Idioma: Inglés
Publicado por LAP Lambert Academic Publishing, 2012
ISBN 10: 384734711X ISBN 13: 9783847347118
Librería: preigu, Osnabrück, Alemania
EUR 51,00
Cantidad disponible: 5 disponibles
Añadir al carritoTaschenbuch. Condición: Neu. Liquid-Liquid Equilibria of Ternary Systems Using Solvent/Co-Solvent | The Liquid-Liquid Equilibria for pseudo-ternary Systems | Hatim M. Eissa (u. a.) | Taschenbuch | Englisch | LAP Lambert Academic Publishing | EAN 9783847347118 | Verantwortliche Person für die EU: preigu GmbH & Co. KG, Lengericher Landstr. 19, 49078 Osnabrück, mail[at]preigu[dot]de | Anbieter: preigu.
Idioma: Inglés
Publicado por LAP LAMBERT Academic Publishing, 2012
ISBN 10: 384734711X ISBN 13: 9783847347118
Librería: Mispah books, Redhill, SURRE, Reino Unido
EUR 137,98
Cantidad disponible: 1 disponibles
Añadir al carritoPaperback. Condición: Like New. LIKE NEW. SHIPS FROM MULTIPLE LOCATIONS. book.
Idioma: Inglés
Publicado por LAP LAMBERT Academic Publishing, 2012
ISBN 10: 384734711X ISBN 13: 9783847347118
Librería: moluna, Greven, Alemania
EUR 49,26
Cantidad disponible: Más de 20 disponibles
Añadir al carritoKartoniert / Broschiert. Condición: New. Dieser Artikel ist ein Print on Demand Artikel und wird nach Ihrer Bestellung fuer Sie gedruckt. Autor/Autorin: Eissa Hatim M.Dr.Hatim M.Eissa has obtained his PhD degree in Chemistry in 2002. He is author of several articles published in reputed journals and is the member of different working groups.Liquid-liquid equilibrium data of tolue.
Idioma: Inglés
Publicado por LAP Lambert Academic Publishing, 2012
ISBN 10: 384734711X ISBN 13: 9783847347118
Librería: AHA-BUCH GmbH, Einbeck, Alemania
EUR 59,71
Cantidad disponible: 2 disponibles
Añadir al carritoTaschenbuch. Condición: Neu. nach der Bestellung gedruckt Neuware - Printed after ordering - Liquid-liquid equilibrium data of toluene or benzene+n-hexane or n-heptane or n-octane hydrocarbon systems are reported with many solvent mixtures at 298.15K.Complete phase digrams were obtained by evaluating the solubility and tie line results for each ternary mixture. The thermodynamic models :NRTL,UNIQUAC,and UIFAC models were used to correlate the experimental data and to predict the phase compositions of the ternary systems.The NRTL equation fitted the experimental data better than the UNIQUAC and UNIFAC equations:the average root mean square deviations (RMSD) was 0.165 for NRTL as compared to 0.491 for UNIQUAC and 1.304 for UNIFAC.