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Catalysis of Organic..

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126TEMPO Oxidation <strong>of</strong> Alcoholsconcentration <strong>of</strong> the dissolved oxygen in the liquid phase), becomes more importantat higher temperatures. At 43°C, the reaction is fast enough, the starting alcohol iscompletely converted to 2 over the 60 min reaction time and the aldehydesselectivity remains high in the 92-94% range (3c).O2 Uptake rate, mmol/min0.80.70.60.50.40.30.20.143C40C37C34C0.00 5 10 15 20 25 30 35Pressure, psia b c43C40C37C34C0 5 10 15 20 25 30 35Pressure, psi34C37C40C43C0 5 10 15 20 25 30 35Pressure, psi1009896949290Conversion(Selectivity) at 30min, %Fig 3. Effect <strong>of</strong> the oxygen pressure and the temperature on the rate <strong>of</strong> oxidation (a),on the conversion <strong>of</strong> Hexanol-1 (b) and on the selectivity to Hexanal (c) at 34°C (◊),37°C (+), 40°C (□) and 43 °C (○). Conditions: [Hexanol-1] = 2mL (16mmol),CH 3 COOH =10mL, [AA TEMPO] = 0.64mmol, [NBS]=0.048 mmol and Mg(NO 3 ) 2= 1.2 mmol.Reduction <strong>of</strong> the Volume <strong>of</strong> HOAc at High Substrate to Catalyst (S/C) RatiosThe next attempt to further improve the reaction efficiency was to reduce the volume<strong>of</strong> the acetic acid solvent and to proportionally increase the initial concentration <strong>of</strong>the alcohol substrate while keeping the total reaction volume at constant level. Themain purpose <strong>of</strong> these studies was to determine the minimum amount acetic acidneeded to maintain a homogeneous system until complete conversion <strong>of</strong> hexan-1-olto 2. Since the oxidation reaction produces stoichiometric amounts water, it was felt,that the formation <strong>of</strong> a second aqueous phase along with the hydrophobic aldehydephase would lead to the creation <strong>of</strong> a two-phase reaction system with the inevitablepartition <strong>of</strong> the catalyst system between the two phases. In addition it was alsoimportant to determine the highest possible S/C ratio while maintaining a reasonablereaction rate.The starting point here was the 16 mmol scale oxidation reaction using thestandard conditions shown in Figure 4a (curve 1). Full conversion was achieved over22 min at a TOF <strong>of</strong> 68h -1 . In the next experiment (curve 2), the hexan-1-olconcentration was doubled (32mmol scale, 2.7M, 33.3% v/v) while the concentration<strong>of</strong> the AA-TEMPO-MNT-NBS composition was kept at the same level. Again,

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