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Sono state utilizzate equazioni di stato cubiche (EoS) e differenti regole di mixing per ottenere il miglior fitting di dati sperimentali di equilibrio liquido-vapore per il sistema anidride carbonica – acqua (CO2 – H2O). Particolare attenzione è stata posta sulla regola di mixing Panagiotopoulus – Reid andando a ricavare un’espressione generalizzata per i suoi parametri nell’intervallo 110-350°C in funzione della EoS di Peng – Robinson. Cubic equations of state (EoS) have been adopted and different mixing rules have been used to obtain the best fitting of experimental data on vapor-liquid equilibrium (VLE) for carbon dioxide — water (CO2 – H2O). A special attention has been paid to the Panagiotopoulus — Reid mixing rule in order to determine a general relationship for the related parameters in the range 110-350°C to be used in the Peng-Robinson EoS.
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Sono state utilizzate equazioni di stato cubiche (EoS) e differenti regole di mixing per ottenere il miglior fitting di dati sperimentali di equilibrio liquido-vapore per il sistema anidride carbonica – acqua (CO2 – H2O). Particolare attenzione è stata posta sulla regola di mixing Panagiotopoulus – Reid andando a ricavare un’espressione generalizzata per i suoi parametri nell’intervallo 110-350°C in funzione della EoS di Peng – Robinson. Cubic equations of state (EoS) have been adopted and different mixing rules have been used to obtain the best fitting of experimental data on vapor-liquid equilibrium (VLE) for carbon dioxide — water (CO2 – H2O). A special attention has been paid to the Panagiotopoulus — Reid mixing rule in order to determine a general relationship for the related parameters in the range 110-350°C to be used in the Peng-Robinson EoS.
Studio del sistema Anidride Carbonica- Acqua con differenti EoS cubiche e reg...
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diego_caccavo
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Presentazione s nifosi ita engl 2013
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