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Comparison of the mass transfer efficiency of random and structured packings under distillation of positive, neutral, and negative system in the i.d. 0.3 m column

The result's identifiers

  • Result code in IS VaVaI

    <a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F60461373%3A22340%2F25%3A43933545" target="_blank" >RIV/60461373:22340/25:43933545 - isvavai.cz</a>

  • Result on the web

    <a href="https://www.sciencedirect.com/science/article/pii/S0017931026001523?pes=vor&utm_source=scopus&getft_integrator=scopus" target="_blank" >https://www.sciencedirect.com/science/article/pii/S0017931026001523?pes=vor&utm_source=scopus&getft_integrator=scopus</a>

  • DOI - Digital Object Identifier

    <a href="http://dx.doi.org/10.1016/j.ijheatmasstransfer.2026.128476" target="_blank" >10.1016/j.ijheatmasstransfer.2026.128476</a>

Alternative languages

  • Result language

    angličtina

  • Original language name

    Comparison of the mass transfer efficiency of random and structured packings under distillation of positive, neutral, and negative system in the i.d. 0.3 m column

  • Original language description

    Distillation experiments were carried out under total reflux in a 0.3 m i.d. column equipped with a structured packing (Sulzer MellapakPlus™ 252.Y) and a lattice-type random packing (Sulzer NeXRing™ 0.7). Binary C&lt;inf&gt;6&lt;/inf&gt;–C&lt;inf&gt;7&lt;/inf&gt; hydrocarbon mixtures were investigated, including cyclohexane/n-heptane (negative system) and n-hexane/cyclohexane (positive system). Given the close similarity of the gas-phase properties of the systems, comparable separation efficiencies would be expected. Nevertheless, the height equivalent to a theoretical plate differed by approximately 15–20% under identical F &lt;inf&gt;G&lt;/inf&gt; factors, with the highest HETP observed for the negative system and the lowest for the positive system. The same trend was found for both structured and random packings, indicating that the effect is not restricted to a specific packing type. Compared with earlier studies employing wetted-wall columns and first-generation random packings, the magnitude of the effect is reduced for modern industrial packings. Existing models fail to provide a satisfactory quantitative description of the observed behavior. © © 2026. Published by Elsevier Ltd.

  • Czech name

  • Czech description

Classification

  • Type

    J<sub>imp</sub> - Article in a specialist periodical, which is included in the Web of Science database

  • CEP classification

  • OECD FORD branch

    20300 - Mechanical engineering

Result continuities

  • Project

  • Continuities

    I - Institucionalni podpora na dlouhodoby koncepcni rozvoj vyzkumne organizace

Others

  • Publication year

    2025

  • Confidentiality

    S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů

Data specific for result type

  • Name of the periodical

    INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER

  • ISSN

    0017-9310

  • e-ISSN

    1879-2189

  • Volume of the periodical

    260

  • Issue of the periodical within the volume

    June

  • Country of publishing house

    GB - UNITED KINGDOM

  • Number of pages

    9

  • Pages from-to

    1-9

  • UT code for WoS article

    001685522300001

  • EID of the result in the Scopus database

    2-s2.0-105029245011