2009
DOI: 10.1016/j.apcata.2009.06.025
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New and efficient procedure for the oxidation of dioxybenzylic alcohols into aldehydes with Pt and Pd-based catalysts under flow reactor conditions

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Cited by 29 publications
(11 citation statements)
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“…The continuous-flow oxidation of vanillyl alcohol to vanillin was reported by Semenov et al 148 Yields up to 98% were obtained within the first hour of run time (Scheme 1). The mesoreactor consisted of quartz tubing (7 mm diameter, 1 mL) and was loaded with palladium catalyst on Subunit (a commercially available supporting matrix).…”
Section: Transition Metal-catalyzed Aerobic Oxidation Processes In Comentioning
confidence: 96%
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“…The continuous-flow oxidation of vanillyl alcohol to vanillin was reported by Semenov et al 148 Yields up to 98% were obtained within the first hour of run time (Scheme 1). The mesoreactor consisted of quartz tubing (7 mm diameter, 1 mL) and was loaded with palladium catalyst on Subunit (a commercially available supporting matrix).…”
Section: Transition Metal-catalyzed Aerobic Oxidation Processes In Comentioning
confidence: 96%
“…Oxidation of vanillyl alcohol to vanillin under flow reaction conditions. 148 Kobayashi et al described the first quantitative aerobic oxidation process of both primary and secondary alcohols to its respective aldehydes and ketones in a microreactor. 149 , 150 The reactor consisted out of a wall coated, gold-immobilized, capillary column.…”
Section: Transition Metal-catalyzed Aerobic Oxidation Processes In Comentioning
confidence: 99%
“…Conversion efficiency of VAL to VN was determined as follows [46,60,61]: Turn-over frequencies (TOFs) per surface atom were calculated according to:…”
Section: Photocatalytic Reactionmentioning
confidence: 99%
“…Both wallcoated [275] and packed bed microreactor configurations [183,276,277] have been used for this purpose. Biomass oxidations performed in milli-scale (packed bed) reactors, may benefit similarly in terms of the desired product yield from transport intensification and a precise process control there, as demonstrated in the conversions of HMF to FFCA/FDCA, [269] glycerol to different C 2 /C 3 aldehydes and acids, [272][273][274] glucose to gluconic acid, [278] bioethanol to acetic acid, [279] lignin to vanillin, [280] and its derivatives (e. g., vanillyl alcohol to vanillin and piperonyl alcohol to piperonal) [281] (Figure 4). Furthermore, alternative oxidation procedures such as rigorous ozonolysis reactions can be controlled and regulated more effectively in continuous flow microreactors.…”
Section: Opportunitiesmentioning
confidence: 99%