{ "cells": [ { "cell_type": "markdown", "metadata": {}, "source": [ "## Chapter 11 - Additional topics in phase equillibrium" ] }, { "cell_type": "markdown", "metadata": {}, "source": [ "## Example: 11.1 Page: 458" ] }, { "cell_type": "code", "execution_count": 4, "metadata": { "collapsed": false }, "outputs": [ { "name": "stdout", "output_type": "stream", "text": [ "Example: 11.1 - Page: 458\n", "\n", "\n", "Molecular Formula of Sulphur is S8\n" ] } ], "source": [ "from __future__ import division\n", "print \"Example: 11.1 - Page: 458\\n\\n\"\n", "\n", "# Solution\n", "\n", "#*****Data******#\n", "a = 2.423## [g]\n", "b = 100## [g]\n", "Lf = 35.7## [cal/g]\n", "Tf = 353.1## [cal/g]\n", "delta_Tf = 0.64## [OC]\n", "R = 2## [cal/mol K]\n", "Mw = 32## [Molecular wt. of Sulphur, g/mol]\n", "#*************#\n", "\n", "M2 = ((R*Tf**2/(1000*Lf))*(a*1000/(b)))/delta_Tf## [g/mol]\n", "n = M2/Mw#\n", "print \"Molecular Formula of Sulphur is S%d\"%(round(n))#" ] }, { "cell_type": "markdown", "metadata": {}, "source": [ "## Example: 11.2 Page: 459" ] }, { "cell_type": "code", "execution_count": 5, "metadata": { "collapsed": false }, "outputs": [ { "name": "stdout", "output_type": "stream", "text": [ "Example: 11.2 - Page: 459\n", "\n", "\n", "Molal Freezing point is 5.10 kg/kmol\n", "\n" ] } ], "source": [ "print \"Example: 11.2 - Page: 459\\n\\n\"\n", "\n", "# Solution\n", "\n", "#*****Data******#\n", "Tf = 5 + 273## [K]\n", "Lf = 9830## [J/mol]\n", "R = 8.314## [J/mol K]\n", "M1 = 78## [kg/kmol]\n", "#**************#\n", "\n", "Kf = R*Tf**2*M1/(1000*Lf)## [kg/kmol]\n", "print \"Molal Freezing point is %.2f kg/kmol\\n\"%(Kf)#" ] }, { "cell_type": "markdown", "metadata": {}, "source": [ "## Example: 11.3 Page: 458" ] }, { "cell_type": "code", "execution_count": 6, "metadata": { "collapsed": false }, "outputs": [ { "name": "stdout", "output_type": "stream", "text": [ "Example: 11.3 - Page: 458\n", "\n", "\n", "Latent Heat of Fusion of phenol is 26.54 cal/g\n", "\n" ] } ], "source": [ "print \"Example: 11.3 - Page: 458\\n\\n\"\n", "\n", "# Solution\n", "\n", "#*****Data******#\n", "T_melting = 40## [OC]\n", "Tf = T_melting + 273## [K]\n", "a = 0.172## [g]\n", "b = 12.54## [g]\n", "T_new = 39.25## [OC]\n", "M2 = 135## [Molecular wt. of acetanilide, g/mol]\n", "R = 2## [cal/mol K]\n", "#**************#\n", "\n", "delta_T = T_melting - T_new## [OC]\n", "Kf = delta_T*b*M2/(1000*a)#\n", "Lv = ((R*Tf**2/(1000)))/Kf## [cal/g]\n", "print \"Latent Heat of Fusion of phenol is %.2f cal/g\\n\"%(Lv)#" ] }, { "cell_type": "markdown", "metadata": {}, "source": [ "## Example: 11.4 Page: 461" ] }, { "cell_type": "code", "execution_count": 7, "metadata": { "collapsed": false }, "outputs": [ { "name": "stdout", "output_type": "stream", "text": [ "Example: 11.4 - Page: 461\n", "\n", "\n", "Molecular weight of anthracene is 178 kg/kmol\n" ] } ], "source": [ "print \"Example: 11.4 - Page: 461\\n\\n\"\n", "\n", "# Solution\n", "\n", "#*****Data******#\n", "T_boiling = 118.24## [OC]\n", "Tb = T_boiling + 273## [K]\n", "a = 0.4344## [g]\n", "b = 44.16## [g]\n", "Lv = 121## [cal/g]\n", "T_new = 118.1## [OC]\n", "R = 2## [cal/mol K]\n", "#**************#\n", "\n", "delta_Tb = T_boiling - T_new## [OC]\n", "M2 = (R*Tb**2/(1000*Lv))*(a*1000/(b*delta_Tb))#\n", "print \"Molecular weight of anthracene is %d kg/kmol\"%(round(M2))#" ] }, { "cell_type": "markdown", "metadata": {}, "source": [ "## Example: 11.5 Page: 462" ] }, { "cell_type": "code", "execution_count": 1, "metadata": { "collapsed": false }, "outputs": [ { "name": "stdout", "output_type": "stream", "text": [ "Example: 11.5 - Page: 462\n", "\n", "\n", "Molar Latent Heat of Vaporisation is 31638 J/mol\n" ] } ], "source": [ "print \"Example: 11.5 - Page: 462\\n\\n\"\n", "\n", "# Solution\n", "\n", "#*****Data******#\n", "delta_Tb = 2.3## [K]\n", "w1 = 100## [g]\n", "M1 = 78## [g/mol]\n", "w2 = 13.86## [g]\n", "M2 = 154## [g/mol]\n", "Tb = 353.1## [K]\n", "R = 8.314## [J/mol K]\n", "#****************#\n", "\n", "# Molality:\n", "m = w2*1000/(w1*M2)## [mol/kg]\n", "# Molal Elevation Constant:\n", "Kb = delta_Tb/m## [K kg/mol]\n", "# Molar Latent Heat of Vaporisation:\n", "Lv = R*Tb**2*M1/(1000*Kb)## [J/mol]\n", "print \"Molar Latent Heat of Vaporisation is %d J/mol\"%(Lv)#" ] }, { "cell_type": "markdown", "metadata": {}, "source": [ "## Example: 11.6 Page: 465" ] }, { "cell_type": "code", "execution_count": 10, "metadata": { "collapsed": false }, "outputs": [ { "name": "stdout", "output_type": "stream", "text": [ "Example: 11.6 - Page: 465\n", "\n", "\n", "Osmotic Pressure is 594.38 kPa\n", "\n" ] } ], "source": [ "print \"Example: 11.6 - Page: 465\\n\\n\"\n", "\n", "# Solution\n", "\n", "#*****Data******#\n", "Temp = 50 + 273## [K]\n", "w2 = 60## [g]\n", "w1 = 1500## [g]\n", "M1 = 18## [g/mol]\n", "M2 = 180## [g/mol]\n", "Vl = 18*10**(-6)## [Molar Volume of water, cubic m/mol]\n", "R = 8.314## [J/mol K]\n", "#***************#\n", "\n", "# Mole fraction of glucose:\n", "x2 = (w2/M2)/((w2/M2) + (w1/M1))#\n", "# Applying Eqn. (11.45):\n", "P = R*Temp*x2/Vl## [N/square m]\n", "P = P/1000## [kPa]\n", "print \"Osmotic Pressure is %.2f kPa\\n\"%(P)#" ] }, { "cell_type": "markdown", "metadata": {}, "source": [ "## Example: 11.7 Page: 465" ] }, { "cell_type": "code", "execution_count": 11, "metadata": { "collapsed": false }, "outputs": [ { "name": "stdout", "output_type": "stream", "text": [ "Example: 11.7 - Page: 465\n", "\n", "\n", "Osmotic Pressure of the solution is 4.92 atm\n" ] } ], "source": [ "print \"Example: 11.7 - Page: 465\\n\\n\"\n", "\n", "# Solution\n", "\n", "#*****Data******#\n", "w2 = 0.6## [g]\n", "w3 = 1.8## [g]\n", "Temp = 27 + 273## [K]\n", "V1 = 100## [cubic cm]\n", "M2 = 60## [g/mol]\n", "M3 = 180## [g/mol]\n", "R = 0.082## [L.atm/mol.K]\n", "#****************#\n", "\n", "V1 = V1/1000## [litre]\n", "# C: Concentration per litre\n", "C = ((w2/M2) + (w3/M3))/V1## [mol/litre]\n", "P = C*R*Temp## [atm]\n", "print \"Osmotic Pressure of the solution is %.2f atm\"%(P)#" ] } ], "metadata": { "kernelspec": { "display_name": "Python 2", "language": "python", "name": "python2" }, "language_info": { "codemirror_mode": { "name": "ipython", "version": 2 }, "file_extension": ".py", "mimetype": "text/x-python", "name": "python", "nbconvert_exporter": "python", "pygments_lexer": "ipython2", "version": "2.7.9" } }, "nbformat": 4, "nbformat_minor": 0 }