path: root/Fundamentals_of_Fluid_Mechanics/ch_3.ipynb

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  {
   "cells": [
    {
     "cell_type": "heading",
     "level": 1,
     "metadata": {},
     "source": [
      "Chapter 3 :Elementary fluid dynamics"
     ]
    },
    {
     "cell_type": "heading",
     "level": 3,
     "metadata": {},
     "source": [
      "Example 3.1 Page No.99"
     ]
    },
    {
     "cell_type": "code",
     "collapsed": false,
     "input": [
      "\n",
      "v1=100                            #mi/hr\n",
      "ht=10000                         #ft\n",
      "#from standard table for static pressure at an altitude\n",
      "p1=1456                        #lb/ft**2(abs)\n",
      "P1=1456*0.006947        #psi\n",
      "d=0.001756                   #slugs/ft**3\n",
      "#1 mi/hr = 1.467 ft/s \n",
      "\n",
      "#calculation\n",
      "p2=p1+(d*(v1*1.467)**2/2)          #lb/ft**3\n",
      "#in terms of gage pressure p2g\n",
      "p2g=p2-p1                                   #lb/ft**2\n",
      "#1lb/ft**2 = 0.006947 psi\n",
      "P2=p2*0.006947                         #psi\n",
      "P2g=p2g*0.006947#psi\n",
      "#pressure difference indicated by the pitot tube = pdiff\n",
      "pdiff=P2-P1                               #psi\n",
      "\n",
      "#Result\n",
      "print \"Pressure at point 1 =\",round(P1,2),\"psi\"\n",
      "print \"Pressure at point 2 in terms of gage pressure=\",round(P2g,2),\"psi\"\n",
      "print \"pressure difference indicated by the pitot static tube=\",round(pdiff,2),\"psi\"\n"
     ],
     "language": "python",
     "metadata": {},
     "outputs": [
      {
       "output_type": "stream",
       "stream": "stdout",
       "text": [
        "Pressure at point 1 = 10.11 psi\n",
        "Pressure at point 2 in terms of gage pressure= 0.13 psi\n",
        "pressure difference indicated by the pitot static tube= 0.13 psi\n"
       ]
      }
     ],
     "prompt_number": 1
    },
    {
     "cell_type": "heading",
     "level": 3,
     "metadata": {},
     "source": [
      "Example 3.7 Page No.115"
     ]
    },
    {
     "cell_type": "code",
     "collapsed": false,
     "input": [
      "%pylab inline"
     ],
     "language": "python",
     "metadata": {},
     "outputs": [
      {
       "output_type": "stream",
       "stream": "stdout",
       "text": [
        "\n",
        "Welcome to pylab, a matplotlib-based Python environment [backend: module://IPython.zmq.pylab.backend_inline].\n",
        "For more information, type 'help(pylab)'.\n"
       ]
      }
     ],
     "prompt_number": 3
    },
    {
     "cell_type": "code",
     "collapsed": false,
     "input": [
      "\n",
      "dia=0.1                             #m\n",
      "dia1=1.0                           #m\n",
      "h=2.0                               #m\n",
      "\n",
      "#calculation\n",
      "#bernoulli's equation: p1+(0.5*d*V1**2)+(sw*z1)= p2+(0.5*d*V2**2)+(sw*z2)\n",
      "#assuming p1=p2=0, and z1=h and z2=0\n",
      "#(0.5*d*V1**2)+(g*h)= (0.5*d*V2**2)\n",
      "#assuming steady flow Q1=Q2, Q=A*V. hence, A1*V1=A2*V2\n",
      "#V1=((dia/dia1)**2)*V2\n",
      "#hence V2=((2*g*h)/(1-(dia/dia1)**4))**0.5\n",
      "import math\n",
      "V2=((2*9.81*h)/(1-(dia/dia1)**4))**0.5\n",
      "Q=(math.pi/4*(dia)**2)*V2\n",
      "\n",
      "#result\n",
      "print \"The flow rate needed is=\",round(Q,5),\"m**3/s\"\n",
      "\n",
      "#Plot\n",
      "h=[0,0.2,0.4,0.5,0.6,0.62]\n",
      "D=[1,1.001,1.01,1.03,1.08,1.10]\n",
