TABLE 3.
No. of N. eutropha cells (ml−1) | Conversion rates (μmol reactor−1 h−1)
|
NO2−/NH3 ratio | Sp act (μmol of NH4+ g of protein−1 h−1)
|
|||||
---|---|---|---|---|---|---|---|---|
Ammonia | Nitrite | NO2b | NO | Nitrate | B. anammoxidansc | N. eutrophad | ||
0e | 141.4 | 187.9 | 0 | 0.01 | 36.8 | 1.33 | 4,423 | |
107 | 149.9 | 191.4 | 14.4 | 13.5 | 38.1 | 1.28 | 4,579 | 1,080 |
5 × 107 | 183.8 | 183.2 | 70.6 | 71.2 | 41.3 | 1.00 | 4,963 | 1,462 |
108 | 226.2 | 185.8 | 129.4 | 119.1 | 49.3 | 0.82 | 5,525 | 1,545 |
The reactor with the anammox biomass was supplemented with 0, 107, 5 × 107, or 108 N. eutropha cells ml−1. The consumption and production rates were calculated on the basis of the substrates added to the reactor and the products leaving the reactor. The standard deviation for five replicate experiments was less than ± 5%.
In sterile control experiments, the NO2 consumption resulting from the reaction of NO2 with water was determined. The values obtained were subtracted from the data obtained with cells.
The specific ammonia oxidation activity of B. anammoxidans was calculated on the basis of nitrate production.
The specific ammonia oxidation activity of N. eutropha was calculated on the basis of NO2 consumption and NO production.
The anammox biomass contained about 2 × 103 Nitrosomonas cells ml−1.