Labofina, S.a.

Guy F Debande

Jacques F Grootjans

Raymond N Cahen

Process for removing the nitrogen impurities from a liquid hydrocarbon mixture comprising introducing into a low volume mixer the hydrocarbons to be treated together with a dilute aqueous acid solution to form an emulsion, withdrawing said emulsion into a decantation zone where it breaks and recycling to the low volume mixer from 80 to 95% by volume of the aqueous acid solution coming from the decantation zone, so as to maintain in said low volume mixer a volume ratio of the hydrocarbons to the aqueous acid solution from about 0.3 to about 13, preferably from about 0.5 to about 4, and the pH of the aqueous acid solution from about 0.1 to about 1.5.

Process for removing the nitrogen impurities from a hydrocarbon mixture

A process for hydrogenating polymers which are derived from olefin units containing 4 carbon atoms is disclosed whereby white oils which exhibit a low iodine value (e.g., below 0.26) are obtained under relatively mild reaction conditions. The hydrogenation is effected in the presence of a catalyst comprising platinum on an alumina support exhibiting a total pore volume of at least 0.25 ml/g of which about 90 to 98% are provided by pores the mean size of which is below 100A.

Hydrogenation process of olefin polymers for producing white oils

A process for hydrogenating polymers which are derived from olefin units containing 4 carbon atoms is disclosed whereby white oils which exhibit a low iodine value (e.g., below 0.26) are obtained under relatively mild reaction conditions. The hydrogenation is effected in the presence of a catalyst comprising palladium on a bimodal alumina support ehibiting a total pore volume of at least 0.25 ml/g of which 35 to 50% are provided by small pores the mean size of which is below 300A and 25 to 35% are provided by large pores the mean size of which is above 300A and is at least 1.5 times the mean size of the small pores.

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Watermael, Belgium

Guy F Debande