      "xlabel(\"d/D \") \n",
      "ylabel(\"Q/Q0\") \n",
      "plt.xlim((0,0.8))\n",
      "plt.ylim((1,1.10))\n",
      "a=plot(h,D)\n",
      "show(a)"
     ],
     "language": "python",
     "metadata": {},
     "outputs": [
      {
       "output_type": "stream",
       "stream": "stdout",
       "text": [
        "The flow rate needed is= 0.0492 m**3/s\n"
       ]
      },
      {
       "metadata": {},
       "output_type": "display_data",
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Fo34NtdVpo+S/Ll2p89tvv8WcOXOwceNGjBo1SokyXaqztrbW/l7u2rULsbGx\nsv4L05Uajx8/jrq6OtTV1SE9PR1r167FfffdJ1uNrtZ56tQp+3u5fft2REZGYsCAAaqrc/z48TCZ\nTGhpaUFTUxMOHTqEiRMnqq5OwDpnUFJSglmzZslan40rdd57773Yvn072tvbcfz4cTQ1NXUauuqS\n26fh3choNIqQkBARHBws1qxZI4QQ4o033hBvvPGG/Tl//OMfxciRI0VMTIw4evSoKuv84YcfxG23\n3SZuuOEGceONN4rAwEBx5swZ1dW5YMECodPp7Ev/xo0bJ3uNrtT50ksvifDwcBEVFSXmz58vKisr\nVVdjR4899phiS2ed1fn666+L8PBwMXbsWDFv3jxx+PBhVdYphBB/+9vfRGhoqEhKShKbNm1SbZ3r\n168XBoNBkfpsnNX5888/i0WLFono6Ggxbdo0sXPnTqevqdnDj4iISD6qHYYiIiL1YFgQEZFTDAsi\nInKKYUFERE4xLIh6IScnB6tXr7b/fPDgQfzud7+DyWTCsGHDEBMTg+DgYEydOlX2vgAid2JYEPXC\nlTsG7N69GzNmzABg3Zvns88+w+HDh5GRkYGHH34Yn332mRJlEvUaw4KomzZt2oSYmBgkJCTg22+/\n7XTtn//8J6ZMmdKpAXPIkCGYN28e5syZg1WrVsldLpFbMCyIuqGhoQHPPPMMdu3ahYKCAvsGd7Zr\n/fv3x9ChQ7v8tWlpafjyyy/lLJfIbTS9kSCR3IqLi5GSkoLhw4cDgH3LbAD46KOP7OfKd6WtrY0b\nXZJm8c6CqBtsu8h2paioCCkpKQ5/7Y4dO5zvv0OkUgwLom6YPn06PvroI5w6dQonTpzAxx9/DMC6\nSeSRI0cwduzYq37N2bNnUVBQgK1bt+Kpp56Su2Qit+AwFFE33HTTTcjNzcWMGTMwePBg+7DTp59+\niujoaPvzfHx8UFpaipiYGDQ3NyMoKAgFBQWdnkOkJdxIkMgNnnvuOYwePRoPPvig0qUQSYJhQURE\nTnHOgoiInGJYEBGRUwwLIiJyimFBREROMSyIiMgphgURETn1//Mag5geBe7+AAAAAElFTkSuQmCC\n"
      }
     ],
     "prompt_number": 4
    },
    {
     "cell_type": "heading",
     "level": 3,
     "metadata": {},
     "source": [
      "Example 3.8 Page No.116"
     ]
    },
    {
     "cell_type": "code",
     "collapsed": false,
     "input": [
      "\n",
      "dia=0.03          #m\n",
      "dia1=0.01        #m\n",
      "p=3                 #kPa(gage)\n",
      "\n",
      "#calculation\n",
      "#density of air d is found using standard temp and pressure conditions\n",
      "d=(p+101)*1000/((286.9)*(15+273))\n",
      "#applying Bernoulli's equation at points 1,2 and 3 p=p1\n",
      "import math\n",
      "v3=((2*p*1000)/d)**0.5\n",
      "Q=(math.pi)/4*(dia1**2)*v3\n",
      "#by continuity equation, A2*v2=A3*v3\n",
      "v2=((dia1/dia)**2)*v3\n",
      "p2=(p*1000)-(0.5*d*(v2**2))\n",
      "\n",
      "#Result\n",
      "print  \"Flowrate =\",round(Q,5),\"m**3/s\"\n",
      "print \"Pressure in the hose=\",round(p2,1),\"N/m**2\""
     ],
     "language": "python",
     "metadata": {},
     "outputs": [
      {
       "output_type": "stream",
       "stream": "stdout",
       "text": [
        "Flowrate = 0.00542 m**3/s\n",
        "Pressure in the hose= 2963.0 N/m**2\n"
       ]
      }
     ],
     "prompt_number": 5
    },
    {
     "cell_type": "heading",
     "level": 3,
     "metadata": {},
     "source": [
      "Example 3.10 Page No. 120"
     ]
    },
    {
     "cell_type": "code",
     "collapsed": false,
     "input": [
      "\n",
      "T=60                               #degree farenheit\n",
      "z1=5                               #ft\n",
      "atmp=14.7                      #psia\n",
      "#applying bernoulli equation at points 1,2 and 3\n",
      "z3=-5                            #ft\n",
      "v1=0                             #large tank\n",
      "p1=0                             #open tank\n",
