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Polyamide Thin-Film Composite Membranes for Potential Raw Biogas Purification: Experiments, Modelling and Scale-up.
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SYSNO ASEP 0460635 Document Type C - Proceedings Paper (int. conf.) R&D Document Type The record was not marked in the RIV Title Polyamide Thin-Film Composite Membranes for Potential Raw Biogas Purification: Experiments, Modelling and Scale-up. Author(s) Izák, Pavel (UCHP-M) RID, ORCID, SAI
Šimčík, Miroslav (UCHP-M) RID, SAI, ORCID
Růžička, Marek (UCHP-M) RID, ORCID, SAI
Kárászová, Magda (UCHP-M) RID, SAI
Sedláková, Zuzana (UCHP-M) RID, ORCID, SAI
Vejražka, Jiří (UCHP-M) RID, ORCID, SAI
Friess, K. (CZ)Source Title Poster Presentation III, Gas and Molecular Separation. - - : North American Membrane Science, 2016 - ISBN N Pages s. 182-183 Number of pages 2 s. Publication form Online - E Action Annual Meeting NAMS 2016 /26./ Event date 21.05.2016 - 25.05.2016 VEvent location Washington Country US - United States Event type WRD Language eng - English Country US - United States Keywords raw biogas ; thin-film composite membrane ; mass transfer Subject RIV CI - Industrial Chemistry, Chemical Engineering R&D Projects LH14006 GA MŠMT - Ministry of Education, Youth and Sports (MEYS) Institutional support UCHP-M - RVO:67985858 EID SCOPUS 85040338352 Annotation The mass transfer coefficients of CO2 and CH4 in the Koch membrane as well as in the Sterlitech membrane were evaluated directly from experiments and by the developed permeation model for each individual experimental case. The final values of the mass transfer coefficients for CO2 and CH4 were evaluated as the averages and were used for the prediction model. The differences in CO2 permeate molar fractions between the experimental data and prediction model were in the range from -19 to +10 % for Koch membrane and from -5 to +4 % for Sterlitech membrane, respectively. Workplace Institute of Chemical Process Fundamentals Contact Eva Jirsová, jirsova@icpf.cas.cz, Tel.: 220 390 227 Year of Publishing 2017
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