ABSTRACT:A 2,2Ј-dihydroxyazobenzene (DHAB) derivative was attached to a chloromethylated cross-linked polystyrene derivative in view of high affinity of DHAB for uranyl ion. Chloromethyl groups of the resin were converted to quaternary ammonium ions by treating with tertiary amines. Capacity of the resins for uranyl-uptake was measured, revealing that about 20 mg of uranium can be complexed to 1 g of the resins. Formation constants (K f ) for uranyl complexes of the resins were determined. In the presence of Ͼ0.1 M bicarbonate ion at pH 8.10, log K f of about 15 was obtained. As bicarbonate concentration was lowered, K f decreased considerably. Degrees of uranyluptake from rapidly flowing uranyl solutions were measured, and the results suggested that rate of uranyl-uptake may not impose a major barrier to application of the resins in uranium extraction from seawater. Uranium extraction from seawater with the resins was carried out on the east coast of Korean peninsula. The amount of uranium extracted from seawater was about 10 g/g resin. This is not satisfactory for economical processes of uranium recovery from seawater. Results of the present study, however, suggested that modification of the DHAB-containing resins can improve uranyl-binding ability, probably leading to economical recovery of uranium from seawater. In addition, simulation of uranyl-binding processes in seawater with the laboratory procedures developed in this study was satisfactory.

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A 2,2′‐dihydroxyazobenzene (DHAB) derivative was attached to a chloromethylated cross‐linked polystyrene derivative in view of high affinity of DHAB for uranyl ion. Chloromethyl groups of the resin were converted to quaternary ammonium ions by treating with tertiary amines. Capacity of the resins for uranyl‐uptake was measured, revealing that about 20 mg of uranium can be complexed to 1 g of the resins. Formation constants (Kf) for uranyl complexes of the resins were determined. In the presence of >0.1 M bicarbonate ion at pH 8.10, log Kf of about 15 was obtained. As bicarbonate concentration was lowered, Kf decreased considerably. Degrees of uranyl‐uptake from rapidly flowing uranyl solutions were measured, and the results suggested that rate of uranyl‐uptake may not impose a major barrier to application of the resins in uranium extraction from seawater. Uranium extraction from seawater with the resins was carried out on the east coast of Korean peninsula. The amount of uranium extracted from seawater was about 10 µg/g resin. This is not satisfactory for economical processes of uranium recovery from seawater. Results of the present study, however, suggested that modification of the DHAB‐containing resins can improve uranyl‐binding ability, probably leading to economical recovery of uranium from seawater. In addition, simulation of uranyl‐binding processes in seawater with the laboratory procedures developed in this study was satisfactory. © 1999 John Wiley & Sons, Inc. J Polym Sci A: Polym Chem 37: 3169–3177, 1999

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