Abstract
The H 2-based membrane biofilm reactor was used to remove nitrate from synthetic ion-exchange brine at NaCl concentrations from ∼3 to 30 g/L. NaCl concentrations below 20 g/L did not affect the nitrate removal flux as long as potassium was available to generate osmotic tolerance for high sodium, the H 2 pressure was adequate, and membrane fouling was eliminated. Operating pHs of 7-8 and periodic citric acid washes controlled membrane fouling and enabled reactor operation for 650 days. At 30 psig H 2 and high nitrate loading rates of 15 to 80 g/m 2 d, nitrate removal fluxes ranged from 2.5 to ∼6 g/m 2 d, which are the highest fluxes observed when treating 30 g/L IX brine. However, percent removals were low, and the H 2 pressure probably limited the removal flux.
Original language | English (US) |
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Pages (from-to) | 100-104 |
Number of pages | 5 |
Journal | Water Science and Technology |
Volume | 65 |
Issue number | 1 |
DOIs | |
State | Published - Jan 20 2012 |
Keywords
- Flux
- Membrane biofilm reactor
- NaCl
- Nitrate removal
ASJC Scopus subject areas
- Environmental Engineering
- Water Science and Technology