“…The rejection of an RO membrane for an organic solute depends on the membrane material, molecular weight cutoff, surface charge, and surface morphology, as well as solute properties (i.e., structure, molecular weight, molecular geometry, p K a , and K ow ) . The low molecular weight of nitromethane (61.04 g/mol), its neutral charge (with a p K a of 10.2 at a feedwater pH of 8.37), and its low log K ow (−0.35) are consistent with poor rejection by RO membranes. − The bench-scale results generally agree with the data collected from the full-scale RO processes, which show nitromethane rejections of 37, 29, 31, and 34% for plants A, B, C, and D, respectively, suggesting that poor nitromethane rejection is generally low during RO, both in clean and fouling environments. The higher rejections observed at the full scale are likely due to fouling deposition on the RO membranes.…”