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diff --git a/Chemical_Reaction_Engineering/ch19.ipynb b/Chemical_Reaction_Engineering/ch19.ipynb new file mode 100755 index 00000000..419b424a --- /dev/null +++ b/Chemical_Reaction_Engineering/ch19.ipynb @@ -0,0 +1,204 @@ +{ + "metadata": { + "name": "" + }, + "nbformat": 3, + "nbformat_minor": 0, + "worksheets": [ + { + "cells": [ + { + "cell_type": "heading", + "level": 1, + "metadata": {}, + "source": [ + "Chapter 19 : The Packed Bed Catalytic Reactor" + ] + }, + { + "cell_type": "heading", + "level": 2, + "metadata": {}, + "source": [ + "Example 19.1 page no : 438" + ] + }, + { + "cell_type": "code", + "collapsed": false, + "input": [ + "\n", + "%pylab inline\n", + "\n", + "from matplotlib.pyplot import *\n", + "\n", + "# Variables\n", + "Cp = 40. #J/mol.k\n", + "Hr = 80000. #J/mol.k\n", + "FAo = 100. #mol/s\n", + "nA = 1.\n", + "nB = 7.\n", + "n = nA + nB\n", + "T1 = 300. #k\n", + "T2 = 600. #k\n", + "T3 = 800. #k\n", + "\n", + "# Calculations\n", + "m = Cp/Hr;\n", + "XA = [0.8,0.78,0.7,0.66,0.5,0.26,0.1,0];\n", + "inv_rA = [20,10,5,4.4,5,10,20,33];\n", + "\n", + "\n", + "plot(XA,inv_rA)\n", + "xlabel(\"Xa\")\n", + "ylabel(\"1/8 X 1/-rA\")\n", + "\n", + "print ('From the plot we can say that a recycle reactor should be used')\n", + "W = FAo*38.4\n", + "R = 1.;\n", + "Q1 = n*FAo*Cp*(T2-T1);\n", + "Q2 = n*FAo*Cp*(T1-T3);\n", + "\n", + "# Results\n", + "print \" The weight of catalyst needed is %.f kg\"%(W)\n", + "print \" The Recycle Ratio is %.f\"%(R)\n", + "print \" The heat exchange for feed is %.f MW\"%(Q1/10**6)\n", + "print \" The heat excahnge for the product is %.f MW\"%(Q2/10**6)\n", + "show()\n" + ], + "language": "python", + "metadata": {}, + "outputs": [ + { + "output_type": "stream", + "stream": "stdout", + "text": [ + "Populating the interactive namespace from numpy and matplotlib\n", + "From the plot we can say that a recycle reactor should be used\n", + " The weight of catalyst needed is 3840 kg\n", + " The Recycle Ratio is 1\n", + " The heat exchange for feed is 10 MW\n", + " The heat excahnge for the product is -16 MW\n" + ] + }, + { + "output_type": "stream", + "stream": "stderr", + "text": [ + "WARNING: pylab import has clobbered these variables: ['draw_if_interactive']\n", + "`%pylab --no-import-all` prevents importing * from pylab and numpy\n" + ] + }, + { + "metadata": {}, + "output_type": "display_data", + "png": 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+ "text": [ + "<matplotlib.figure.Figure at 0x7ff34ba76ed0>" + ] + } + ], + "prompt_number": 4 + }, + { + "cell_type": "heading", + "level": 2, + "metadata": {}, + "source": [ + "Example 19.2 page no : 440" + ] + }, + { + "cell_type": "code", + "collapsed": false, + "input": [ + "\n", + "import math \n", + "from matplotlib.pyplot import *\n", + "\n", + "# Variables\n", + "Cp = 40.\n", + "Hr = 80000.\n", + "m = Cp/Hr;\n", + "FAo = 100. #mol/s\n", + "print ('We should use a mixed flow reactor operating at optimum')\n", + "\n", + "# Calculations and Results\n", + "XA = [0.85,0.785,0.715,0.66,0.58,0.46];\n", + "inv_rAopt = [20,10,5,3.6,2,1];\n", + "plot(XA,inv_rAopt)\n", + "\n", + "area1 = 0.66*3.6;\n", + "area2 = (0.85-0.66)*20;\n", + "W1 = FAo*area1;\n", + "W2 = FAo*area2;\n", + "print \" The weight of catalyst needed for 1st bed is %.1f kg\"%(W1)\n", + "print \" The weight of catalyst needed for 2ndbed is %.1f kg\"%(W2)\n", + "\n", + "#Heat exchange\n", + "#For the first reactor\n", + "Q = (820-300)*Cp+0.66*(-Hr);\n", + "\n", + "#For 100 mol/s\n", + "Q1 = FAo*Q/10**6;#MW\n", + "print \" The amount of heat exchanged for 1st reactor is %.2f MW\"%(Q1)\n", + "\n", + "#For 2nd reactor\n", + "#To go from XA = 0.66 at 820 k to XA = 0.85 at 750 k\n", + "Q2 = FAo*((750-820)*Cp+(0.85-0.66)*(-Hr));\n", + "Q2 = Q2/10**6;\n", + "print \" The amount of heat exchanged for 2nd reactor is %.2f MW\"%(Q2)\n", + "\n", + "#For the exchanger needed to cool the exit stream from 750 k to 300 k\n", + "Q3 = FAo*Cp*(300. - 750);\n", + "Q3 = Q3/10**6;#MW\n", + "print \" The amount of heat exchanged for exchanger is %.2f MW\"%(Q3)\n", + "\n", + "show()\n" + ], + "language": "python", + "metadata": {}, + "outputs": [ + { + "output_type": "stream", + "stream": "stdout", + "text": [ + "We should use a mixed flow reactor operating at optimum\n", + " The weight of catalyst needed for 1st bed is 237.6 kg" + ] + }, + { + "output_type": "stream", + "stream": "stdout", + "text": [ + "\n", + " The weight of catalyst needed for 2ndbed is 380.0 kg\n", + " The amount of heat exchanged for 1st reactor is -3.20 MW\n", + " The amount of heat exchanged for 2nd reactor is -1.80 MW\n", + " The amount of heat exchanged for exchanger is -1.80 MW\n" + ] + }, + { + "metadata": {}, + "output_type": "display_data", + "png": 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