Draw solution recovery using direct contact membrane distillation (DCMD) from osmotic membrane bioreactor (Os-MBR)

This study investigates the application of direct contact membrane distillation (DCMD) for concentrating diluted draw solution (DS) from osmotic membrane bioreactor (Os-MBR). A flat sheet polytetrafluoroethylene (PTFE) hydrophobic membrane with a pore size of 0.2 mu m was used to perform the experiments. The effect of circulation velocity, temperature, and channel spacer effect on permeate flux were investigated. Results indicated that the permeate flux increased with feed temperature and velocity. Spacers enhanced permeate flux up to 35% and the sequence of spacer design in terms of flux was: diamond design > ladder design > without spacer. DCMD process was also applied during long period for re-concentration of draw solution of two organic (CH3COONa & Mg(CH3COO)(2)) and three inorganic salts (NaCl, MgCl2, & CaCl2) under the optimal operating conditions. The optimal DCMD condition was achieved using aqueous NaCl solution. Mg(CH3COO)(2) gave prolong operational period in OsMBR-MD and required more MD membrane flushing. MD membrane flushing followed the order as Mg(CH3COO)(2) > CH3COONa > CaCl2 > MgCl2 > NaCl. For all organic and inorganic DS, the DCMD system was able to achieve DS recovery as per Os-MBR requirement and also produced good quality product water due to high TDS and contaminant rejection (> 99%).