Process for the preparation of a mixture of cyclohexanone and cyclohexanol
AssigneeBayer Aktiengesellschaft
InventorsJurgen Scharschmidt, Christine Mendoza-Frohn, Hans-Josef Buysch, Rainer Klotzbucher
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AssigneeBayer Aktiengesellschaft
InventorsJurgen Scharschmidt, Christine Mendoza-Frohn, Hans-Josef Buysch, Rainer Klotzbucher
Estimating the term…
In the hydrogenation of phenol with H.sub.2 over Pd supported catalysts, the ratio of the products formed, cyclohexanone and cyclohexanol, can be predetermined by specific treatment of the catalysts during the initial activation and regeneration by O.sub.2 pretreatment and H.sub.2 treatment, the following time/temperature conditions being used: a) Cyclohexanone:cyclohexanol=85:15 to 98:2 a1) for initial activation, no O.sub.2 pretreatment and H.sub.2 treatment for 50-10 hours at 300.degree.-500.degree. C.; a2) for regeneration, O.sub.2 pretreatment for 30-0.5 hours at 220.degree.-380.degree. C. and H.sub.2 treatment for 2-6 hours at 150.degree.-250.degree. C.; b) Cyclohexanone:cyclohexanol=30:70 to below 85:15 b1) for initial activation, O.sub.2 pretreatment for 40-3 hours at 250.degree.-500.degree. C. and H.sub.2 treatment for 2-6 hours at 150.degree.-250.degree. C.; b2) for regeneration, O.sub.2 pretreatment for 30-0.5 hours at 380.degree.-600.degree. C. and H.sub.2 treatment for 2-6 hours at 150.degree.-250.degree. C.
A process for the preparation of mixtures of cyclohexanone and cyclohexanol in predetermined ratios to one another in the range from 30:70 to 98:2 by hydrogenation of phenol with hydrogen in the gas phase at 150 to 250.degree. C. under 0.8 to 8 bar over a supported palladium catalyst, wherein, for initial activation and for regeneration after use, the catalyst is subjected to an oxygen pretreatment, if appropriate, and then a hydrogen treatment in each case under 0.8 to 8 bar, the following time/temperature conditions being applied to establish the predetermined ratio:
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