{ "metadata": { "name": "", "signature": "sha256:2221589d3a230bd5e1c3d095a5ede0c1e2f30a613887d893f353723197c86dd5" }, "nbformat": 3, "nbformat_minor": 0, "worksheets": [ { "cells": [ { "cell_type": "heading", "level": 1, "metadata": {}, "source": [ "Chapter 7 : Flow Through Packed Beds\n" ] }, { "cell_type": "heading", "level": 3, "metadata": {}, "source": [ "\n", "example 7.1 page no : 136" ] }, { "cell_type": "code", "collapsed": false, "input": [ "\n", "\n", "import math \n", "\n", "# Initialization of Variable\n", "mu = 1.83/1000\n", "rhom = 1.355*10000 #density mercury\n", "K = 5.\n", "g = 9.81\n", "d = 2.5/100\n", "pi = 3.14\n", "thik = 2.73/100\n", "rho = 3100. #density of particles\n", "Q = 250./(12.*60+54)/10.**6\n", "\n", "#calculation\n", "A = pi*d**2./4.\n", "Vb = A*thik #volume of bed\n", "Vp = 25.4/rho/1000 #volume of particles\n", "e = 1-Vp/Vb\n", "u = Q/A\n", "delP = 12.5/100*rhom*g\n", "S = math.sqrt(e**3*delP/K/u/thik/mu/(1-e)**2)\n", "S = round(S/1000)*1000.\n", "d = 6./S\n", "print \"average particle diameter in (x10**-6m) %.4f\"%(d*10**6)\n", "A = pi*d**2./1000/(4./3*pi*d**3/8*rho)\n", "print \"surface area per gram of cement (cm**2): %.4f\"%(A*10**4)\n", "\n" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "average particle diameter in (x10**-6m) 47.6190\n", "surface area per gram of cement (cm**2): 406.4516\n" ] } ], "prompt_number": 1 }, { "cell_type": "heading", "level": 3, "metadata": {}, "source": [ "example 7.2 page no : 138" ] }, { "cell_type": "code", "collapsed": false, "input": [ "\n", "\n", "import math \n", "\n", "# Initialization of Variable\n", "mu = 2.5/1000\n", "rho = 897.\n", "g = 9.81\n", "pi = 3.1414\n", "K = 5.1\n", "l = 6.35/1000\n", "d = l\n", "hei = 24.5+0.65\n", "len = 24.5\n", "dc = 2.65 #dia of column\n", "thik = 0.76/1000\n", "Vs = pi*d**2/4*l-pi*l/4*(d-2*thik)**2 #volume of each ring\n", "n = 3.023*10**6\n", "e = 1-Vs*n\n", "e = round(e*1000)/1000.\n", "Surfacearea = pi*d*l+2*pi*d**2/4+pi*(d-2*thik)*l-2*pi*(d-2*thik)**2/4\n", "S = Surfacearea/Vs\n", "S = round(S)\n", "delP = hei*g*rho\n", "delP = round(delP/100.)*100.\n", "u = e**3*delP/K/S**2/mu/(1-e)**2/len\n", "Q = pi*dc**2/4*u\n", "print \"initial volumetric flow rate in (m**3/s): %.4f\"%Q\n" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "initial volumetric flow rate in (m**3/s): 2.8271\n" ] } ], "prompt_number": 2 }, { "cell_type": "heading", "level": 3, "metadata": {}, "source": [ "example 7.3 page no : 140" ] }, { "cell_type": "code", "collapsed": false, "input": [ "\n", "\n", "import math \n", "\n", "# Initialization of Variable\n", "dr = 2. #dia of column\n", "mu = 2.02/10**5\n", "rho = 998.\n", "K = 5.1\n", "g = 9.81\n", "Q = 10000./3600\n", "l = 50.8/1000\n", "d = l\n", "n = 5790.\n", "len = 18.\n", "thik = 6.35/1000\n", "pi = 3.1414\n", "\n", "#part1\n", "#calculation\n", "\n", "CA = pi*dr**2./4 #cross sectional area\n", "u = Q/CA\n", "Vs = pi*d**2/4*l-pi*l/4*(d-2*thik)**2 #volume of each ring\n", "e = 1-Vs*n\n", "Surfacearea = pi*d*l+2*pi*d**2/4+pi*(d-2*thik)*l-2*pi*(d-2*thik)**2/4\n", "S = Surfacearea/Vs\n", "S = round(S*10)/10.\n", "delP = K*S**2/e**3*mu*len*u*(1-e)**2\n", "delh = delP/rho/g\n", "print \"pressure drop in terms of (cm of H20) %.4f\"%(delh*100)\n", "\n" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "pressure drop in terms of (cm of H20) 0.3540\n" ] } ], "prompt_number": 3 }, { "cell_type": "code", "collapsed": false, "input": [], "language": "python", "metadata": {}, "outputs": [] } ], "metadata": {} } ] }