents | [HCO3−]consumed ⇔ [OH−]produced ⇔ [NO3−]reduced |
| Final carbonate concentrations | [CO32−]final= [CO32−]initial + [CO32−]produced = [CO32−]initial + [NO3−]reduced |
| Henderson-Hasselbalch equation |
|
| Final equation1 |
|
1: does not apply if [HCO3−]initial < [NO3−]reduced, in this case, the pH is directly calculated from [OH−].
Overview of nitrate maximal reduction rates in heterotrophic cultures testing different pH and nitrate concentrations ranges.
| Inoculum | Experimental Set-Up | pH | Nitrate | Nitrate Maximal Reduction Rate | Ref. |
|---|---|---|---|---|---|
|
| Batch reactor | ND | 17 | 36 mM/d | [ |
|
| Batch reactor, an/aerobic transition | 5.5–9.5 | 25 | 60 mM/d | [ |
|
| Batch reactor, high cell density | 6.4–9.2 | 25 | 4887 mM/d | [ |
|
| Continuous reactor an/aerobic transition | 6.8–7.5 | 25 | 6 mM/d | [ |
| Activated sludge | Sequencing batch reactors | 6.5–9 | 192 | 600 mM/d | [ |
| Activated sludge | Batch reactor | 10–12 | 15 | 2 mM/d | [ |
| Activated sludge | Sequencing batch reactors | 7.2 | 120–645 | 1710 mM/d | [ |
| Activated sludge | Sequencing batch reactors | 7.5–12 | 120 | 1177 mM/d | [ |
| Activated sludge | Sequencing batch reactors | 7.5–9 | 192–580 | 564 mM/d | [ |
|
| Batch reactor | 7.5–9 | 1006 | ND | [ |
| Activated sludge | Sequencing batch reactors | 8.5 | 42 | 137 mM/d | [ |
| Activated sludge | Expanded granular sludge bed | 6–8 | 142–1000 | 99.9 % removal efficiency | [ |
Figure 6Protective mechanisms of Bacillus sp. cultivated at pH 10.5, adapted from after [111,117].
Figure 7Literature overview of the experiments of bacterial denitrification conducted at alkaline pH and/or at high nitrate concentrations.