From fba055ce5aa0955e22bac2413c33493b10ae6532 Mon Sep 17 00:00:00 2001 From: hardythe1 Date: Tue, 5 May 2015 14:21:39 +0530 Subject: add books --- .../Chapter17-Ideal_solutions.ipynb | 250 --------------------- 1 file changed, 250 deletions(-) delete mode 100755 Thermodynamics:_From_concepts_to_applications/Chapter17-Ideal_solutions.ipynb (limited to 'Thermodynamics:_From_concepts_to_applications/Chapter17-Ideal_solutions.ipynb') diff --git a/Thermodynamics:_From_concepts_to_applications/Chapter17-Ideal_solutions.ipynb b/Thermodynamics:_From_concepts_to_applications/Chapter17-Ideal_solutions.ipynb deleted file mode 100755 index 2d6dc101..00000000 --- a/Thermodynamics:_From_concepts_to_applications/Chapter17-Ideal_solutions.ipynb +++ /dev/null @@ -1,250 +0,0 @@ -{ - "metadata": { - "name": "", - "signature": "sha256:0bd1584504a5182c99f46d576a77cfaa07f83a047faf3b55eaafd0cea74518f2" - }, - "nbformat": 3, - "nbformat_minor": 0, - "worksheets": [ - { - "cells": [ - { - "cell_type": "heading", - "level": 1, - "metadata": {}, - "source": [ - "Chapter17-Ideal solutions" - ] - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "Example1-pg367" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "import math\n", - "#calculate Total pressure and composition of vapour phases and composition of last drop liquids\n", - "##initialisation of variables\n", - "Pa= 40. ##kPa\n", - "Pb= 50. ##kPa\n", - "na= 2. ##moles\n", - "nb= 6. ##moles\n", - "##CALCULATIONS\n", - "a= Pb/Pa\n", - "xa= na/(na+nb)\n", - "xb= 1.-xa\n", - "p= xa*Pa+xb*Pb\n", - "y= (xa*Pa)/p\n", - "ya= 1.-y\n", - "Xa= a*xa/(1+(a-1)*xa)\n", - "Xb= 1.-Xa\n", - "##RESULTS\n", - "print'%s %.1f %s'%('Total pressure=',p,'kPa')\n", - "print'%s %.4f %s'%('composition of vapour phase=',y,'')\n", - "print'%s %.4f %s'%('composition of vapour phase=',ya,'')\n", - "print'%s %.4f %s'%('composition of last drop of liquid=',Xa,'')\n", - "print'%s %.4f %s'%('composition of last drop of liquid=',Xb,'')\n" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "Total pressure= 47.5 kPa\n", - "composition of vapour phase= 0.2105 \n", - "composition of vapour phase= 0.7895 \n", - "composition of last drop of liquid= 0.2941 \n", - "composition of last drop of liquid= 0.7059 \n" - ] - } - ], - "prompt_number": 1 - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "Example2-pg371" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "import math\t\n", - "#calculate pressure of the phase of pure A\n", - "##initialisation of variables\n", - "p0= 10. ##Mpa\n", - "R= 8.314 ##J/mol K\n", - "T= 30. ##C\n", - "va= 0.02 ##m^3/kmol\n", - "xa= 0.98\n", - "##CALCULATIONS\n", - "p= p0+(R*(273.15+T)*math.log(xa)/(va*1000.))\n", - "##RESULTS\n", - "print'%s %.2f %s'%('Pressure of the phase of pure A=',p,'Mpa')\n" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "Pressure of the phase of pure A= 7.45 Mpa\n" - ] - } - ], - "prompt_number": 3 - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "Example3-pg373" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "import math\n", - "#calculate the boiling point elevation\n", - "##initialisation of variables\n", - "hfg= 2257.0 ##kJ/kg\n", - "Tb= 100 ##C\n", - "R= 8.314 ##J/mol K\n", - "m2= 10 ##gms\n", - "M2= 58.5 ##gms\n", - "m1= 90. ##gms\n", - "M1= 18. ##gms\n", - "##CALCULATIONS\n", - "x2= (m2/M2)/((m2/M2)+(m1/M1))\n", - "dT= R*math.pow(273.15+Tb,2)*x2/(M1*hfg)\n", - "##RESULTS\n", - "print'%s %.3f %s'%(' Boiling point elevation=',dT,'C')\n" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - " Boiling point elevation= 0.942 C\n" - ] - } - ], - "prompt_number": 4 - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "Example4-pg376" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "import math\n", - "#calculate Osomatic pressures\n", - "##initialisation of variables\n", - "M1= 18.02 ##gms\n", - "m1= 0.965 ##gms\n", - "m2= 0.035 ##gms\n", - "M2= 58.5 ##gms\n", - "R= 8.314 ##J/mol K\n", - "M= 18.02 ##kg\n", - "T= 20. ##C\n", - "vf= 0.001002 ##m^3\n", - "x21= 0.021856 ##m^3\n", - "##CALCULATIONS\n", - "n1= m1/M1\n", - "n2= m2/M2\n", - "x1= n1/(n1+n2)\n", - "x2= n2/(n2+n1)\n", - "P= R*(273.15+T)*x2/(M*vf)\n", - "P1= R*(273.15+T)*x21/(M*vf)\n", - "##RESULTS\n", - "print'%s %.1f %s'%('Osmotic pressure=',P,'kpa')\n", - "print'%s %.1f %s'%('Osmotic pressure=',P1,'kpa')\n" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "Osmotic pressure= 1491.4 kpa\n", - "Osmotic pressure= 2950.2 kpa\n" - ] - } - ], - "prompt_number": 5 - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "Example5-pg377" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "import math\n", - "#what is useful work in the process and heat interaction and maximum work and irreversibility\n", - "##initialisation of variables\n", - "W= 0.\n", - "Q= 0.\n", - "R= 8.314 ##J/mol K\n", - "T0= 300. ##K\n", - "x= 5./13.\n", - "n1= 0.5 ##kmol/s\n", - "n2= 0.8 ##kmol/s\n", - "##CALCULATIONS\n", - "W1= (n1+n2)*R*T0*(x*math.log(1/x)+(1-x)*math.log(1/(1-x)))\n", - "I= W1\n", - "##RESULTS\n", - "print'%s %.f %s'%('useful work of the process=',W,'kW') \n", - "print'%s %.f %s'%('heat interaction=',Q,'kW') \n", - "print'%s %.1f %s'%('maximum work=',W1,'kW') \n", - "print'%s %.1f %s'%('irreversibility=',I,'kW')\n" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "useful work of the process= 0 kW\n", - "heat interaction= 0 kW\n", - "maximum work= 2160.4 kW\n", - "irreversibility= 2160.4 kW\n" - ] - } - ], - "prompt_number": 7 - } - ], - "metadata": {} - } - ] -} \ No newline at end of file -- cgit