CKtes kiECUACION PARA LA CORRELACION DE LAS CONSTANTES DE EQUILIBRIO A PRESION Y TEMPERATURA DADAVALORES DE LOS COEFICIENTES PARA HIDROCARBUROS LIGEROS PARA CALCULAR LA CONSTANTE DE EQUILIBRIO EN FUNCION DE LA PRESION (psia) Y LA TEMPERATURA (R)COMPONENTEaT1aT2aT3aT4aT5aT6aP1aP2aP3aP4aP5COMPONENTEMetanoc1-292,860.0000 00008.24450-0.8951059.84650000MetanoEtilenoc2=-600,076.8750 00007.90595-0.8467742.94594000EtilenoEtanoc2-687,248.2500 00007.90699-0.8860049.02654000EtanoPropilenoc3=-923,484.6875 00007.71725-0.8787147.67624000PropilenoPropanoc3-970,688.5625 00007.15059-0.7698406.9022400PropanoIsobutanoic4-1,166,846.0000 00007.72668-0.922130000Isobutanon-Butanonc4-1,280,557.0000 00007.94986-0.964550000n-ButanoIsopentanoiC5-1,481,583.0000 00007.58071-0.931590000IsopentanonPentanonC5-1,524,891.0000 00007.33129-0.891430000nPentanon-HexanonC6-1,778,901.0000 00006.96783-0.846340000n-Hexanon-HeptanonC7-2,013,803.0000 00006.52914-0.795340000n-Heptanon-OctanonC80.0000 -7,646.81641 00012.48457-0.731520000n-Octanon-NonanonC9-2,551,040.0000 00005.69313-0.678180000n-Nonanon-DecanonC100.0000 -9,760.45703 00013.80354-0.714700000n-Decano