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Diffstat (limited to 'Chemical_Reaction_Engineering/ch4.ipynb')
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diff --git a/Chemical_Reaction_Engineering/ch4.ipynb b/Chemical_Reaction_Engineering/ch4.ipynb new file mode 100755 index 00000000..cd660b67 --- /dev/null +++ b/Chemical_Reaction_Engineering/ch4.ipynb @@ -0,0 +1,81 @@ +{ + "metadata": { + "name": "" + }, + "nbformat": 3, + "nbformat_minor": 0, + "worksheets": [ + { + "cells": [ + { + "cell_type": "heading", + "level": 1, + "metadata": {}, + "source": [ + "Chapter 4 : Introduction to Reactor Design" + ] + }, + { + "cell_type": "heading", + "level": 2, + "metadata": {}, + "source": [ + "Example 4.1 page no : 88" + ] + }, + { + "cell_type": "code", + "collapsed": false, + "input": [ + "\n", + "# Variables\n", + "a = 1.\n", + "b = 3.\n", + "c = 6.\n", + "#Initial concentrations\n", + "CAo = 100. # feed\n", + "CBo = 200. # feed\n", + "Cio = 100. # feed\n", + "#Final concentrations\n", + "CA = 40. # reacter exit\n", + "\n", + "# Calculations\n", + "# Find CB,XA,XB\n", + "ea = (6.-4.)/4;\n", + "XA = (CAo-CA)/(CAo+ea*CA);\n", + "eb = (ea*CBo)/(b*CAo);\n", + "XB = b*CAo*XA/CBo;\n", + "CB = CBo*(1-XB)/(1+eb*XB);\n", + "\n", + "# Results\n", + "print \"The final concentration of BCB is %.f\"%(CB)\n", + "print \" XA and XB are %.2f ,%.2f\"%(XA,XB)\n", + " \n" + ], + "language": "python", + "metadata": {}, + "outputs": [ + { + "output_type": "stream", + "stream": "stdout", + "text": [ + "The final concentration of BCB is 40\n", + " XA and XB are 0.50 ,0.75\n" + ] + } + ], + "prompt_number": 1 + }, + { + "cell_type": "code", + "collapsed": false, + "input": [], + "language": "python", + "metadata": {}, + "outputs": [] + } + ], + "metadata": {} + } + ] +}
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