Coal tar residue
(CTR) is recognized as a hazardous industrial
waste with a high carbon content and coal tar consisting mainly of
toxic polycyclic aromatic hydrocarbons (PAHs). The coal tar in CTR
can be deeply processed into high-value-added fuels and chemicals.
Effective separation of coal tar and residue in CTR is a high-value-added
utilization method for it. In this paper, ethyl acetate, ethanol,
and
n
-hexane were chosen as extractants to study
the extraction process of coal tar from CTR, considering the mass
transfer in the liquid phase outside the CTR particles and the diffusion
inside the CTR particles, and a mathematical model of the solid–liquid
extraction process of CTR was established based on Fick’s second
law. First, the mass-transfer coefficients (
k
f
) and effective diffusion coefficients (
D
e
) of ethyl acetate, ethanol, and
n
-hexane
in solid–liquid extraction at 35 °C were determined to
be 1.54 × 10
–5
and 4.99 × 10
–10
m
2
·s
–1
, 1.14 × 10
–5
and 3.57 × 10
–10
m
2
·s
–1
, and 1.01 × 10
–5
and 3.48
× 10
–10
m
2
·s
–1
, respectively. Furthermore, the simulated values obtained by the
model also maintained a high degree of agreement with the experimental
results, which indicates the high accuracy prediction of the model.
Finally, the model was used to investigate the effects of the solvent–solid
ratio, temperature, and stirring speed on the extraction rates with
the three extractants. According to the analysis with gas chromatography–mass
spectrometry (GC-MS), among the three solvents,
n
-hexane extracted the highest content of aliphatic hydrocarbons (ALHs),
ethyl acetate extracted the highest content of oxygenated compounds
(OCs), and ethanol extracted the highest content of aromatic hydrocarbons
(ARHs). The model and experimental data can be used to provide accurate
predictions for industrial utilization of CTR.