//Variable declaration: F = 5000 //Mass flow rate of NaOH (lb/h) xF = 20/100 //Old concentration of NaOH solution TF = 100 //Feed temperature ( F) xL = 40/100 //New concentration of NaOH solution xv = 0 //Vapour concentration at x yv = 0 //Vapour concentration at y T1 = 198 //Boiling temperature of solution in the evaporator ( F) T2 = 125 //Saturated steam temperature ( F) U = 400 //Overall heat transfer coefficient (Btu/h.ft^2. F) Ts = 228 //Steam temperature ( F) //Calculation: //From steam tables at 228 F and 5 psig: hS = 1156 //Enthalpy of steam (Btu/lb) hC = 196 //Enthalpy of condensate (Btu/lb) hV = hS-hC //Enthalpy of vapour (Btu/lb) Tw = 125.4 //Boiling point of water at 4 in Hg absolute ( F) hS2 = 1116 //Enthalpy of saturated steam at 125 F (Btu/lb) hs = 0.46 //Heat capacity of superheated steam (Btu/lb. F) //From figure 18.3: hF = 55 //Enthalpy of feed (Btu/lb) hL = 177 //Enthalpy of liquor (Btu/lb) L = F*xF/xL //Mass of liquor (lb) V = L //Mass of vapour (lb) hV = hS2+hs*(T1-T2) //Enthalpy of vapour leaving the solution (Btu/lb) S = (V*hV+L*hL-F*hF)/(hS-hC) //Mass flow rate of steam (lb/h) Q = S*(hS-hC) //Total heat requirement (Btu) A = Q/(U*(Ts-T1)) //Required heat transfer area (ft^2) S = round(S*10**-1)/10**-1 //Result: printf("The steam flow rate is : %f lb/h .",S) printf("The required heat transfer area is : %.0f ft^2 .",A)