      "p3=0                             #open jet\n",
      "#applying continuity equation A2*v2=A3*v3 A2=A3 so v2=v3\n",
      "\n",
      "#calculation\n",
      "v3=(2*32.2*(z1-z3))**0.5\n",
      "#vapor pressure of water at 60 degree farenheit = p2=0.256 psia\n",
      "p2=0.256\n",
      "z2=z1-((((p2-atmp)*144)+(0.5*1.94*v3**2))/62.4)\n",
      "\n",
      "#result\n",
      "print \"The maximum height over which \\n the water can be siphoned without cavitation occuring=\",round(z2,3),\"ft\""
     ],
     "language": "python",
     "metadata": {},
     "outputs": [
      {
       "output_type": "stream",
       "stream": "stdout",
       "text": [
        "The maximum height over which \n",
        " the water can be siphoned without cavitation occuring= 28.321 ft\n"
       ]
      }
     ],
     "prompt_number": 6
    },
    {
     "cell_type": "heading",
     "level": 3,
     "metadata": {},
     "source": [
      "Example 3.11 Page No.122"
     ]
    },
    {
     "cell_type": "code",
     "collapsed": false,
     "input": [
      "\n",
      "sg=0.85\n",
      "Q1=0.005                        #m**3/s\n",
      "Q2=0.05                         #m**3/s\n",
      "dia1=0.1                         #m\n",
      "dia2=0.06                        #m\n",
      "\n",
      "#calculation\n",
      "#A2/A1=dia2/dia1\n",
      "import math\n",
      "d=sg*1000\n",
      "Arat=(dia2/dia1)**2\n",
      "A2=math.pi/4*(dia2**2)\n",
      "pdiffs=(Q1**2)*d*(1-(Arat**2))/(2*1000*(A2**2))\n",
      "pdiffl=(Q2**2)*d*(1-(Arat**2))/(2*1000*(A2**2))\n",
      "print \"The pressure difference ranges from =\",round(pdiffs,3),\"kpa\"  \"to\" ,round(pdiffl,0),\"kpa\""
     ],
     "language": "python",
     "metadata": {},
     "outputs": [
      {
       "output_type": "stream",
       "stream": "stdout",
       "text": [
        "The pressure difference ranges from = 1.157 kpato 116.0 kpa\n"
       ]
      }
     ],
     "prompt_number": 7
    },
    {
     "cell_type": "heading",
     "level": 3,
     "metadata": {},
     "source": [
      "Example 3.12 Page No.124"
     ]
    },
    {
     "cell_type": "code",
     "collapsed": false,
     "input": [
      "\n",
      "z1=5                          #m\n",
      "a=0.8                        #m\n",
      "b=6                          #m\n",
      "Cc=0.61                 #since a/z1=ratio=0.16<0.2 Cc= contracction coefficient\n",
      "z2=Cc*a\n",
      "\n",
      "#calculation\n",
      "#Q/b=flowrate\n",
      "flowrate=z2*((2*9.81*(z1-z2))/(1-((z2/z1)**2)))**0.5\n",
      "#considering z1>>z2 and neglecting kinetic energy of the upstream fluid\n",
      "flowrate1=z2*(2*9.81*z1)**0.5\n",
      "#result\n",
      "print \"The flowrate per unit width=\",round(flowrate,2),\"m**2/s\"\n",
      "print \"The flowrate per unit width when we consider z1>>z2=\",round(flowrate1,1),\"m**2/s\"\n",
      "\n",
      "#Plot\n",
      "import matplotlib.pyplot as plt\n",
      "fig = plt.figure()\n",
      "ax = fig.add_subplot(111)\n",
      "\n",
      "h=[5,10,15]\n",
      "D=[4.61,6.5,8]\n",
      "xlabel(\"z1  (m)\") \n",
      "ylabel(\"Q/b (m**2/s)\") \n",
      "plt.xlim((0,15))\n",
      "plt.ylim((0,9))\n",
      "\n",
      "ax.plot([5], [4.61], 'o')\n",
      "ax.annotate('(5 m,4.61 m**2/s)', xy=(5,4.5))\n",
      "a=plot(h,D)\n",
      "show(a)"
     ],
     "language": "python",
     "metadata": {},
     "outputs": [
      {
       "output_type": "stream",
       "stream": "stdout",
       "text": [
        "The flowrate per unit width= 4.61 m**2/s\n",
