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.