{ "metadata": { "name": "", "signature": "sha256:c0b8814a6ac7ab401db03352df216c35ffd27c0ad0849fd68734e0e65b766ec4" }, "nbformat": 3, "nbformat_minor": 0, "worksheets": [ { "cells": [ { "cell_type": "heading", "level": 1, "metadata": {}, "source": [ "Chapter 4: Principles of Fluid Flow" ] }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 4.1 , Page no:172" ] }, { "cell_type": "code", "collapsed": false, "input": [ "import math\n", "from __future__ import division\n", "\n", "#Variable declaration\n", "L = 3 ; #Length\n", "D = 0.01 ; #ID\n", "V = 0.2 ; #Average Velocity\n", "rho =999.7 ; #kg /m^ 3\n", "\n", "#calculations\n", "v =1.306 * 10** -6 ; #m^2/ s\n", "ReD =0.2*0.01/(1.306*10** -6) ;\n", "f = 16/ ReD ;\n", "deltap = 4*f*(L/D)*( rho*V **2) /2;\n", "Vmax = 2*V;\n", "\n", "#result\n", "print\"Pressure drop is\",round(deltap,4),\"Pa\";\n", "print\"Maximum velocity is\",round(Vmax,3),\"m/s\";" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "Pressure drop is 250.6768 Pa\n", "Maximum velocity is 0.4 m/s\n" ] } ], "prompt_number": 1 }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 4.2(a) , Page no:180" ] }, { "cell_type": "code", "collapsed": false, "input": [ "import math\n", "from __future__ import division\n", "\n", "#Variable declaration\n", "L = 3 ; #m\n", "D = 0.01 ; #m\n", "V = 0.2 ;#m/ s\n", "rho = 971.8 ; #kg /m^ 3\n", "\n", "#calculations\n", "v = 0.365 * 10** -6 ; #m^2/ s\n", "ReD = D*V/v;\n", "f =0.079*( ReD )**( -0.25) ;\n", "deltap = (4*f*L* rho *V**2) /(D *2) ;\n", "x = ((f/2) **0.5) *V ;\n", "yplus = 0.005* x /(0.365*10** -6) ;\n", "Vmax = x *(2.5* math.log ( yplus ) + 5.5) ;\n", "ratio = Vmax /V;\n", "\n", "#result\n", "print\"(a) If the temperature of water is increased to 80 degree C\";\n", "print\"Pressure drop is\",round(deltap,4),\"Pa\";\n", "print\"Vmax =\",round(Vmax,4),\"m/s\";\n", "print\"Vmax/Vbar =\",round(ratio,4);" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "(a) If the temperature of water is increased to 80 degree C\n", "Pressure drop is 214.1563 Pa\n", "Vmax = 0.2515 m/s\n", "Vmax/Vbar = 1.2575\n" ] } ], "prompt_number": 2 }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 4.2(b) , Page no:180" ] }, { "cell_type": "code", "collapsed": false, "input": [ "import math\n", "from __future__ import division\n", "\n", "#Variable declaration\n", "L = 3 ; #m\n", "D = 0.01 ; #m\n", "V = 0.2 ; #m/s\n", "V1 =0.7;\n", "v1 = 1.306 * 10** -6 ; #m^2/ s\n", "V1 =0.7; #m/ s\n", "\n", "#calculations\n", "ReD1 =V1*D /(1.306*10** -6) ;\n", "f1 = 0.079*( ReD1 )**( -0.25) ;\n", "deltap1 = (4* f1*L *999.7*0.7**2) /(0.01*2) ;\n", "x1 = (( f1 /2)**0.5) *V1 ;\n", "y1plus = 0.005* x1 /( v1);\n", "Vmax1 = x1 *(2.5* math.log ( y1plus ) + 5.5) ;\n", "ratio1 = Vmax1 /V1;\n", "\n", "#result\n", "print\"(b) If the velocity is increased to 0.7 \";\n", "print\"Reynolds no is\",round(ReD1,4);\n", "print\"Pressure drop is\",round(deltap1,4),\"pa\";\n", "print\"y+ at centre line =\",round(y1plus,4);\n", "print\"Vmax is\",round(Vmax1,4),\"pa\";\n", "print\"Vmax/Vbar =\",round(ratio1,4);" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "(b) If the