Dehydrolinalool → Linalool

참여 물질

반응 단계

In a 300 ml pressure reactor, 10 g of the Ru catalyst as described in the catalyst production example were placed in a catalyst basket insert and 150 g (0.99 mol) of dehydrolinalool were added. The hydrogenation was carried out using pure hydrogen at a constant pressure of 40 bar and a temperature of 80° C. After a reaction time of 4 hours, the reactor was vented. The conversion of dehydrolinalool was 95% and linalool was obtained in a selectivity of 90%.

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