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authordebashisdeb2014-06-20 15:42:42 +0530
committerdebashisdeb2014-06-20 15:42:42 +0530
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treef54eab21dd3d725d64a495fcd47c00d37abed004 /Industrial_Instrumentation/Chapter_5.ipynb
parenta78126bbe4443e9526a64df9d8245c4af8843044 (diff)
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removing problem statements
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--- a/Industrial_Instrumentation/Chapter_5.ipynb
+++ b/Industrial_Instrumentation/Chapter_5.ipynb
@@ -1,874 +1,918 @@
{
"metadata": {
- "name": "Chapter_5"
- },
- "nbformat": 2,
+ "name": "",
+ "signature": "sha256:6f1ee33190d8c693b6015349dc3ea8fa65731657e9afb9deaa10542a8aa4bde7"
+ },
+ "nbformat": 3,
+ "nbformat_minor": 0,
"worksheets": [
{
"cells": [
{
- "cell_type": "markdown",
+ "cell_type": "markdown",
+ "metadata": {},
"source": [
"<h1>Chapter 5: Flow <h1>"
]
- },
+ },
{
- "cell_type": "markdown",
+ "cell_type": "markdown",
+ "metadata": {},
"source": [
"<h3>Example 5.1, Page Number: 310<h3>"
]
- },
+ },
{
- "cell_type": "code",
- "collapsed": false,
+ "cell_type": "code",
+ "collapsed": false,
"input": [
- "'''flow rate calulation'''",
- "",
- "import math",
- "#(i)",
- "",
- "#variable declaration",
- "d=75.0*10**-3 # diameter of pipe",
- "a=math.pi*d**2/4 # area of cross section of pipe",
- "v=760.0*10**-3 # flow velocity",
- "",
- "#calculation",
- "Q=v*a",
- "Q=Q*10**3",
- "print('(i)\\nVolume Flow Rate Q=%.3f *10^-3 m^3/sec' %Q)",
- "rho=1000.0",
- "W=rho*Q*10**-3",
- "",
- "#result",
+ "\n",
+ "\n",
+ "import math\n",
+ "#(i)\n",
+ "\n",
+ "#variable declaration\n",
+ "d=75.0*10**-3 # diameter of pipe\n",
+ "a=math.pi*d**2/4 # area of cross section of pipe\n",
+ "v=760.0*10**-3 # flow velocity\n",
+ "\n",
+ "#calculation\n",
+ "Q=v*a\n",
+ "Q=Q*10**3\n",
+ "print('(i)\\nVolume Flow Rate Q=%.3f *10^-3 m^3/sec' %Q)\n",
+ "rho=1000.0\n",
+ "W=rho*Q*10**-3\n",
+ "\n",
+ "#result\n",
"print('\\n(ii)\\nMass Flow rate W=%.3f kg/sec' %W)"
- ],
- "language": "python",
+ ],
+ "language": "python",
+ "metadata": {},
"outputs": [
{
- "output_type": "stream",
- "stream": "stdout",
+ "output_type": "stream",
+ "stream": "stdout",
"text": [
- "(i)",
- "Volume Flow Rate Q=3.358 *10^-3 m^3/sec",
- "",
- "(ii)",
+ "(i)\n",
+ "Volume Flow Rate Q=3.358 *10^-3 m^3/sec\n",
+ "\n",
+ "(ii)\n",
"Mass Flow rate W=3.358 kg/sec"
]
}
- ],
+ ],
"prompt_number": 1
- },
+ },
{
- "cell_type": "markdown",
+ "cell_type": "markdown",
+ "metadata": {},
"source": [
"<h3>Example 5.2, page Number:310<h3>"
]
- },
+ },
{
- "cell_type": "code",
- "collapsed": false,
+ "cell_type": "code",
+ "collapsed": false,
"input": [
- "'''Volumetric flow rate calculation'''",
- "",
- "import math",
- "",
- "#variable declaration",
- "D=40.0 # Diameter of pipe",
- "d=20.0 # Diameter of Orifice",
- "mr=15.0 # Manometer reading",
- "",
- "#calculation",
- "h=(13.6-1)*15.0*10.0",
- "B=d/D",
- "M=1/math.sqrt(1-(B**4))",
- "Cd=0.5999",
- "x=math.sqrt(2*9.8*h*(10**-3))",
- "Q=x*Cd*M*(math.pi*((20*(10**-3))**2))/4",
- "Q=Q*3600.0",
- "",
- "#result",
- "print('Volumetric flow rate Q= %.4f m^3/hr' %Q)",
- "#Answer slightly deviates from answer given in the book because of pi value.",
+ "\n",
+ "\n",
+ "import math\n",
+ "\n",
+ "#variable declaration\n",
+ "D=40.0 # Diameter of pipe\n",
+ "d=20.0 # Diameter of Orifice\n",