velocity is increased to 0.7 \n", "Reynolds no is 5359.8775\n", "Pressure drop is 2713.6598 pa\n", "y+ at centre line = 182.087\n", "Vmax is 0.8804 pa\n", "Vmax/Vbar = 1.2577\n" ] } ], "prompt_number": 3 }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 4.3 , Page no:181" ] }, { "cell_type": "code", "collapsed": false, "input": [ "import math\n", "from __future__ import division\n", "\n", "#Variable declaration\n", "P = 80 * 10**3 ; #Pa\n", "L = 10 ; #m\n", "Vbar = 1.9 ; #m/s\n", "l = 0.25 ; #m\n", "b = 0.15 ; #m\n", "rho = 1.185 ; #kg /m^ 3\n", "\n", "#calculations\n", "mew = 18.35 * 10** -6 ; #kg /m s\n", "rho1 = rho *(80/101.3) ; #kg /m^ 3\n", "r = b/l;\n", "De = (4* l/2*b /2) /(l/2 + b /2) ;\n", "Dl = (2/3 + 11/24*0.6*(2 -0.6)) * De ;\n", "Re = rho1 * Dl * Vbar / mew ;\n", "f = 0.079*( Re ** -0.25) ;\n", "deltaP = 4*f*(L/ Dl )*( rho1 *( Vbar **2) /2) ;\n", "power = deltaP *( Vbar *l*b)\n", "\n", "#result\n", "print\"Reynolds no =\",round(Re,4);\n", "print\"f =\",round(f,4);\n", "print\"Pressure drop =\",round(deltaP,4),\"Pa\";\n", "print\"Power required =\",round(power,4),\"W\";" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "Reynolds no = 19107.1453\n", "f = 0.0067\n", "Pressure drop = 2.3024 Pa\n", "Power required = 0.164 W\n" ] } ], "prompt_number": 4 }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 4.4 , Page no:189" ] }, { "cell_type": "code", "collapsed": false, "input": [ "import math\n", "from __future__ import division\n", "\n", "#Variable declaration\n", "l = 2 ; #m\n", "b = 1 ; #m\n", "V = 1 ; #m/s\n", "rho = 1.060 ; #kg /m^ 3\n", "x = 1.5 ; #m^2/s\n", "\n", "#calculations\n", "v = 18.97 * 10** -6 ;\n", "Re = V*x/v; #Reynolds number\n", "d = 5*x/( Re **(1/2) ) *1000 ;\n", "Rel = V*l/v;\n", "cf = 1.328* Rel** -(1/2) ; #drag coefficient\n", "Fd = 0.00409*(1/2) *rho *(2* l*b) *1**2;\n", "\n", "#result\n", "print\"Thickness of Boundary layer at x =1.5 is \",round(d,4),\"mm\"\n", "print\"Drag Coefficient cf =\",round(cf,5);\n", "print\"Drag Force FD =\",round(Fd,6),\"N\";" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "Thickness of Boundary layer at x =1.5 is 26.6716 mm\n", "Drag Coefficient cf = 0.00409\n", "Drag Force FD = 0.008671 N\n" ] } ], "prompt_number": 5 }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 4.5 , Page no:195" ] }, { "cell_type": "code", "collapsed": false, "input": [ "import math\n", "from __future__ import division\n", "\n", "#Variable declaration\n", "l = 2 ; #m\n", "v = 4 ; #m/s\n", "\n", "#calculations\n", "mew = 18.1*10** -6; #N s /m^ 2\n", "rho = 1.205*1.5; #kg /m^ 3\n", "Rel = rho*v*l/ mew ;\n", "Cf = 0.074*(7.989*10**5) **( -0.2) - 1050/ Rel ;\n", "Df = Cf *1/2* rho*l*v **2;\n", "x = 3*10**5 * (18.1*10** -6) /(1.808*4) ;\n", "\n", "#result\n", "print\"Drag coefficieent is\",round(Cf,6);\n", "print\"Drag force per meter width =\",round(Df,6),\"N\";\n", "print\"Value of xc is\",round(x,6),\"m\";" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "Drag coefficieent is 0.003569\n", "Drag force per meter width = 0.103221 N\n", "Value of xc is 0.75083 m\n" ] } ], "prompt_number": 6 } ], "metadata": {} } ] }