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Catalysis of Organic..

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Tanielyan et al. 123Fig 1a shows the near first order relationship between the MeO-TEMPOconcentration and the reaction rate (curve 3) and at the same time it shows a gradualdeterioration <strong>of</strong> the reaction selectivity to the aldehyde 2 at higher MeO-TEMPOconcentrations in the region 0.5-1.0 mmol (3 - 6 mol %), (curve 2). The only productdetected along with the desired aldehyde 2 is the product <strong>of</strong> the over-oxidation,hexanoic acid.In Fig 1b, the [Br - ]/[MeO-TEMPO] ratio was varied over a relatively wide rangeat equimolar concentrations for MeO-TEMPO and Mg(NO 3 ) 2 <strong>of</strong> 0.48mmol (3mol%). Three distinct regions are clearly seen: i) a region <strong>of</strong> low Br concentrationwhere increasing the NBS concentration leads to dramatic rate increase and wherethe conversion <strong>of</strong> 1, measured at 60 min reaction time reached 100% at selectivity to2 <strong>of</strong> 97-98%, ii) a region, where increasing the concentration <strong>of</strong> the NBS did notproduce a significant change in the reaction effectiveness and iii) a region, wherefurther increase in the [Br]/[MeO-TEMPO] ratio led to a rate reduction (curve 3).O RCHO2NO 2 BrO -+NH +E D C B O AHO -1/2O 2NORCH 2OHBr - NScheme 2.In the next set <strong>of</strong> experiments, the MeO-TEMPO concentration was fixed at 0.48mmol (3 mol%) and the NBS concentration at 0.048 mmol (0.3 mol%) while theMg(NO 3 ) 2 / [MeO-TEMPO] ratio was gradually increased in the range shown inFigure 1c. The first region <strong>of</strong> relatively low concentration <strong>of</strong> [Mg(NO 3 ) 2 ] ischaracterized by a first order relationship between the rate <strong>of</strong> oxidation and thenitrate concentration and in the same region, at Mg(NO 3 ) 2 / [MeO-TEMPO] ≅ 1, acomplete conversion <strong>of</strong> 1 was observed with high aldehyde selectivity. Furtherincrease in the nitrate concentration, however, leads to severe inhibition, resulting ingradual deactivation <strong>of</strong> the catalyst system and rapid decline in the reaction rates(curve 2 and 3).At the current initial concentrations <strong>of</strong> 1 in the acetic acid solvent, (1.33M, 16.6v/v %), the optimum ratio between the three components <strong>of</strong> the catalyst systemseams to be MeO-TEMPO:Mg(NO 3 ) 2 :NBS = 1:1:0.1. As we will show in the nextsection, the higher the initial concentration <strong>of</strong> the alcohol substrate, the more NBS isneeded for achieving high reaction rates in the selective oxidation <strong>of</strong> 1 to 2.A plausible reaction sequence including a multi step cascade <strong>of</strong> four redoxcycles is shown in Scheme 2. Since we have no experimental data to support eitherthe nature <strong>of</strong> the intermediate species involved or their oxidation state, nor have weOH

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