A method for recovering waste high-boiling-point heat-transfer oil comprises the steps: 1, pre-
processing waste heat-transfer oil; 2, performing hydrogenation refining on the
waste heat-transfer oil pre-processed in the step 1; and 3, performing
fractional distillation on the
waste heat-transfer oil subjected to hydrogenation refining in the step 2. Concretely,
fractional distillation in the step 3 is performed according to the following steps: 1), enabling liquid-phase oil separated out from hydrogenation low-pressure separation composition to enter a reduced-pressure flash-
evaporation tower, cooling a
gas phase getting out from the top of the reduced-pressure flash-
evaporation tower by a condenser, and enabling the cooled
gas phase to enter a
reflux tank at the
tower top, pumping and exhausting the
gas phase into
atmosphere, pumping out a
liquid phase via a
reflux pump and taking the
liquid phase as
naphtha and sending to a
storage tank; and 2) pressurizing falling-film
distillation tower bottom distillates and conveying to a reduced-pressure
distillation tower by a conveying pump, cooling a gas phase getting out from the top of the reduced-pressure
distillation tower by a condenser and enabling the cooled gas phase to enter a
reflux tank at the tower top for oil-
gas separation, enabling the
liquid phase to be as reduced-pressure tower-top oil and enter a condenser for cooling, one
branch of the reduced-pressure tower-top oil is used for column-plate refluxing, one
branch of the reduced-pressure tower-top oil is used as 7#
white oil and conveyed to an irrigated-area
storage tank for self use and export sale, and one
branch of the reduced-pressure tower-top oil is used 15#
white oil and conveyed to an irrigated-area
storage tank for self use and export sale. The method has the characteristics of low
energy consumption, cleaning,
environmental protection, high economic benefit economic benefit and high yield.