Abstract
The application of the forward osmosis membrane bioreactor (FO-MBR) requires further investigation in the area of process optimization. In current study, different operational parameters for improving the overall efficiency of FO-MBR were studied and optimized in batch and semi-continuous experiments. The effect of osmotic back-washing, cross-flow velocity of the feed solution (activated sludge), and particle size were studied on the FO-MBR flux. All batch experiments were of 8 h duration, comprising 7 h filtration and 1 h osmotic backwash. It was found that osmotic backwashing was ineffective for complete flux recovery in a hollow fibre FO-MBR, due to severity of the fouling caused by the activated sludge feed in 'active layer facing draw solution' mode. A slightly better recovery was observed however with a single 60 min backwash as compared to 2 backwash cycles of 30 min each or 3 backwash cycles of 20 min each. A cross-flow velocity of 0.105 m/s proved optimum. Higher velocities caused a breakdown of flocs and reduced the mean particle size, the latter resulting in lower water flux. Similarly, lower cross flow velocities were not able to provide effective membrane scouring, resulting in lower water flux. The particle size decreased with operational time in the FO-MBR. It was also established that, above the optimum cross flow velocity, flux is inversely proportional to the difference between the initial and final particle size of sludge.