From b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b Mon Sep 17 00:00:00 2001 From: priyanka Date: Wed, 24 Jun 2015 15:03:17 +0530 Subject: initial commit / add all books --- 479/CH14/EX14.3/Example_14_3.sce | 51 ++++++++++++++++++++++++++++++++++++++++ 1 file changed, 51 insertions(+) create mode 100755 479/CH14/EX14.3/Example_14_3.sce (limited to '479/CH14/EX14.3/Example_14_3.sce') diff --git a/479/CH14/EX14.3/Example_14_3.sce b/479/CH14/EX14.3/Example_14_3.sce new file mode 100755 index 000000000..71bb32ae9 --- /dev/null +++ b/479/CH14/EX14.3/Example_14_3.sce @@ -0,0 +1,51 @@ +//Chemical Engineering Thermodynamics +//Chapter 14 +//Thermodynamics of Chemical Reactions + +//Example 14.3 +clear; +clc; + +//Given +H_C2H4 = 12500;//Standard heat of formation of ethylene at 25 de cel +H_C2H4O = -12190;//Standard heat of formation of ethylene oxide at 25 deg cel +H_CO2 = -94052;//Standard heat of formation of CO2 at 25 deg cel +H_H2O = -57798;//Standard heat of formation of H2O at 25 deg cel +T1 = 200;//temperature at which mixture entered in deg cel +Ti = 25;//intermediate temperature in deg cel +T2 = 260;//product temperature in deg cel +Cp_air_a = 7;//Mean specific heat for 25 to 200 deg cel in Kcal/Kgmole +Cp_C2H4_a = 18;//Mean specific heat for 25 to 200 deg cel in Kcal/Kgmole +//Mean specific heat for 25 to 260 deg cel in Kcal/Kgmole are given as: +Cp_C2H4_b = 19; +Cp_C2H4O_b = 21; +Cp_O2_b = 7.30; +Cp_N2_b = 7.00; +Cp_CO2_b = 10.00; +Cp_H2O_b = 8.25; +//Basis: 1 Kgmole of ethylene as feed +n_air = 9;//Kgmoles +n_C2H4 =1;//Kgmoles +n_C2H4_1 = 0.6//ethylene consumed while converting in C2H4O in Kgmoles (Rxn 1) +n_C2H4_2 = 0.3;//ethylene burnt completely to CO2 in Kgmoles (Rxn 2) + +//To Calculate the heat must be removed if the product temperature should not exceed 260 deg cel +n_O2 = n_air*0.21;//Kgmoles of O2 fed +n_N2 = n_air-n_O2;//Kgmoles of N2 fed +//Rxn 1: (0.6)C2H4 + (0.3)O2 - (0.6)C2H4O;...(i) 60% of C2H4 is converted to C2H4O +n_O2_1 = n_C2H4_1/2;//Kgmoles of oxygen consumed +n_C2H4O_1 = n_C2H4_1;//C2H4O formed in Kgmoles +//Rxn 2: (0.3)C2H4 + (0.9)O2 - (0.6)CO2+ (0.6)H20;...(ii) 30%conversion +n_O2_2 = 3*n_C2H4_2;//Kgmoles of O2 reacted +n_CO2_2 = 2*n_C2H4_2;//Kgmoles of CO2 formed +n_H2O_2 = 2*n_C2H4_2;//Kgmoles of H2O formed +n_C2H4_r = n_C2H4 - n_C2H4_1 - n_C2H4_2;//unreacted ethylene in Kgmoles +n_O2_r = n_O2 - n_O2_1-n_O2_2;//unreacted O2 in Kgmoles +//The overall rxn is given by (i)&(ii), +//(0.9)C2H4 + (1.2)O2 - (0.6)C2H4O + (0.6)CO2 + (0.6)H2O...(iii) +del_H = (0.6*H_C2H4O)+(0.6*H_CO2)+(0.6*H_H2O)-(0.9*H_C2H4);//since,standard enthalpy of O2 is zero; Standard heat of rxn in Kcal/Kgmole +Q1 = (n_C2H4*Cp_C2H4_a + n_air*Cp_air_a)*(Ti-T1);//Sensible heat in feed in Kcal +Q2 = (n_C2H4_r*Cp_C2H4_b + n_C2H4O_1*Cp_C2H4O_b + n_CO2_2*Cp_CO2_b + n_H2O_2*Cp_H2O_b + n_O2_r*Cp_O2_b + n_N2*Cp_N2_b)*(T2-Ti);//Sensible heat in product in Kcal +Q = Q1+Q2+del_H; +mprintf('The heat to be removed is %f Kcal so that the product temperature is 260 deg celsius',-Q); +//end -- cgit