The invention provides a process for treating waste liquids from catalytic
cracking flue gas desulfurization. The process comprises the following steps: enabling a part of waste liquids from a
quenching washing
tower to enter a hydraulic
cyclone separator so as to be subjected to
solid-liquid separation, returning the thin liquids to the
quenching washing
tower so as to be recycled, enabling the thick liquids to enter a
neutralization reactor so as to be subjected to
neutralization reaction, enabling the neutralized waste liquids to enter a
slurry pond so as to be mixed with a flocculating agent uniformly, and enabling the mixture to enter an expansion-drum type filter so as to be subjected to
solid-liquid separation with a thick
slurry and a supernatant being obtained; returning part of the supernatant to the
quenching washing
tower so as to be recycled, discharging the remaining supernatant into an oxidation tank, removing the pseudo-COD containing
sulfite roots and
bisulfite roots by oxidizing, and directly discharging the qualified
sewage; enabling the thick
slurry to enter a
settling pond from the bottom of the expansion-drum type filter so as to be further settled, feeding the thick slurry subjected to settlement into a
dewatering machine so as to be concentrated and dewatered, directly transporting the filter cakes obtained by
dewatering the thick slurry, returning the filtrate from the
dewatering of the thick slurry to the slurry pond, and mixing the filtrate with the waste liquids so as to be retreated. The process provided by the invention has the advantages of a stable and efficient
treatment effect, strong
shock resistance, low investment and small floor area occupation and convenience of operation.