Anthracene and carbazole are both
highly value-added products in
the anthracene fraction of coal tar, and it is a difficult task to
separate and purify anthracene and carbazole from the anthracene fraction/crude
anthracene, which consists of many components, differing only slightly
in boiling points. To seek a highly efficient solvent to separate
carbazole from crude anthracene, the solubilities of anthracene and
carbazole in tetrachloroethylene (PCE) and the mixtures of xylene
+ PCE, N,N-dimethylformamide (DMF)
+ urea, and DMF + H2O were measured. The separation efficiencies
of DMF + 30% H2O, DMF + urea, and DMF + isopropanolamine
mixtures with different percentages of urea or isopropanolamine were
examined by the cooling crystallization process. Chlorobenzene, PCE,
and xylene + 40% PCE mixture were used in the carbazole refining process.
The results showed that, with the addition of the third component
of urea, isopropanolamine, or water to DMF, the solubility of anthracene
and carbazole is inhibited to some extent and the selectivity is increased.
The separation efficiency is improved using the mixed solvents, DMF
+ urea and DMF + isopropanolamine, when the percentage of urea or
isopropanolamine in DMF is below 15 or 40%, respectively. The content
of carbazole in crude carbazole is higher than 58.14 or 64.80 wt %
using DMF + urea or DMF + isopropanolamine, respectively. The yield
is greater than 84.43 wt %, and the impurity of anthracene is less
than 10.28 wt %. In addition, the content of anthracene in refined
anthracene is higher than 92.31 wt % with the yield above 80.23 wt
%. During the carbazole refining process when using chlorobenzene
as the solvent, the purity of carbazole can reach 98.97 wt % and the
total yield was 67.89 wt %.