Search Results - "MORAVKOVA, Lenka"

Organic vapour permeation in amorphous and semi-crystalline rubbery membranes: Experimental data versus prediction by solubility parameters by Jirsáková, Karolina, Stanovský, Petr, Dytrych, Pavel, Morávková, Lenka, Přibylová, Kateřina, Petrusová, Zuzana, Jansen, Johannes C., Izák, Pavel

“…The applicability of Hansen and Hoftyzer and van Krevelen solubility parameters for the prediction of potential VOC/N2 separation efficiency was analysed with…”
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Regeneration of thin-film composite membrane used for permeation of hexane vapors by Petrusová, Zuzana, Morávková, Lenka, Stanovský, Petr, Machanová, Karolina, Koštejn, Martin, Jandová, Věra, Izák, Pavel

“…•TFC membrane ages after exposure of hexane vapors and storage at dry conditions.•Membrane flux decreases while selectivity is improved for aged…”
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Volumetric behavior of the ternary system (methyl tert-butyl ether+methylbenzene+butan-1-ol) and its binary sub-system (methyl tert-butyl ether+butan-1-ol) within the temperature range (298.15 to 328.15)K by Morávková, Lenka, Troncoso, Jacobo, Škvorová, Magda, Havlica, Jaromír, Petrus, Pavel, Sedláková, Zuzana

“…•Excess molar volume determined from experimental density values.•Excess adiabatic compressibility.•Excess isobaric thermal expansivity.•Peng–Robinson equation…”
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Minimization of the Theoretical Error of Input Parameters for a Vapor Permeation Apparatus by Dytrych, Pavel, Vajglová, Zuzana, Morávková, Lenka, Jandová, Věra, Izák, Pavel, Petrusová, Zuzana

“…All input experimental errors for membrane flux determination were analyzed. The overall error in pressure did not largely influence the determination of…”
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Biomethane Production from Biogas by Separation Using Thin‐Film Composite Membranes by Sedláková, Zuzana, Kárászová, Magda, Vejražka, Jiří, Morávková, Lenka, Esposito, Elisa, Fuoco, Alessio, Jansen, Johannes Carolus, Izák, Pavel

“…Raw biogas obtained from a sewage plant was successfully purified by a single‐step method to a quality compatible with compressed natural gas (CNG) standards…”
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Volumetric behaviour of the (2,2,4-trimethylpentane+methylbenzene+butan-1-ol) ternary system and its binary sub-systems within the temperature range (298.15–328.15)K by Morávková, Lenka, Troncoso, Jacobo, Machanová, Karolina, Sedláková, Zuzana

“…•Density measurements.•Excess molar volume at atmospheric pressure.•Redlich–Kister equation.•ERAS model.•Comparison of our data with literature data. Densities…”
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Volumetric behavior of the ternary system benzene-2-methoxy-2-methylbutane-2,2,4-trimethylpentane and all binary sub-systems at temperature range (298.15–318.15)K by HOUSKOVA, Hana, MORAVKOVA, Lenka, SEDLAKOVA, Zuzana, BOUBLIK, Tomas, KOLSKA, Zdenka

“…► Density measurements. ► Excess molar volume at atmospheric pressure. ► Redlich–Kister equation. ► Peng–Robinson equation. ► Comparison of our data with…”
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Ceramic Foam-Supported Perovskites as Catalysts for Combustion of Methane by Jirátová, Květa, Morávková, Lenka, Malecha, Jiří, Koutský, Bohumil

“…Methane combustion in the presence of various types of perovskites supported on ceramic foams has been studied with respect to the CO and NO x formation. The…”
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Ceramic Foam in Catalytic Combustion of Methane by Jirátová, Květa, Morávková, Lenka, Malecha, Jiří, Koutský, Bohumil

“…Catalytic combustion of methane has been studied in the presence of catalysts supported on ceramic foams. Low concentrations of NO x (in the range of 5 - 50 mg…”
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Reductive amination of diethylene glycol to morpholine over supported nickel catalysts : zeolites as catalyst admixtures by JIRATOVA, K, SNAJDAUFOVA, H, MORAVKOVA, L, KUBELKOVA, L

“…The effect of HZSM-5, H-silicalite and amorphous silica admixtures on the surface properties of nickel catalysts as well as on their activities, selectivities…”
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Examination of high-loaded nickel catalysts by IR spectroscopy : effect of the support and Pd on surface properties by JIRATOVA, K, MORAVKOVA, L, SNAJDAUFOVA, H, PAUKSHTIS, E. A

“…Activation of the ammonia molecule and subsequent adsorption of the NH 2 fragment on the surface of the NiO + Pd/TiO 2 catalysts, in contrast to NiO + Pd/SiO 2…”
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