        "The flowrate per unit width when we consider z1>>z2= 4.8 m**2/s\n"
       ]
      },
      {
       "metadata": {},
       "output_type": "display_data",
       "png": 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BQUFCCKH+vssfe2bixInilVdeEW5ubiIwMLDC10pLS4Wrq2uV1x87dqz49ddf66VXkh9t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\niEhGGOpERDLCUCcikpH/B3UDvsh3l9PbAAAAAElFTkSuQmCC\n"
      }
     ],
     "prompt_number": 8
    },
    {
     "cell_type": "heading",
     "level": 3,
     "metadata": {},
     "source": [
      "Example 3.13 Page No.125"
     ]
    },
    {
     "cell_type": "code",
     "collapsed": false,
     "input": [
      "\n",
      "Qrat=3**2.5\n",
      "\n",
      "#Result\n",
      "print(\"The flowrate is proportional to H**2.5\")\n",
      "print \"When depth is increased from H0 to 3H0 Q increases \",round(Qrat,1),\"times\"\n"
     ],
     "language": "python",
     "metadata": {},
     "outputs": [
      {
       "output_type": "stream",
       "stream": "stdout",
       "text": [
        "The flowrate is proportional to H**2.5\n",
        "When depth is increased from H0 to 3H0 Q increases  15.6 times\n"
       ]
      }
     ],
     "prompt_number": 9
    },
    {
     "cell_type": "heading",
     "level": 3,
     "metadata": {},
     "source": [
      "Example 3.15 Page No.130"
     ]
    },
    {
     "cell_type": "code",
     "collapsed": false,
     "input": [
      "\n",
      "h=10                       #Km\n",
      "#air is in a standard atmosphere\n",
      "p1=26.5                 #kPa\n",
      "T1=-49.9               #degree celcius\n",
      "d=0.414                #Kg/m**3\n",
      "k=1.4\n",
      "Ma1=0.82             #Mach\n",
      "#for incompressible flow,\n",
      "pdiff=(k*Ma1**2)/2*p1\n",
      "#for compressible isentropic flow, \n",
      "pdiff1=((1+((k-1)/2)*(Ma1**2))**(k/(k-1))-1)*p1\n",
      "\n",
      "#result\n",
      "print(\"Stagnation pressure on leading edge on the wing of the Boeing:\")\n",
      "print \"when flow is imcompressible =\",round(pdiff,1),\"kpa\"\n",
      "print \"when flow is compressible and isentropic =\",round(pdiff1,1),\"kpa\""
     ],
     "language": "python",
     "metadata": {},
     "outputs": [
      {
       "output_type": "stream",
       "stream": "stdout",
       "text": [
        "Stagnation pressure on leading edge on the wing of the Boeing:\n",
        "when flow is imcompressible = 12.5 kpa\n",
        "when flow is compressible and isentropic = 14.7 kpa\n"
       ]
      }
     ],
     "prompt_number": 10
    },
    {
     "cell_type": "heading",
     "level": 3,
     "metadata": {},
     "source": [
      "Example 3.17 Page No.132"
     ]
    },
    {
     "cell_type": "code",
     "collapsed": false,
     "input": [
      "\n",
      "V=5               #m/s\n",
      "sg=1.03\n",
      "h=50              #m\n",
      "#since static pressure is greater than stagnation pressure, Bernoulli's equation is incorrect\n",
      "#calculation\n",
      "#p2=(d*(V1**2)/2)+(d*g*h)  V1=V\n",
      "#result\n",
      "p2=(((sg*1000)*(V**2)/2) + (sg*1000*9.81*h))/1000  #kPa\n",
      "print \"The pressure at stagnation point 2 =\",round(p2,1),\"kpa\""
     ],
     "language": "python",
     "metadata": {},
     "outputs": [
      {
       "output_type": "stream",
       "stream": "stdout",
       "text": [
        "The pressure at stagnation point 2 = 518.1 kpa\n"
       ]
      }
     ],
     "prompt_number": 11
    }
   ],
   "metadata": {}
  }
 ]
}