<?xml version='1.0' encoding='utf-8'?>
<?xml-stylesheet type="text/xsl" href="/v2/static/oai2.xsl"?>
<OAI-PMH xmlns="http://www.openarchives.org/OAI/2.0/" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.openarchives.org/OAI/2.0/ http://www.openarchives.org/OAI/2.0/OAI-PMH.xsd">
  <responseDate>2026-10-11T17:58:33Z</responseDate>
  <request identifier="oai:figshare.com:article/34020470" metadataPrefix="oai_dc" verb="GetRecord">https://api.figshare.com/v2/oai</request>
  <GetRecord>
    <record>
      <header>
        <identifier>oai:figshare.com:article/34020470</identifier>
        <datestamp>2026-09-29T02:07:28Z</datestamp>
        <setSpec>category_4</setSpec>
        <setSpec>category_13</setSpec>
        <setSpec>category_21</setSpec>
        <setSpec>category_272</setSpec>
        <setSpec>category_873</setSpec>
        <setSpec>category_734</setSpec>
        <setSpec>category_133</setSpec>
        <setSpec>portal_63</setSpec>
        <setSpec>item_type_6</setSpec>
        <setSpec>month_year_09_2026</setSpec>
      </header>
      <metadata>
        <oai_dc:dc xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance"  xmlns:oai_dc="http://www.openarchives.org/OAI/2.0/oai_dc/" xmlns:dc="http://purl.org/dc/elements/1.1/" xsi:schemaLocation="http://www.openarchives.org/OAI/2.0/oai_dc/ http://www.openarchives.org/OAI/2.0/oai_dc.xsd">
          <dc:title>Entrainer Screening, Vapor–Liquid Equilibrium
Measurement, and Extractive Distillation Simulation for the Ethyl
Propionate–Ethanol Azeotropic System</dc:title>
          <dc:creator>Ying Qiao (555575)</dc:creator>
          <dc:creator>Xiuyu Zhang (760602)</dc:creator>
          <dc:creator>Yun Zou (165943)</dc:creator>
          <dc:creator>Ruining He (10647709)</dc:creator>
          <dc:creator>Zhangfa Tong (2134969)</dc:creator>
          <dc:subject>Biochemistry</dc:subject>
          <dc:subject>Genetics</dc:subject>
          <dc:subject>Biotechnology</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>Plant Biology</dc:subject>
          <dc:subject>screened via cosmo</dc:subject>
          <dc:subject>reliable thermodynamic consistency</dc:subject>
          <dc:subject>il mole fraction</dc:subject>
          <dc:subject>economic analysis shows</dc:subject>
          <dc:subject>dilution solvent capacity</dc:subject>
          <dc:subject>challenging industrial problem</dc:subject>
          <dc:subject>252 ionic liquids</dc:subject>
          <dc:subject>extractive distillation simulation</dc:subject>
          <dc:subject>based extractive distillation</dc:subject>
          <dc:subject>vacuum distillation</dc:subject>
          <dc:subject>rs theory</dc:subject>
          <dc:subject>relative volatility</dc:subject>
          <dc:subject>obtain high</dc:subject>
          <dc:subject>evaluating selectivity</dc:subject>
          <dc:subject>ethylene glycol</dc:subject>
          <dc:subject>ethyl propionate</dc:subject>
          <dc:subject>entrainer screening</dc:subject>
          <dc:subject>effectively improved</dc:subject>
          <dc:subject>completely eliminated</dc:subject>
          <dc:subject>8 %.</dc:subject>
          <dc:description>The separation of ethyl propionate
(EtPr) from the EtPr-ethanol
(EtOH) azeotropic system is a challenging industrial problem. Herein,
252 ionic liquids (ILs) were screened via COSMO-RS theory, and tributylmethylammonium
acetate ([N&lt;sub&gt;4441&lt;/sub&gt;][Ac]) was selected as the optimal extractive
distillation entrainer by evaluating selectivity and infinite-dilution
solvent capacity. Vapor–liquid equilibrium (VLE) data of the
EtPr (1) + EtOH (2) + [N&lt;sub&gt;4441&lt;/sub&gt;][Ac] (3) system were measured
at 101.3 kPa. The added [N&lt;sub&gt;4441&lt;/sub&gt;][Ac] effectively improved
the relative volatility of EtPr and completely eliminated the azeotrope
at an IL mole fraction of 8%. The NRTL model provided accurate data
correlation with reliable thermodynamic consistency. An optimized
extractive distillation process was established via Aspen Plus V11
to obtain high-purity EtPr and EtOH. Economic analysis shows that
the proposed process reduces total annual cost (TAC) by 18.75% and
38.83% compared with ethylene glycol-based extractive distillation
and vacuum distillation, respectively.</dc:description>
          <dc:date>2026-09-28T00:00:00Z</dc:date>
          <dc:type>Text</dc:type>
          <dc:type>Journal contribution</dc:type>
          <dc:identifier>10.1021/acs.iecr.6c01223.s001</dc:identifier>
          <dc:relation>https://figshare.com/articles/journal_contribution/Entrainer_Screening_Vapor_Liquid_Equilibrium_Measurement_and_Extractive_Distillation_Simulation_for_the_Ethyl_Propionate_Ethanol_Azeotropic_System/34020470</dc:relation>
          <dc:rights>CC BY-NC 4.0</dc:rights>
        </oai_dc:dc>
      </metadata>
    </record>
  </GetRecord>
</OAI-PMH>
