Conclusions
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1.
A one-channel, two-stage process has been developed for the hydrogenative purification of distillate fractions from liquid pyrolysis products, using a palladium catalyst in the first stage, an aluminum-cobalt-molybdenum catalyst in the second stage, and a hydrogen pressure of 40 atm.
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2.
The use of a low-temperature palladium catalyst in the first stage permits a simplified technology and an improved product quality; the products can be used to the production of C6-C8 aromatic hydrocarbons.
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3.
It has been shown that it is possible to separate benzene, toluene, and total xylenes in amounts comprising 98.0, 97.0, and 92.0% of the theoretical, respectively, from a hydrofined pyrocondensate (containing 65.7% of aromatic hydrocarbons), by means of extraction with diethylene glycol and subsequent distillation.
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Translated from Khimiya i Tekhnologiya Toplivi Masel, No. 4, pp. 6–9, April, 1969.
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Barents, A.D., Vo1' -Épshtein, A.B., Krichko, A.A. et al. Production of aromatic hydrocarbons by the hydrogenative purification of liquid pyrolysis products. Chem Technol Fuels Oils 5, 243–247 (1969). https://doi.org/10.1007/BF00730177
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DOI: https://doi.org/10.1007/BF00730177