The utility model belongs to the technical field of
deep processing of
coal tar, and particularly relates to a decrystallized
anthracene oil production system which comprises a main decrystallized
anthracene oil tank, and a main feeding
pipe, a main discharging
pipe and a main discharging pump which are arranged on the main decrystallized
anthracene oil tank, the auxiliary feeding
pipe, the auxiliary discharging pipe and the auxiliary discharging pump are arranged on the auxiliary anthracene removal tank; and the
mixing tank is connected with outlets of the main feeding pipe and the auxiliary discharging pipe. Cooling, crystallizing and centrifugally separating anthracene oil extracted from the bottom of the
tar rectifying
tower to obtain decrystallized anthracene oil and crude anthracene; and removing anthracene,
phenanthrene,
carbazole and the like in the crude anthracene through subsequent refining to obtain heteroanthracene-removed oil. Generally, the
viscosity of
impurity-removed anthracene oil is large, the
viscosity of de-crystallized anthracene oil is small, the
impurity-removed anthracene oil and the de-crystallized anthracene oil are conveyed into a
mixing tank through a main discharging pipe and an auxiliary discharging pipe respectively and mixed in the
mixing tank, and the feeding amount of the
impurity-removed anthracene oil and the feeding amount of the de-crystallized anthracene oil are adjusted by adjusting the flow of a main discharging pump and the flow of an auxiliary discharging pump, so that the
viscosity of mixed liquid (mixed anthracene oil) in the mixing tank is adjusted; therefore, the viscosity requirements for different purposes can be met.