{ "metadata": { "name": "" }, "nbformat": 3, "nbformat_minor": 0, "worksheets": [ { "cells": [ { "cell_type": "heading", "level": 1, "metadata": {}, "source": [ "Chapter 16 Earliness of Mixing, Segregation, and RTD" ] }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 16.1 pageno : 358" ] }, { "cell_type": "code", "collapsed": false, "input": [ "\n", "import math \n", "from scipy.integrate import quad \n", "\n", "# Variables\n", "Co = 1.\n", "k = 1.\n", "t = 1. #given\n", "\n", "# Calculations and Results\n", "C1 = (-1+math.sqrt(1-4*t*(-Co)))/2*t;\n", "#For the plug flow reactor\n", "#t = 1/k(1/C2-1/C1)\n", "C2 = C1/(1+k*t*C1);\n", "print \" Conversion for flow scheme A is %.3f\"%(C2)\n", "\n", "#For plug flow\n", "C3 = Co/(1+k*t*Co);\n", "#For mixed flow reactor\n", "C4 = (-1+math.sqrt(1-4*t*(-C3)))/2*t;\n", "print \" Conversion for flow scheme B is %.3f\"%(C4)\n", "\n", "#Using exit age distribution fn for 2 equal plug-mixed flow reactor system,umath.sing fig 12.1\n", "t_bar = 2.\n", "in_ = 1000.\n", "\n", "def f3(t): \n", "\t return (2/t_bar)*(math.exp(1-2*t/t_bar))/(1+Co*k*t)\n", "\n", "C5 = quad(f3,t_bar/2,in_)[0]\n", "\n", "print \" Conversion for flow scheme C,D,E is %.3f\"%(C5)\n", "\n" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ " Conversion for flow scheme A is 0.382\n", " Conversion for flow scheme B is 0.366\n", " Conversion for flow scheme C,D,E is 0.361" ] }, { "output_type": "stream", "stream": "stdout", "text": [ "\n" ] } ], "prompt_number": 1 }, { "cell_type": "code", "collapsed": false, "input": [], "language": "python", "metadata": {}, "outputs": [] } ], "metadata": {} } ] }