Abstract
In the petrochemical industry, the separation of propylene/propane is
usually paid much attention due to its high energy-consuming and
environmental challenges. In this work, an energy-efficient extractive
distillation (ED) separation process of propylene/propane is proposed by
introducing a tailor-made ionic liquid (IL) solvent. The structure
optimization of ILs is performed with a novel design objective in the
computer-aided ionic liquid design (CAILD) method. By solving a
formulated CAILD-based mixed-integer nonlinear programming (MINLP)
problem, the ethylimidazolium ethyl sulfate ([C2IM][EtSO4]) is identified as the best IL solvent. The separation performance of [C2IM][EtSO4]
in the ED process of propylene/propane is then evaluated through
rigorous process simulation in Aspen Plus. For comparison, the
conventional separation process of propane/propylene is also simulated
and optimized. Based on the optimized operations, in-depth energy and
economic assessment are conducted for an industrial-scale separation of
propane/propylene in a Chinese refining industry. Remarkably, the [C2IM][EtSO4]-based ED process has 68.9% energy savings and 74.7% cost reduction when compared to the conventional process.
Original language | English |
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Article number | 124930 |
Journal | Fuel |
Volume | 326 |
Number of pages | 11 |
ISSN | 0016-2361 |
DOIs | |
Publication status | Published - 2022 |
Keywords
- Propylene/propane separation
- Ionic liquid
- CAILD
- Process simulation
- Extractive distillation