{ "metadata": { "name": "" }, "nbformat": 3, "nbformat_minor": 0, "worksheets": [ { "cells": [ { "cell_type": "heading", "level": 1, "metadata": {}, "source": [ "Chapter 22 :\n", "\n", "G/L Reactions on Solid \n", "\n", "Catalysts: Trickle Beds, Slurry \n", "\n", "Reactors, and Three-Phase \n", "\n", "Fluidized Beds" ] }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 22.1 pageno : 511" ] }, { "cell_type": "code", "collapsed": false, "input": [ "import math \n", "\n", "# Variables\n", "PA = 101325. #Pa\n", "HA = 36845. #PA.m3.l/mol\n", "CBo = 1000. #mol/m3\n", "v = 10**-4 #m3*l/s\n", "h = 5. #m\n", "A = 0.1 #m2\n", "\n", "# Calculations\n", "CA = PA/HA;\n", "FBo = v*CBo;\n", "Vr = A*h;\n", "dp = 5*10**-3; #mcat\n", "d_solid = 4500. #kg/m3cat\n", "De = 8*10**-10; #m3l/mcat.s\n", "n = 0.5;\n", "b = 1.;\n", "k = 2.35*10**-3;\n", "L = dp/6.;\n", "kai_overall = 0.02;\n", "kac_ac = 0.05;\n", "f = 0.6;\n", "#For a half-order reaction\n", "Mt = L*math.sqrt((n+1)*(k*d_solid*(CA)**(n-1))/(2*De));\n", "E = 1/Mt;\n", "rA = (1/((1/(kai_overall))+(1/(kac_ac))+(1/(k*b*(CA**(n-1))*E*f*d_solid))))*(PA/HA);\n", "#From Material Balance\n", "XB = b*rA*Vr/FBo;\n", "\n", "# Results\n", "print \" The conversion of acetone is %.3f\"%(XB)\n" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ " The conversion of acetone is 0.158\n" ] } ], "prompt_number": 2 }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 22.2 pageno : 513" ] }, { "cell_type": "code", "collapsed": false, "input": [ "%matplotlib inline\n", "\n", "import math \n", "from matplotlib.pyplot import *\n", "from numpy import *\n", "\n", "# Variables\n", "PA = 14.6*101325; #Pa\n", "HA = 148000.; # liquid\n", "Vr = 2.;\n", "Vl = Vr;\n", "b = 1.;\n", "fs = 0.0055;\n", "\n", "# Calculations\n", "k = 5.*10**-5; #m6l/kg.molcat.s\n", "dp = 5*10**-5; #mcat\n", "kac = 4.4*10**-4;kai = 0.277; #m3l/m3.r.s\n", "density = 1450.; #kg/m3\n", "De = 5*10**-10; #m3l/mcat.s\n", "L = dp/6; #for spherical particle\n", "CA = PA/HA;\n", "X = 0.9;\n", "CBo = 2500.\n", "CB = CBo*(1-X);\n", "ac = 6*fs/dp;\n", "K = kac*ac;\n", "\n", "CB = [2500,1000,250];\n", "e = [0.19,0.29,0.5];\n", "Mt = zeros(3)\n", "rA = zeros(3)\n", "inv_rA = zeros(3)\n", "for i in range(3):\n", " Mt[i] = L*math.sqrt(k*CB[i]*density/De);\n", " rA[i] = CA/((1./kai)+(1./K)+(1./(k*density*e[i]*fs*CB[i])))\n", " inv_rA[i] = 1/rA[i];\n", "\n", "# Results\n", "plot(CB,inv_rA)\n", "ylabel(\"1/-rA\")\n", "Area = 3460.\n", "t = Vl*Area/(b*Vr);\n", "t = t/60. #min\n", "print \" The time required for 90 percentage conversion of reactant is %.f\"%t,\n", "print \"min\"\n", "show()\n" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "Populating the interactive namespace from numpy and matplotlib\n", " The time required for 90 percentage conversion of reactant is 58" ] }, { "output_type": "stream", "stream": "stdout", "text": [ " min\n" ] }, { "output_type": "stream", "stream": "stderr", "text": [ "WARNING: pylab import has clobbered these variables: ['draw_if_interactive', 'e']\n", "`%pylab --no-import-all` prevents importing * from pylab and numpy\n" ] }, { "metadata": {}, "output_type": "display_data", "png": 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