Zobrazeno 1 - 10
of 19
pro vyhledávání: '"P.J.G. Huttenhuis"'
Autor:
Nathalie J. M. C. Penders-van Elk, Geert Versteeg, Nick Aldenkamp, P.J.G. Huttenhuis, Espen S. Hamborg
Publikováno v:
Journal of Chemical & Engineering Data. 59:3397-3406
In this work the vapor liquid equilibria (VLE) of carbon dioxide in both taurine (KTaurate) and glycine (KGlycinate) potassium salts are measured and compared to literature data. The VLE data were measured at two salt concentrations of approximately
Autor:
Sylvie Fradette, Nathalie J. M. C. Penders-van Elk, Geert Versteeg, P.J.G. Huttenhuis, Espen S. Hamborg, Jonathan Carley
Publikováno v:
International Journal of Greenhouse Gas Control, 12(12), 259-268. ELSEVIER SCI LTD
In the present work the absorption of carbon dioxide in aqueous N-methyldiethanolamine (MDEA) and aqueous sodium carbonate with and without carbonic anhydrase (CA) was studied in a stirred cell contactor in the temperature range 298-333 K. The CA was
Publikováno v:
Industrial and Engineering Chemistry Research, 48(8), 4051-4059. AMER CHEMICAL SOC
In this work, 72 new experimental solubility data points for H(2)S and CO(2) mixtures in aqueous N-methyldiethanol amine (MDEA) solutions at different methane partial pressures (up to 69 bara) are presented. They are correlated using an electrolyte e
Publikováno v:
Energy Procedia, 1(1), 1131-1138
Carbon dioxide can be removed from flue gas streams with aqueous solutions of alkanolamines. In the absorber carbon dioxide is contacted with the solvent and due to several chemical reactions the carbon dioxide is converted into ionic species. These
Publikováno v:
Fluid Phase Equilibria, 264(1), 99-112. ELSEVIER SCIENCE BV
In this study the electrolyte equation of state as proposed by Solbraa [E. Solbraa, Equilibrium and non-equilibrium thermodynamics of natural gas processing, Ph.D. thesis Norwegian University of Science and Technology, 2002] was systematically studie
Publikováno v:
Energy Procedia, 4(1), 599-605
Aqueous solutions of alkanolamines are commonly used in CO2 capture processes. To describe these complex processes rigorous mass transfer models are needed, in which all mass transfer, kinetics and thermodynamics are incorporated correctly. To improv
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::baa2b9abfdb6161f33b9e708631d2c42
https://research.rug.nl/en/publications/0b82d074-9362-4ff5-9368-04ce48888a2c
https://research.rug.nl/en/publications/0b82d074-9362-4ff5-9368-04ce48888a2c
Publikováno v:
International Journal of Oil, Gas and Coal Technology, 1(4), 399-424
In this work the electrolyte equation of state as developed previously for the system MDEA-H2O-CO2-CH4 (Huttenhuis et al. (2008), pp.99-112) was further developed for the system MDEA-H2O-H2S-CH4. With this thermodynamic equilibrium model the total so
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