Studies of the thermodynamics and kinetics of dyeing over the past 60-70 years have not resulted in complete acceptance for one mechanism for the dyeing process. Contrary to the two existing explanations of wool-dye isotherm data (the Gilbert-Rideal and Donnan theories), the uptake of the acid dye used in this study conforms to the law of mass action. In addition, although it has generally been accepted that the kinetics of wool dyeing is diffusion controlled, the uptake rate of the acid dye used in this study can be modeled by a second-order rate expression based on the formation of a protein-dye complex as the rate determining step. The mechanism developed from this study involves the dye and other anions present in the dye solution interacting independently with the wool, rather than the dye displacing smaller anions in a strict ion exchange manner.
: Five low rank, coal-based adsorbents, i.e. coal, grus, two chars, and an activated carbon were used to adsorb a low molecular weight organic compound from aqueous solution. The rates of adsorption were found to conform to pseudo ürst order kinetics with good correlation (r2 greater than 0.996). This kinetic model was used to calculate pseudo ürst order rate constants min-1) and rela-(k 1 º tive rate constants (rate constant/unit mass of adsorbent, for the adsorption process. k 1 / min-1 g-1)Rate properties have been explained in terms of both a diþ usion and chemically controlled rate determining step. Rate constants for the üve adsorbents vary as expected on the basis of their physical properties, that is slowest for grus (compressed coal) and fastest for the activated carbon.
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