In comparison, experimental results showed that both solution pH and temperature were significant for defining soluble Mn2+ removal using the MnOx(s)-coated media process; further, the impacts of pH on soluble Mn2+ removal were magnified under low temperature (<10 °C) conditions. Information presented in Table 2 shows the percentage of finished water soluble Mn2+ concentration values that exceeded the recommended Newport News Water Authority goal of 0.015 mg/L when sorted by pH and temperature for the full-scale Harwood's Mill plant data. As shown in Table 2, the percentage of finished water soluble Mn2+ concentration values exceeding the goal generally decreased as the solution temperature increased. Likewise, the percentage of finished water soluble Mn2+ concentration values exceeding the goal of 0.015 mg/L decreased as the pH increased within each temperature range. Finally, results presented in Table 2 also demonstrate that an increase in solution pH may at least partially mitigate the negative effects of low water temperature on Mn removal using MnOx(s)-coated filter media treatment systems.
Percentage of finished water soluble Mn concentration values exceeding the target of 0.015 mg/L as a function of water temperature and solution pH (data analyzed from Newport News Water Authority full-scale water plant operations)
. | Solution pH value . | |||
---|---|---|---|---|
Temperature . | 5.7–6.0 . | 6.0–6.3 . | 6.3–6.6 . | > 6.6 . |
<5 °C | 100 | 60 | 80 | 66 |
5–10 °C | 65 | 54 | 61 | 56 |
10–15 °C | 45 | 30 | 19 | 0 |
15–20 °C | 25 | 8 | 10 | 0 |
20–25 °C | 11 | 8 | 0 | 0 |
>25 °C | 6 | 5 | 0 | 0 |
. | Solution pH value . | |||
---|---|---|---|---|
Temperature . | 5.7–6.0 . | 6.0–6.3 . | 6.3–6.6 . | > 6.6 . |
<5 °C | 100 | 60 | 80 | 66 |
5–10 °C | 65 | 54 | 61 | 56 |
10–15 °C | 45 | 30 | 19 | 0 |
15–20 °C | 25 | 8 | 10 | 0 |
20–25 °C | 11 | 8 | 0 | 0 |
>25 °C | 6 | 5 | 0 | 0 |