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Polyamide Thin-Film Composite Membranes for Potential Raw Biogas Purification: Experiments and Modelling.

The result's identifiers

  • Result code in IS VaVaI

    <a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F67985858%3A_____%2F16%3A00459437" target="_blank" >RIV/67985858:_____/16:00459437 - isvavai.cz</a>

  • Result on the web

    <a href="http://dx.doi.org/10.1016/j.seppur.2016.05.008" target="_blank" >http://dx.doi.org/10.1016/j.seppur.2016.05.008</a>

  • DOI - Digital Object Identifier

    <a href="http://dx.doi.org/10.1016/j.seppur.2016.05.008" target="_blank" >10.1016/j.seppur.2016.05.008</a>

Alternative languages

  • Result language

    angličtina

  • Original language name

    Polyamide Thin-Film Composite Membranes for Potential Raw Biogas Purification: Experiments and Modelling.

  • Original language description

    This work reports on raw biogas purification method via swollen polyamide thin-film composite membranes. Experiments on permeation of gas mixture through two commercial thin-film polyamidencomposite (TFC) membranes were performed using an in-house permeation apparatus. The active polyamide top layer of TFC membranes was swollen by water present in a feed stream of raw biogas, whose relative humidity was higher than 85%. An effective CO2/CH4 separation was based on the significantly higher solubility of carbon dioxide in water compared to that of methane. The transport properties of both composite membranes are discussed together with the structure of membrane top active layer. One-dimensional mathematical model for flow and mass transport in the membrane cell was developed. The model enables the evaluation of the mass transport coefficients by the iterative fitting of experimental data in the co-current and counter-current flow arrangements. The model also determines concentration profiles of gas component on both sides of the membrane, which are otherwise immeasurable experimentally. The model can be used to evaluate the effect of changing the membrane area on the performance of the membrane module. Model results are discussed with respect to the required CH4 enrichment.

  • Czech name

  • Czech description

Classification

  • Type

    J<sub>x</sub> - Unclassified - Peer-reviewed scientific article (Jimp, Jsc and Jost)

  • CEP classification

    CI - Industrial chemistry and chemical engineering

  • OECD FORD branch

Result continuities

  • Project

    Result was created during the realization of more than one project. More information in the Projects tab.

  • Continuities

    I - Institucionalni podpora na dlouhodoby koncepcni rozvoj vyzkumne organizace

Others

  • Publication year

    2016

  • Confidentiality

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

Data specific for result type

  • Name of the periodical

    Separation and Purification Technology

  • ISSN

    1383-5866

  • e-ISSN

  • Volume of the periodical

    167

  • Issue of the periodical within the volume

    JUL 14

  • Country of publishing house

    NL - THE KINGDOM OF THE NETHERLANDS

  • Number of pages

    11

  • Pages from-to

    163-173

  • UT code for WoS article

    000377738800020

  • EID of the result in the Scopus database

    2-s2.0-84967189190