diff options
Diffstat (limited to 'Chemical_Engineering_Thermodynamics/ch14_1.ipynb')
| -rw-r--r-- | Chemical_Engineering_Thermodynamics/ch14_1.ipynb | 34 |
1 files changed, 12 insertions, 22 deletions
diff --git a/Chemical_Engineering_Thermodynamics/ch14_1.ipynb b/Chemical_Engineering_Thermodynamics/ch14_1.ipynb index 03350db4..be081f3c 100644 --- a/Chemical_Engineering_Thermodynamics/ch14_1.ipynb +++ b/Chemical_Engineering_Thermodynamics/ch14_1.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:98f2e1e0f1c561d3ee302fd629093b7572c8b263613f73036059e7020f90d8cc" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,8 +28,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Proving a mathematical relation\n", - "\n", + " \n", "import math\n", "\n", "# Variables,\n", @@ -93,9 +93,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Comparision of Margules and van Laar eqations\n", - "\n", - "\n", + " \n", "import math \n", "from numpy import zeros\n", "from scipy.stats import linregress\n", @@ -169,8 +167,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of activity coefficients\n", - "\n", + " \n", "# Variables,\n", "T = 60 + 273.15;\t\t\t#[K] - Temperature\n", "R = 1.987;\t\t\t#[cal/mol*K] - Universal gas constant\n", @@ -244,8 +241,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of the value of activity coefficients\n", - "\n", + " \n", "# Variables \n", "T = 307;\t\t\t#[K]\n", "x_1 = 0.047;\n", @@ -372,8 +368,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of the value of activity coefficients\n", - "\n", + " \n", "# Variables,\n", "T = 25 + 273.15;\t\t\t#[K] - Temperature\n", "R = 1.987;\t\t\t#[cal/mol*K] - Universal gas constant\n", @@ -426,8 +421,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of the value of activity coefficients\n", - "\n", + " \n", "# Variables,\n", "T = 25 + 273.15;\t\t\t#[K] - Temperature\n", "mol_HCl = 0.001;\t\t\t#[mol/kg] - Molality of HCl\n", @@ -479,8 +473,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of the value of activity coefficients\n", - "\n", + " \n", "# Variables,\n", "T = 25 + 273.15;\t\t\t#[K] - Temperature\n", "mol_CaCl2 = 0.001;\t\t\t#[mol/kg] - Molality of HCl\n", @@ -528,8 +521,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Proving a mathematical relation\n", - "\n", + " \n", "# Variables,\n", "T = 50 + 273.15;\t\t\t#[K] - Temperature\n", "R=8.314;\t\t\t#[J/mol*K] - Universal gas constant\n", @@ -583,8 +575,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# calculation of enthalpy entropy and Gibbs free energy\n", - "\n", + " \n", "# Variables\n", "T = 293.15;\t\t\t#[K] - Temperature\n", "R=8.314;\t\t\t#[J/mol*K] - Universal gas constant\n", @@ -654,8 +645,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determination of Gibbs free energy and enthalpy change\n", - "\n", + " \n", "# Given\n", "T = 60 + 273.15;\t\t\t#[K] - Temperature\n", "R = 8.314;\t\t\t#[J/mol*K] - Universal gas constant\n", |