Dispesed alkaline substrate (das) a novel option for the passive treatment of waters with high metal concentrations

  1. RÖTTING TOBIAS, STEFAN
Dirigida por:
  1. Carlos Ayora Ibáñez Director/a
  2. Jesús Carrera Ramírez Codirector/a

Universidad de defensa: Universitat Politècnica de Catalunya (UPC)

Fecha de defensa: 25 de mayo de 2007

Tribunal:
  1. José Luis Cortina Pallás Presidente/a
  2. José Miguel Nieto Liñán Secretario
  3. Steve Banwart Vocal
  4. Albert Soler Gil Vocal
  5. Adam Jarvis Vocal

Tipo: Tesis

Teseo: 137979 DIALNET

Resumen

Acid mine drainage (AMD) and other metal-polluted anthropogenic discharges are a major cause of water contamination world-wide. Conventional treatment plants are expensive to operate, and application at remote sites may be impractical. Passive treatment systems, which only require naturally available energy sources and infrequent maintenance, may be an economical option to decontaminate these waters. Nevertheless, they are prone to clogging and passivation (loss of permeability or reactivity, respectively) when used to treat water with high metal concentrations or high acidity loads. Many passive treatment systems are based on calcite dissolution that removes trivalent metals such as Fe(III) and Al, but not divalent metals (e.g. Zn, Mn, Cu, Pb, Ni, Cd). To overcome these problems, a novel Dispersed Alkaline Substrate (DAS) was developed and tested in this dissertation. DAS consists of a fine-grained alkaline reagent (e. g. calcite or MgO [caustic magnesia] sand) mixed with a coarse inert matrix (e. g. wood chips). Calcite-DAS was capable of treating Acid Mine Drainage with an inflow net acidity of 1350-2300 mg/L as CaCO3, removing an average 1200 mg/L as CaCO3 in laboratory columns. The substrate functioned without clogging during over one year at an acidity load of 150 g acidity/m2·day, five times the loading rate recommended for conventional passive treatment systems. Al, Fe(III), Cu and Pb were virtually eliminated and some Zn, Ni and Cd were removed at low flow rates. The system was also tested at a field pilot plant constructed at Monte Romero mine (Huelva Province, SW Spain), where a 3 m3 calcite-DAS tank eliminated a median net acidity of 900 mg/L as CaCO3 at an acidity load of 600 g acidity/m2·day and an Al-load of 30 g/m2·day. However, the tank eventually clogged due to formation of an Al- and gypsum-rich hardpan within the substrate. Clogging by Al-precipitates probably could be retarded by lower Al-loads.