Abstract A process for the production of o-phenylphenol in the presence of a catalyst composed of a gamma -alumina or silica-alumina support having a BET surface area of 150 - 300 m2/g, a pore capacity of 0.50 - 0.85 ml/g and an iron content of at most 0.1 % by weight in terms of Fe2O3 and an alumina content of at least 90 %, the support carrying thereon platinum in an amount of 0.1 - 5.0 % by weight based on the support, iridium in an amount of 0.1 - 0.4 times that of the platinum and an alkali metal oxide in an amount of 0.5 - 8.0 % by weight of the support. o-Phenylphenol is prepared at a high selectivity over a long period of time by supplying onto the catalyst maintained at 300 DEG - 420 DEG C o-cyclohexylphenol or a dehydrodimerized condensate obtained by aldol condensation of cyclohexanone together with gaseous hydrogen in an amount per hour in terms of liquid volume of 0.1 - 1.5 times the volume of the catalyst, and elevating the reaction temperature stepwise or continuously with the lapse of the reaction time, while slowing down, if necessary, the rate of supplying the starting materials, to effect a dehydrogenation reaction.
A process for the production of o-phenylphenol, characterized by contacting in the presence of hydrogen carrier gas o-cyclohexylphenol or a dehydrodimerized condensate obtained by aldol condensation of cyclohexanone with a catalyst material at 300°-420° C in an amount per hour in terms of liquid volume of 0.1-1.5 times the volume of the catalyst, said catalyst being composed of γ-alumina or silica-alumina support having a BET surface area of 150-300 m 2 /g, a pore capacity of 0.50-0.85 ml/g, an iron content of at most 0.1% by weight in terms of Fe 2 O 3 and an alumina content of at least 90%, said support having carried thereon platinum in an amount of 0.1-5.0% by weight based on said support, iridium in an amount of 0.1-0.4 times the amount of platinum, and an alkali metal oxide in an amount of 0.5-8.0% by weight based on said support.
Claim 2
Dependent Claim
146 words
A process for the production of o-phenylphenol, characterized by contacting in the presence of hydrogen carrier gas o-cyclohexylphenol or a dehydrodimerized condensate obtained by aldol condensation of cyclohexanone with a catalyst material at 300°-420° C in an amount per hour in terms of liquid volume of 0.1-1.5 times the volume of the catalyst, said catalyst being composed of γ-alumina or silica-alumina support having a BET surface area of 150-300 m 2 /g, a pore capacity of 0.50-0.85 ml/g, an iron content of at most 0.1% by weight in terms of Fe 2 O 3 and an alumina content of at least 90%, said support having carried thereon platinum in an amount of 0.1-5.0% by weight based on said support, iridium in an amount of 0.1-0.4 times the amount of platinum, and an alkali metal oxide in an amount of 0.5-8.0% by weight based on said support.
Claim 3
Dependent Claim
25 words
A process according to claim 1 wherein the reaction temperature is elevated within a range of 300°-420° C with the lapse of the reaction time.
Claim 4
Dependent Claim
23 words
A process according to claim 1 wherein, the rate of supplying the starting material is reduced with the lapse of the reaction time.
Claim 5
Dependent Claim
18 words
A process according to claim 1 wherein said alkali metal oxide is an oxide of sodium or potassium.