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Decarbonised H2 recovery and CO2 capture using a cost-effective membrane plant: A step towards energy transition

The result's identifiers

  • Result code in IS VaVaI

    <a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F61989100%3A27650%2F25%3A10258879" target="_blank" >RIV/61989100:27650/25:10258879 - isvavai.cz</a>

  • Result on the web

    <a href="https://www.scopus.com/pages/publications/105020021474?origin=resultslist" target="_blank" >https://www.scopus.com/pages/publications/105020021474?origin=resultslist</a>

  • DOI - Digital Object Identifier

    <a href="http://dx.doi.org/10.1016/j.fuproc.2025.108353" target="_blank" >10.1016/j.fuproc.2025.108353</a>

Alternative languages

  • Result language

    angličtina

  • Original language name

    Decarbonised H2 recovery and CO2 capture using a cost-effective membrane plant: A step towards energy transition

  • Original language description

    Separation of H2 from CO2 is crucial in industry, since they are the products of water gas shift reaction. In addition, the demand for pure H2, as well as the potential reuse of CO2 as reactant, are increasing as a consequence of the transition from fossil fuels to decarbonization processes. In this scenario, this work aims to propose a possible solution to get simultaneously pure H2 and CO2, meeting the world&apos;s requirements in terms of reduction of CO2 emissions and transition to cleaner energy. A simulated plant combining Pd-based and SAPO-34 membrane modules is able to provide pure H2, with a final recovery higher than 97%. In addition, the entire CO2 fed to SAPO-34 unit is recovered in the permeate stream, with a concentration of 97.7%. A cost analysis shows that feed gas gives a higher contribution than compression, heat exchange and membranes (e.g., 70, 20, 3 and 7% respectively). Net profit and net present value are positive within a specific feed gas price range (e.g., net profit up to 0.10 and 0.155 $/Nm3, depending on the labour cost set), showing that the process can be cost-effective and profitable. H2 purification cost ranges between 2.6 and 7.8 $/kg.

  • 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

    20501 - Materials engineering

Result continuities

  • Project

  • Continuities

    O - Projekt operacniho programu

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

    Fuel Processing Technology

  • ISSN

    0378-3820

  • e-ISSN

    1873-7188

  • Volume of the periodical

    279

  • Issue of the periodical within the volume

    prosinec

  • Country of publishing house

    NL - THE KINGDOM OF THE NETHERLANDS

  • Number of pages

    12

  • Pages from-to

    108353

  • UT code for WoS article

    001608202800001

  • EID of the result in the Scopus database

    2-s2.0-105020021474