The invention belongs to the technical field of
organic chemistry, and particularly relates to a separation and
recovery method of a
mixed solution. In order to solve the problem of
high energy consumption of a rectification separation mode in the prior art, the invention provides a separation and
recovery method of a
mixed solution, which comprises the following steps: transferring the
mixed solution containing
tetrachloroethylene,
hexachloroethane,
hexachlorobutadiene and
hexachlorobenzene into a melt crystallizer, and carrying out programmed cooling by using the melt crystallizer until the temperature of the mixed solution is 25-100 DEG C, so as to obtain a mixed solution containing
tetrachloroethylene,
hexachloroethane,
hexachlorobutadiene and
hexachlorobenzene; solidifying the high-melting-point substance in the mixture onto a crystallizer to obtain a product
crystal; transferring the
liquid phase as residual liquid into a residual
liquid tank; raising the temperature to 185-190 DEG C to sublimate and condense
hexachloroethane to form hexachloroethane crystals; heating the remaining product crystals to 220-230 DEG C for melting, and discharging the remaining product crystals into a product tank to obtain a
hexachlorobenzene solution; and carrying out rectification separation on the residual liquid to obtain a
tower top light component
tetrachloroethylene product and a
tower bottom heavy component
hexachlorobutadiene product. The highest
operation temperature is 250 DEG C or below, and the
energy consumption is low.