Dataset: titaniaalumina.csv Source: S. Tong, I.G. Dalla Lana, K.T. Chuang (1993). "Kinetic Modelling of the Hydrolysis of Carbonyl Sulfide Catalyzed by Either Titania or Alumina," The Canadian Journal of Chemical Engineering, Vol. 71, pp. 392-400. Description: Models of Kinetics for process catalyzed by titania or alumina. Y = reverse reaction rate X1 = inlet P_cos, X2=inlet P_H2O, X3=outlet P_cos, X4=outlet P_H2O Models fit: Eley-Rideal: Y = B1B2X1X2/(1+B2X2) Modified Eley-Rideal: Y=B1B2X1X2/(1+B2X2)^B3 Langmuir-Hinshelwood Model 1: Y = B1B2B3X1X2/(1+B2X1+B3X2) Langmuir-Hinshelwood Model 2: Y = B1B2B3X1X2/((1+B2X1)(1+B3X2)) variable Names: metal /* 1=alumina 2=titania */ tempC /* temperature */ inP_cos inP_H2O outP_cos outP_H2O rate_cos