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        <datestamp>2026-09-30T01:05:52Z</datestamp>
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          <dc:title>Selective Adsorption
of Methyl Acetate from Model
Fischer–Tropsch Synthetic Oil on 13X Zeolite: Experimental
and Computational Insights</dc:title>
          <dc:creator>Fangyu Zhao (163571)</dc:creator>
          <dc:creator>Qiangqiang Xue (8762787)</dc:creator>
          <dc:creator>Ruihan Yang (3832696)</dc:creator>
          <dc:creator>Wei Wan (793804)</dc:creator>
          <dc:creator>Yuhan Gao (2563966)</dc:creator>
          <dc:creator>Yujun Wang (1947196)</dc:creator>
          <dc:creator>Guangsheng Luo (1652341)</dc:creator>
          <dc:subject>Biophysics</dc:subject>
          <dc:subject>Biochemistry</dc:subject>
          <dc:subject>Environmental Sciences not elsewhere classified</dc:subject>
          <dc:subject>Chemical Sciences not elsewhere classified</dc:subject>
          <dc:subject>Biological Sciences not elsewhere classified</dc:subject>
          <dc:subject>reliable predictive model</dc:subject>
          <dc:subject>ion – dipole</dc:subject>
          <dc:subject>fischer – tropsch</dc:subject>
          <dc:subject>density functional theory</dc:subject>
          <dc:subject>creating strong positive</dc:subject>
          <dc:subject>acidity characterizations indicated</dc:subject>
          <dc:subject>equilibrium adsorption capacity</dc:subject>
          <dc:subject>elucidating adsorption mechanisms</dc:subject>
          <dc:subject>representative ester oxygenate</dc:subject>
          <dc:subject>selective adsorption mechanisms</dc:subject>
          <dc:subject>order kinetic models</dc:subject>
          <dc:subject>selective adsorption behavior</dc:subject>
          <dc:subject>removing methyl acetate</dc:subject>
          <dc:subject>superior adsorption performance</dc:subject>
          <dc:subject>13x zeolite originates</dc:subject>
          <dc:subject>experimental adsorption behavior</dc:subject>
          <dc:subject>selective adsorption</dc:subject>
          <dc:subject>adsorption behavior</dc:subject>
          <dc:subject>methyl acetate</dc:subject>
          <dc:subject>adsorption stability</dc:subject>
          <dc:subject>adsorption sites</dc:subject>
          <dc:subject>13x zeolite</dc:subject>
          <dc:subject>ester oxygenates</dc:subject>
          <dc:subject>ester groups</dc:subject>
          <dc:subject>adsorption kinetics</dc:subject>
          <dc:subject>work establishes</dc:subject>
          <dc:subject>theoretical approach</dc:subject>
          <dc:subject>simulations reproduced</dc:subject>
          <dc:subject>preferentially adsorb</dc:subject>
          <dc:subject>polar carbonyl</dc:subject>
          <dc:subject>monte carlo</dc:subject>
          <dc:subject>molecular surface</dc:subject>
          <dc:subject>limited understanding</dc:subject>
          <dc:subject>hydrogen bonding</dc:subject>
          <dc:subject>general strategy</dc:subject>
          <dc:subject>efficient removal</dc:subject>
          <dc:subject>computational insights</dc:subject>
          <dc:subject>combined experimental</dc:subject>
          <dc:subject>calculations suggested</dc:subject>
          <dc:subject>activated carbon</dc:subject>
          <dc:description>The efficient removal of ester oxygenates from Fischer–Tropsch
(FT) synthetic oil remains challenging due to limited understanding
of selective adsorption mechanisms and adsorption kinetics. Herein,
a combined experimental and theoretical approach was employed to investigate
the selective adsorption behavior, kinetics, and mechanism of removing
methyl acetate, a representative ester oxygenate, from a methyl acetate/1-decene/decane
model FT synthetic oil using 13X zeolite, γ-alumina, and activated
carbon. Dynamic breakthrough experiments revealed that 13X zeolite
exhibited substantially higher adsorption selectivity and removal
efficiency toward methyl acetate than γ-alumina and activated
carbon. The adsorption behavior on 13X zeolite was well described
by both pseudo-first-order and pseudo-second-order kinetic models.
Moreover, 13X zeolite demonstrated excellent regeneration capability
and adsorption stability, maintaining its performance over six consecutive
adsorption–desorption cycles. Structural and acidity characterizations
indicated that the superior adsorption performance of 13X zeolite
originates from its well-developed hierarchical pore structure and
abundant Lewis acid sites. Density functional theory (DFT) calculations
suggested that the polar carbonyl and ester groups in methyl acetate
induce pronounced charge separation on the molecular surface, creating
strong positive and negative electrostatic potential regions. These
features enable methyl acetate to preferentially adsorb on 13X zeolite
through electrostatic (ion–dipole) attraction, hydrogen bonding,
and van der Waals forces, effectively displacing weakly polar hydrocarbon
molecules from adsorption sites. Monte Carlo (MC) simulations reproduced
the experimental adsorption behavior and provided a reliable predictive
model for equilibrium adsorption capacity. This work establishes an
integrated experimental–computational paradigm for elucidating
adsorption mechanisms and predicting oxygenate removal performance,
providing a general strategy for the purification of Fischer–Tropsch
synthetic oil.</dc:description>
          <dc:date>2026-09-29T00:00:00Z</dc:date>
          <dc:type>Text</dc:type>
          <dc:type>Journal contribution</dc:type>
          <dc:identifier>10.1021/acs.iecr.6c03238.s001</dc:identifier>
          <dc:relation>https://figshare.com/articles/journal_contribution/Selective_Adsorption_of_Methyl_Acetate_from_Model_Fischer_Tropsch_Synthetic_Oil_on_13X_Zeolite_Experimental_and_Computational_Insights/34028430</dc:relation>
          <dc:rights>CC BY-NC 4.0</dc:rights>
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