Aromatics Process Flowsheets & Simulations
Explore 7 validated, solved Aromatics simulation flowsheets in MaximaLabs — real components: benzene, toluene, o_xylene, methylcyclohexane, phenol, sulfolane. Open any one directly in your browser.
Solved via: PENG-ROBINSON, NRTL.
Aromatics column (Strigle)
A simple aromatics splitter recovering benzene overhead from a toluene/xylene-heavy feed, as described by R. Strigle (Gulf Publishing, 1987) — a classic packed-column textbook design case.
4 unit ops • PENG-ROBINSON
21 0
View & openMCHT extractive distillation with phenol
Extractive distillation of methylcyclohexane (MCH) and toluene using phenol as the selective solvent, adapted from Tiverios and Van Brunt (Ind. Eng. Chem. Res. 2000, 39, 1614). Phenol raises toluene's relative volatility away from MCH enough to split an otherwise close-boiling pair; a solvent-recovery column then splits toluene from the phenol (reported as its own product rather than recycled).
7 unit ops • PENG-ROBINSON
21 0
View & openSulfolane extractive distillation of aromatics
Extractive distillation recovering benzene and toluene from a stabilized reformate's C6-C7 non-aromatics (represented by methylcyclohexane) using sulfolane, after Figure 10.2/10.6 of T. Brouwer (PhD thesis, TU Twente, 2021). A vacuum solvent-recovery column then splits the aromatics from the sulfolane (reported as its own product rather than recycled). Note: the extractive column (ED) does not fully converge within the solver's iteration cap for this 4-component polar/nonpolar system and returns a partial profile — shown for the process topology rather than as a converged reference case.
7 unit ops • PENG-ROBINSON
21 0
View & openSulfolane liquid-liquid extraction of aromatics
Liquid-liquid extraction of aromatics from a refinery catalytic-reformer stream with sulfolane, after Figure 10.1 of T. Brouwer (PhD thesis, TU Twente, 2021). A countercurrent extraction cascade pulls benzene and toluene preferentially into the sulfolane-rich extract, leaving a methylcyclohexane-rich raffinate.
5 unit ops • NRTL
21 0
View & openBTX aromatics train
Benzene / toluene / p-xylene split in a two-column train — 99+% purity on all three products. From the ChemSep casebook (CScasebook_BTX).
6 unit ops • PENG-ROBINSON
22 0
View & openReformate splitter
A single column cutting catalytic reformate into a light benzene/hexane overhead and a toluene/xylene bottoms — the IECR 50, 5680 configuration from the ChemSep casebook.
4 unit ops • PENG-ROBINSON
22 0
View & openReformate splitter via dividing-wall column
A refinery catalytic-reformer stream (benzene/toluene/o-xylene plus a non-aromatic n-heptane proxy) is split into three purified aromatics cuts by a single thermally-coupled dividing-wall column instead of two ordinary columns in series — the same DWC economics as the BTX example, applied to a genuine reformate splitter duty. Dejanovic, Matijasevic, Jansen, Olujic, "Designing a Packed Dividing Wall Column for an Aromatics Processing Plant," Ind. Eng. Chem. Res. 2011, 50, 5680.
5 unit ops • PENG-ROBINSON
21 0
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