Urea dewaxing of low n-paraffin content oils
AssigneeDeutsche Texaco Aktiengesellschaft
InventorsMaximilian Kunert, Hans-Georg Wegner
Life of this patent
Estimating the term…
Abstract
Mineral oils containing small amounts (less than 2 weight percent) of normal paraffins may be urea dewaxed to produce refrigerator oils having Freon cloud or flock points of at least minus 55.degree.C. by utilizing large excesses of the amount of crystalline urea theoretically required for complete conversion of the n-paraffins into solid adduct and conducting the adduct formation under conditions of vigorous agitation.
Claims8
In a process for dewaxing liquid mineral oils comprising reacting said liquid mineral oils with urea in the presence of an organic solvent to form solid, n-paraffin-urea adducts, separating said adducts from the solution of the dewaxed mineral oil, decomposing or extracting the separated adducts, recovering and recycling the urea and, optionally, recovering the n-paraffins, the improvement which comprises:
- a. diluting a mineral oil containing less than 2 weight percent of a n-paraffins with an organic solvent, said solvent being one which does not form an adduct with urea, in which urea is substantially insoluble and which has a density substantially below that of the n-paraffin-urea adduct,
- b. combining the mineral oil solution with solid urea, the amount of urea being a multiple of the amount required for the completed conversion of the n-paraffins into n-paraffin-urea adduct,
- c. vigorously mixing the mixture of mineral oil solution and urea by pumping the mixture of mineral oil solution and urea through a closed loop whereby said mixture is continuously circulated for a period of time sufficient to form n-paraffin-urea adduct,
- d. separating from the mixture of step (c) a solids-free solution of dewaxed mineral oil, and
- e. recovering from said solids-free solution the organic solvent and a dewaxed mineral oil product having a reduced n-paraffin content,
- f. continuously removing a portion of said circulating mixture,
- g. removing the solids from said portion,
- h. returning said solids-free portion to said circulating mixture,
- i. recovering the urea from the separated solids of step (g) by decomposing the adduct in said solids, and
- j. returning the recovered urea to the circulating mixture.
Dependencies are inferred from the claim text.