The primary goal of this research
was to investigate several water
treatment unit operations for converting RO concentrate produced from
treated municipal wastewater into potable water. The secondary goal
was to evaluate the use of an electrochemical cell for producing the
reagents needed to operate a fluidized bed crystallization reactor
(FBCR), regenerate ion exchange media, and produce a ferric iron coagulating
agent. The effectiveness of the pretreatment processes to prevent
membrane fouling were evaluated for conventional and high-efficiency
reverse osmosis (HERO). Fluidized bed crystallization removed 93 to
>97% of hardness ions, 42% of silica, and 6.5% of total organic
carbon.
Membrane fouling during HERO was lower than that for conventional
RO for pretreatment using fluidized bed crystallization and ion exchange.
However, conventional RO with ferric iron coagulation following fluidized
bed crystallization and ion exchange showed the least membrane fouling
and increased recovery in the second stage RO by 470%. The use of
an electrochemical cell for generating the reagents needed for the
pretreatment processes was evaluated. Energy costs for operating the
electrochemical cell for making acid, base, and ferric iron coagulant
were 4.1 kWh per m3 of RO concentrate. The use of electrochemically
generated reagents combined with fluidized bed crystallization produces
no waste solutions from the pretreatment processes.