Selective Coagulant Recovery from Water Treatment Plant Residuals Using Donnan Membrane Process

• Published in: Environmental science & technology 2003-10, Vol.37 (19), p.4468-4474
• Main Authors: Prakash, Prakhar, SenGupta, Arup K
• Format: Article
• Language: English
• Subjects: Alum Compounds - isolation & purification; Aluminum; Applied sciences; Electrochemistry; Exact sciences and technology; Filtration; Flowers & plants; Ion Exchange; Membranes; Membranes, Artificial; Models, Theoretical; Osmosis; Other industrial wastes. Sewage sludge; Particle Size; Pollution; Sewage - chemistry; Waste Disposal, Fluid - methods; Wastes; Water Purification - methods; Water treatment; Water treatment plants
• ISSN: 0013-936X; 1520-5851
• DOI: 10.1021/es030371q

Fouling of membrane surfaces by particulate matter and large organic molecules is relatively common for pressure-driven membrane processes, namely, reverse osmosis (RO), nanofiltration (NF), and ultrafiltration (UF). Donnan membrane process (DMP) or Donnan Dialysis is driven by electrochemical potential gradient across a semipermeable ion exchange membrane. Theoretically, DMP is not susceptible to fouling by fine particulates and/or large organic molecules. According to information available in the open literature, however, DMP has not been tried to treat slurry or sludge with relatively high concentration of suspended solids or large organic molecules. This study presents the salient results of an extensive investigation pertaining to selective alum recovery from water treatment residuals (WTR) using DMP. Water treatment plants use alum, Al2(SO4)3·14H2O, as a coagulant, alum being finally converted and discharged as insoluble aluminum hydroxide along with natural organic matters (NOM), suspended solids, and other trace impurities. One commercial cation exchange membrane, namely Nafion 117 from DuPont Chemical Co., was used in the study for treating WTR obtained from two different water treatment plants in Pennsylvania. A series of laboratory tests confirmed that over 70% of alum is easily recoverable, and recovered alum is essentially free of particulate matter, NOM, and other trace metals. Most importantly, after repeated usage in the presence of high concentration of NOM and suspended solids, there was no noticeable decline in aluminum flux through the membrane, i.e., membrane surface fouling was practically absent. The DMP process involves coupled transport of Al3+ and H+ across the cation exchange membrane, and intramembrane transport was the rate-limiting step. Experimentally determined aluminum−hydrogen interdiffusion coefficient (D̄Al - H) values within the membrane were quite high (∼10-6 cm2/s) under representative conditions, thus confirming high alum recovery rate. DMP was also found equally effective in recovering Fe(III) based coagulants from WTR.