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+
+clc
+//Initialization of variables
+G = 2.3 // Gas flow in gmol/sec
+L = 4.8 // Liquid flow in gmol/sec
+y0 = 0.0126 // entering gas Mole fraction of CO2
+yl = 0.0004 // Exiting gas mole fraction of CO2
+xl = 0 // Exiting liquid mole fraction of CO2
+d = 40 // Diameter of the tower in cm
+x0star = 0.0080// if the amine left in equilibrium with the entering gas would contain 0.80 percent C02
+Kya = 5*10^-5 // Overall M.T.C and the product times the area per volume in gmol/cm^3-sec
+//Calculations
+A =%pi*(d^2)/4
+x0 = ((G*(y0-yl))/(L)) + xl // Entering liquid mole fraction of CO2
+m = y0/x0star // Equilibirum constant
+c1 = G/(A*Kya)
+c2 = 1/(1-(m*G/L))
+c3 = log((y0-m*x0)/(yl-m*xl))
+l = (G/(A*Kya))*(1/(1-((m*G)/L)))*(log((y0-m*x0)/(yl-m*xl)))/100 //length of the tower in metres
+//Results
+printf("The length of the tower is %.1f m",l)