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In contrast to N -phenylthiophthalimide, the regeneration of PhSeBr is strongly exothermic by 14.7 kcal mol 1 with a barrier of only 15.3 kcal mol 1 (for details see Supplementary Fig

Further analysis, separating utility consumption from other biorefinery processes, reveals that energy consumption (reactor operation and biomass recovery) represents 96.2% of the costs, while water consumption, despite evaporative losses (30,000 m 3 ha 1 year 1 ), constitutes only 0.5% of the total costs (Acin et al

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