TABLE 1.
Process or balance | Parameters at pH 7/pH 5 under the indicated conditions |
|||
---|---|---|---|---|
Veillonella atypica |
Veillonella parvula |
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Anaerobic | Aerobic | Anaerobic | Aerobic | |
Oxidation (2H production [mM]) | ||||
Lactate utilization (Pyr + Ace + Pro)a | 0.959/1.075 | 0.377/0.380 | 0.525/0.603 | 0.224/0.148 |
Acetate production via oxidation (Ace – For)b | 0.353/0.359 | 0.180/0.146 | 0.332/0.350 | 0.070/0.053 |
Reduction (2H consumption [mM]) | ||||
Propionate production (Pro × 2)c | 0.935/1.110 | 0.075/0.079 | 0.279/0.177 | 0.000/0.000 |
NO3– reduction (NO2–)d | 0.149/0.214 | 0.020/0.021 | 0.544/0.687 | 0.012/0.029 |
Reduction-oxidation balance ([a + b]/[c + d]) | 1.21/1.08 | 5.89/5.28 | 1.04/1.10 | 24.47/6.99 |
The amount of lactate utilized was estimated from the total amounts of pyruvate (Pyr), acetate (Ace), and propionate (Pro). One mole of 2H (reducing power) can be produced by oxidizing 1 mol of lactate to 1 mol of Pyr (Fig. 5).
The amount of acetate produced via oxidation was estimated by subtracting the amount of formate (For) produced from the amount of Ace produced. One mole of 2H can be produced by oxidizing 1 mol of Pyr to 1 mol of Ace (Fig. 5).
Two moles of 2H can be consumed by reducing 1 mol of Pyr to 1 mol of Pro (Fig. 5).
One mole of 2H can be consumed by reducing 1 mol of NO3– to 1 mol of NO2– (Fig. 5).