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An adsorption-based kinetic model was sought that accurately predicts simultaneous saccharification and fermentation (SSF) of insoluble lignocellulosic substrates in batch and continuous reactors. With a common set of three heuristic parameters, a hydrolysis rate equation of the form r = {k [times ] (1 [minus ] x) n + c} [times ](ES)/(C[cedil ] s ) in conjunction with Langmuir adsorption...
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