diff options
Diffstat (limited to 'Chemical_Engineering_Thermodynamics/ch17_1.ipynb')
| -rw-r--r-- | Chemical_Engineering_Thermodynamics/ch17_1.ipynb | 57 |
1 files changed, 23 insertions, 34 deletions
diff --git a/Chemical_Engineering_Thermodynamics/ch17_1.ipynb b/Chemical_Engineering_Thermodynamics/ch17_1.ipynb index f87043e6..004b3bab 100644 --- a/Chemical_Engineering_Thermodynamics/ch17_1.ipynb +++ b/Chemical_Engineering_Thermodynamics/ch17_1.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:e354b0525ce1aff27214eb76f8a2c9be56cfff2939a8a4b8688a7fe1cea4959c" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,8 +28,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determination of number of moles\n", - "\n", + " \n", "from scipy.optimize import fsolve \n", "import math \n", "\n", @@ -165,8 +165,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determination of equilibrium composition\n", - "\n", + " \n", "# Variables\n", "T = 600;\t\t\t#[K] - Reactor temperature\n", "P = 300;\t\t\t#[atm] - Reactor pressure\n", @@ -236,8 +235,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determination of the value of equilibrium constant\n", - "\n", + " \n", "# Variables\t\t\n", "T = 600;\t\t\t#[K] - Reactor temperature\n", "P = 4;\t\t\t#[atm] - Reactor pressure\n", @@ -332,8 +330,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determination of mole fraction\n", - "\n", + " \n", "# Variables\n", "T = 400;\t\t\t#[K] - Reactor temperature\n", "P = 1;\t\t\t#[atm] - Reactor pressure\n", @@ -380,7 +377,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determination of number of moles\n", + " \n", "\n", "# Variables\n", "T = 749.;\t\t\t#[K] - Reactor temperature\n", @@ -479,7 +476,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# \t\tCalculation of mole fraction\n", + " \n", "\n", "# Variables\n", "T = 500;\t\t\t#[K]\n", @@ -612,7 +609,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#Dtermination of heat of reaction \n", + " \n", "\n", "from scipy.optimize import fsolve \n", "import math \n", @@ -740,7 +737,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Tabulation of equilibrium constant values\n", + " \n", "\n", "from numpy import *\n", "\n", @@ -859,7 +856,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determination of mean standard enthalpy of reaction\n", + " \n", "\n", "# Variables\n", "\t\t\t# SO2 + (1/2)*O2 - SO3\n", @@ -905,7 +902,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determination of equilibrium composition\n", + " \n", "\n", "# Variables\n", "T_1 = 298.15;\t\t\t#[K]\n", @@ -1069,7 +1066,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determination of equilibrium composition\n", + " \n", "\n", "# Variables\n", "T = 25 + 298.15;\t\t\t#[K] - Temperature\n", @@ -1135,7 +1132,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determination of the\n", + " \n", "\n", "# Variables\t\t\t\n", "T_1 = 298.15;\t\t\t#[K] - Smath.tan(math.radiansard reaction temperature\n", @@ -1219,7 +1216,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of the value of Gibbs free energy\n", + " \n", "\n", "# Variables\n", "\t\t\t# CaCO3 (s1) - CaO (s2) + CO2 (g)\n", @@ -1284,7 +1281,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of nu\n", + " \n", "\n", "# Variables\n", "T = 700 + 273.15;\t\t\t#[K]\n", @@ -1359,8 +1356,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determination of value of the equilibrium constant\n", - "\n", + " \n", "# Variables \n", "T_1 = 298.15;\t\t\t#[K] - Smath.tan(math.radiansard reaction temperature\n", "T_2 = 1042;\t\t\t#[K] - Reaction temperature\n", @@ -1456,7 +1452,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determination of the value of equilibrium constant\n", + " \n", "\n", "# Variables \n", "T_1 = 298.15;\t\t\t#[k] - Smath.tan(math.radiansard reaction temperature\n", @@ -1545,8 +1541,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of standard equilibrium cell voltage\n", - "\n", + " \n", "# Variables\n", "delta_G_H2O_298 = -237.034;\t\t\t#[kJ/mol] - Smath.tan(math.radiansard Gibbs free energy of formation of H2O (l) at 298 K\n", "F = 96485;\t\t\t#[C/mol] - Faraday constant\n", @@ -1614,8 +1609,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of number of chemical reactions\n", - "\n", + " \n", "# Variables\t\t\t\n", "P = 2;\t\t\t# Number of phases\n", "C = 5;\t\t\t# Number of components\n", @@ -1704,8 +1698,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of number of chemical reactions\n", - "\n", + " \n", "# Variables\t\t\t\n", "T = 400.;\t\t\t#[K] - Temperature\n", "P = 1.;\t\t\t#[atm] - Pressure\n", @@ -1866,9 +1859,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of equilibrium composition\n", - "\n", - "# Variables\n", + " \n", "T = 600;\t\t\t#[K] - Temperature\n", "P = 1;\t\t\t#[atm] - Pressure\n", "R = 1.987;\t\t\t#[cal/mol-K] - Universal gas consatnt\n", @@ -1974,9 +1965,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determination of number of moles\n", - "\n", - "# Variables \n", + " \n", "T = 600 + 273.15;\t\t\t#[K] - Reaction temperature\n", "P = 1;\t\t\t#[atm] - Reaction pressure\n", "\n", |