This paper aims to review the problem of colour in textile ef¯uents, the different classes of dyes available and their contribution to the problem. Through new regulations, pressure is being placed on water companies all over the world to reduce the amount of colour in sewage ef¯uent. Dyes exhibit low toxicity to mammals and aquatic organisms and therefore colour consents are normally applied for aesthetic and industrial reasons rather than for prevention of toxicity. The absorbance, ADMI values and concentrations of dyes in ef¯uent are examined here with particular reference to reactive azo dyes used in cotton processing. Colour consents, the problem of colour in textile wastewaters and the importance for research in this area are also discussed. Dye concentrations of 0.01 g dm À3 up to 0.25 g dm À3 have been cited as being present in dyehouse ef¯uent, depending on the dyes and processes used. ADMI values ranged from 50 to 3890 units for the dyeing of cotton. It was concluded that 1500 ADMI units was a reasonable value to aim for when simulating coloured ef¯uents. Simulated textile ef¯uents may be used for research purposes. These should resemble real wastes as closely as possible, but it is often dif®cult to replicate the ADMI values, absorbance and spectra of real ef¯uents. The concentrations of dye used in simulated ef¯uents examined in literature varied from 0.01 g dm À3 to 7 g dm À3.As absorbance and ADMI values change with the types of dye used, it is dif®cult to relate these values to dye concentrations. A concentration of 0.18 g dm À3 of a Red or Yellow dye or 0.43 g dm À3 of a blue dye would provide an ADMI of approximately 1500 units and ®ts within the range of dye concentrations presented in literature. A dye mixture simulating colour in a real textile ef¯uent is suggested and some limitations of simulating actual wastewaters discussed.

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The operational stability of peroxidases was considerably enhanced by generating hydrogen peroxide in situ from glucose and oxygen. For example, the total turnover number of microperoxidase-11 in the oxidation of thioanisole was increased sevenfold compared with that obtained with continuous addition of H(2)O(2). Coimmobilization of peroxidases with glucose oxidase into polyurethane foams afforded heterogeneous biocatalysts in which the hydrogen peroxide is formed inside the polymeric matrix from glucose and oxygen. The total turnover number of chloroperoxidase in the oxidation of thioanisole and cis-2-heptene was increased to new maxima of 250. 10(3) and 10. 10(3), respectively, upon coimmobilization with glucose oxidase. Soybean peroxidase, which normally shows only classical peroxidase activity, was transformed into an oxygen-transfer catalyst when coimmobilized with glucose oxidase. The combination catalyst mediated the enantioselective oxidation of thioanisole [50% ee (S)] with 210 catalyst turnovers.