The refined utilization of various
parts of hybrid residual C4
has received increasing attention, but the mixed C4 is difficult to
separate due to complex components and close boiling points. This
paper proposes an innovative separation method using complex extractive
distillation by adding cuprous chloride ethanolamine (C2H7NO–CuCl) into the conventional extractant, as
a complexing agent. The vapor–liquid equilibrium (VLE) data
were measured for six different systems, namely, the mixed C4–dimethylformamide
(DMF) system and the mixed C4–DMF–C2H7NO–CuCl system, the mixed C4–acetonitrile (ACN)
system and the mixed C4–ACN–C2H7NO–CuCl system, and the mixed C4–methyl–ethyl
ketone (MEK) system and the mixed C4–MEK–C2H7NO–CuCl system. Results showed that the relative
volatility of butane–butene solution was significantly increased
with the addition of the complexing agent systems. After careful consideration
of various influencing factors, the mixed C4–MEK–C2H7NO–CuCl system was selected as the best
extraction separation system, and technological experiments were carried
out to further explore its feasibility and advanced nature. Results
showed that when the solvent-to-feed ratio (S/F) was 12.5, the reflux
ratio of extractive distillation column (R
1) was 1.5, and the reflux ratio of solvent recovery column (R
2) was 2.5, the purity of butene was more than
97.0%, and the separation yield was more than 95.0%. Furthermore,
the solvent-to-feed ratio of complex extractive distillation was only
70% of ordinary extractive distillation, the reflux ratio was only
60% of ordinary extractive distillation, and the stripping temperature
of the complex extractive distillation column was only about 423.15
K, which was lower than that of the ordinary extractive distillation
column.