diff options
Diffstat (limited to 'Chemical_Engineering_Thermodynamics/ch2_2.ipynb')
| -rw-r--r-- | Chemical_Engineering_Thermodynamics/ch2_2.ipynb | 59 |
1 files changed, 18 insertions, 41 deletions
diff --git a/Chemical_Engineering_Thermodynamics/ch2_2.ipynb b/Chemical_Engineering_Thermodynamics/ch2_2.ipynb index 659ed555..b3f8bd13 100644 --- a/Chemical_Engineering_Thermodynamics/ch2_2.ipynb +++ b/Chemical_Engineering_Thermodynamics/ch2_2.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:6aa23fb1475338cf467e7afb5732b8b9e456bbb3ad63c14224d73232d920457e" }, "nbformat": 3, "nbformat_minor": 0, @@ -28,8 +29,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determination of acentric factor\n", - "\n", + " \n", "import math\n", "\n", "# Variables\n", @@ -71,8 +71,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of acentric factor\n", - "\n", + " \n", "# Variables\n", "\t\t\t#math.log10(Psat)=8.1122-(1592.864/(t+226.184))\t\t\t# 'Psat' in [mm Hg] and 't' in [c]\n", "Tc = 513.9;\t\t\t#[K] - Critical temperature\n", @@ -116,8 +115,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of virial coefficients\n", - "\n", + " \n", "# Variables\n", "T = 380;\t\t\t#[K] - Temperature\n", "Tc = 562.1;\t\t\t#[K] - Critical temperature\n", @@ -173,8 +171,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of mass using virial equation of state\n", - "\n", + " \n", "# Variables\n", "V_1 = 0.3;\t\t\t#[m**(3)]\t\t\t#volume of cylinder\n", "T = 60+273.15;\t\t\t#[K] - Temperature\n", @@ -234,8 +231,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of molar volume\n", - "\n", + " \n", "# Variables\n", "T = 373.15;\t\t\t#[K] - Temperature\n", "P = 101325;\t\t\t#[N/m**(2)] - Pressure\n", @@ -288,8 +284,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of molar volume and virial coefficients\n", - "\n", + " \n", "# Variables\n", "T = 50+273.15;\t\t\t#[K] - Temperature\n", "P = 15*10**(5)\t\t\t#[N/m**(2)] - Pressure\n", @@ -405,9 +400,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determination of second and third virial coefficients\n", - "\n", - "# Variables\n", + " \n", "T = 0 + 273.15;\t\t\t#[K] - Temperature\n", "R = 8.314;\t\t\t#[J/mol*K] - Universal gas constant\n", "from numpy import linalg,array\n", @@ -464,9 +457,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Estimation of second virial coefficient\n", - "\n", - "# Variables\n", + " \n", "T = 444.3;\t\t\t#[K] - Temperature\n", "R = 8.314;\t\t\t#[J/mol*K] - Universal gas constant\n", "B_11 = -8.1;\t\t\t#[cm**(3)/mol]\n", @@ -532,9 +523,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Estimation of molar volume\n", - "\n", - "# Variables\n", + " \n", "T = 71+273.15;\t\t\t#[K] - Temperature\n", "P = 69*10**(5)\t\t\t#[N/m**(2)] - Pressure\n", "y1 = 0.5;\t\t\t#[mol] - mole fraction of equimolar mixture\n", @@ -625,9 +614,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of maximum temperature\n", - "\n", - "# Variables\n", + " \n", "P = 6.*10**(6)\t\t\t# [Pa] - Pressure\n", "P_max = 12.*10**(6)\t\t\t# [Pa] - Max pressure to which cylinder may be math.exposed\n", "T = 280.;\t\t\t#[K] - Temperature\n", @@ -755,10 +742,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of pressure\n", - "\n", - "# Variables\n", - "\n", + " \n", "V_vessel = 0.1;\t\t\t#[m**(3)]\t\t\t# Volume of vessel\n", "T = 25 + 273.15;\t\t#[K] - Temperature\n", "R = 8.314;\t\t\t#[J/mol*K] - Universal gas constant\n", @@ -815,9 +799,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of pressure\n", - "\n", - "# Variables\n", + " \n", "\n", "V_vessel = 360*10**(-3)\t\t\t#[m**(3)] - volume of vessel\n", "T = 62+273.15;\t\t\t#[K] - Temperature\n", @@ -905,9 +887,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determination of compressibility factor\n", - "\n", - "# Variables\n", + " \n", "T = 500+273.15;\t\t\t#[K] - Temperature\n", "R = 8.314;\t\t\t#[J/mol*K] - Universal gas constant\n", "P = 325*1000;\t\t\t#[Pa] - Pressure\n", @@ -981,8 +961,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determination of molar volume\n", - "\n", + " \n", "from scipy.optimize import fsolve\n", "\n", "\n", @@ -1054,8 +1033,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of volume\n", - "\n", + " \n", "# Variables\n", "T = 500+273.15;\t\t\t#[K] - Temperature\n", "P = 15.;\t\t\t#[atm] - Pressure\n", @@ -1173,8 +1151,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Estimation of compressibility factor\n", - "\n", + " \n", "# Variables\n", "T = 310.93;\t\t\t#[K] - Temperature\n", "P = 2.76*10**(6)\t\t\t#[N/m**(2)] - Pressure\n", |