FIELD: technological processes.
SUBSTANCE: invention relates to method of thermal processes gasolines refining, involving their mixing with oil fractions - hydrogen donors at temperature of less than 100 °C with subsequent processing under catalytic cracking conditions at temperature of 420-480 °C in reactor-regenerator system, on catalyst for carrying out hydrogen transfer reactions. Hydrogen donors used are following oil fractions: straight-run wide gasoline fraction with start boiling point of 62 °C and with variable end boiling point to 180 °C, aromatic producing compound raffinate with start boiling point of 62 °C and with variable end boiling point to 180 °C, straight-run kerosene fraction with boiling temperature range of 140-240 °C, straight-run diesel fraction with boiling temperature range of 180-360 °C, at their ratio with thermal processes petrols of 1:(1-3). Thermal processes gasolines include thermal cracking processes, viscosity breaking, coking gasolines.
EFFECT: thermal processes gasolines catalytic refinement without using molecular hydrogen, wider raw material base for high-quality commercial gasolines producing, as well as higher yield of target gasoline fraction.
1 cl, 2 tbl, 9 ex
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Authors
Dates
2016-10-10—Published
2015-07-21—Filed