+ "mr=15.0 # Manometer reading\n",
+ "\n",
+ "#calculation\n",
+ "h=(13.6-1)*15.0*10.0\n",
+ "B=d/D\n",
+ "M=1/math.sqrt(1-(B**4))\n",
+ "Cd=0.5999\n",
+ "x=math.sqrt(2*9.8*h*(10**-3))\n",
+ "Q=x*Cd*M*(math.pi*((20*(10**-3))**2))/4\n",
+ "Q=Q*3600.0\n",
+ "\n",
+ "#result\n",
+ "print('Volumetric flow rate Q= %.4f m^3/hr' %Q)\n",
+ "#Answer slightly deviates from answer given in the book because of pi value.\n",
"#if pi=3.14, then answer is same as in textbook "
- ],
- "language": "python",
+ ],
+ "language": "python",
+ "metadata": {},
"outputs": [
{
- "output_type": "stream",
- "stream": "stdout",
+ "output_type": "stream",
+ "stream": "stdout",
"text": [
"Volumetric flow rate Q= 4.2649 m^3/hr"
]
}
- ],
+ ],
"prompt_number": 2
- },
+ },
{
- "cell_type": "markdown",
+ "cell_type": "markdown",
+ "metadata": {},
"source": [
"<h3>Example 5.3, Page Number: 310<h3>"
]
- },
+ },
{
- "cell_type": "code",
- "collapsed": false,
+ "cell_type": "code",
+ "collapsed": false,
"input": [
- "'''Nominal flow velocity'''",
- "",
- "import math",
- "#variable declaration",
- "Re=10.0**5 # Reynolds number",
- "D=40.0*10**-3 # Diameter of pipe ",
- "v=10**-6 # Kinematic viscosity in m^2/sec",
- "",
- "#calculation",
- "V1=Re*v/D",
- "A1=(math.pi*(40.0*10**-3)**2)/4",
- "A2=(math.pi*(20.0*10**-3)**2)/4",
- "V2=V1*A1/A2",
- "",
- "#result",
+ "\n",
+ "\n",
+ "import math\n",
+ "#variable declaration\n",
+ "Re=10.0**5 # Reynolds number\n",
+ "D=40.0*10**-3 # Diameter of pipe \n",
+ "v=10**-6 # Kinematic viscosity in m^2/sec\n",
+ "\n",
+ "#calculation\n",
+ "V1=Re*v/D\n",
+ "A1=(math.pi*(40.0*10**-3)**2)/4\n",
+ "A2=(math.pi*(20.0*10**-3)**2)/4\n",
+ "V2=V1*A1/A2\n",
+ "\n",
+ "#result\n",
"print('V2=%.1f m/sec' %V2)"
- ],
- "language": "python",
+ ],
+ "language": "python",
+ "metadata": {},
"outputs": [
{
- "output_type": "stream",
- "stream": "stdout",
+ "output_type": "stream",
+ "stream": "stdout",
"text": [
"V2=10.0 m/sec"
]
}
- ],
+ ],
"prompt_number": 3
- },
+ },
{
- "cell_type": "markdown",
+ "cell_type": "markdown",
+ "metadata": {},
"source": [
"<h3>Example 5.4, Page Number: 311<h3>"
]
- },
+ },
{
- "cell_type": "code",
- "collapsed": false,
+ "cell_type": "code",
+ "collapsed": false,
"input": [
- "'''pressure difference calculation'''",
- "",
- "import math",
- "",
- "#variable declaration",
- "Cd=0.61 # discharge coefficient",
- "D=40.0*10**-3 # Diameter of pipe",
- "d=20.0*10**-3 # Diameter of Orifice ",
- "",
- "#calculation",
- "M=1/math.sqrt(1-(d/D)**4)",
- "V2=10.0",
- "rho=1000.0",
- "g=9.8",
- "X=V2*math.sqrt(rho/(2*g))/(Cd*M)",
- "p_diff=X**2",
- "p_diff=math.floor(p_diff/100)",
- "p_diff=p_diff/100.0",
- "",
- "",
- "#result",
+ "\n",
+ "\n",
+ "import math\n",
+ "\n",
+ "#variable declaration\n",
+ "Cd=0.61 # discharge coefficient\n",
+ "D=40.0*10**-3 # Diameter of pipe\n",
+ "d=20.0*10**-3 # Diameter of Orifice \n",
+ "\n",
+ "#calculation\n",
+ "M=1/math.sqrt(1-(d/D)**4)\n",
+ "V2=10.0\n",
+ "rho=1000.0\n",
+ "g=9.8\n",
+ "X=V2*math.sqrt(rho/(2*g))/(Cd*M)\n",
+ "p_diff=X**2\n",
+ "p_diff=math.floor(p_diff/100)\n",
+ "p_diff=p_diff/100.0\n",
+ "\n",
+ "\n",
+ "#result\n",
"print('P1-P2 = %.2f kg/cm^2'%p_diff)"
- ],
- "language": "python",
+ ],
+ "language": "python",
+ "metadata": {},
"outputs": [
{
- "output_type": "stream",
- "stream": "stdout",
+ "output_type": "stream",
+ "stream": "stdout",
"text": [
"P1-P2 = 1.28 kg/cm^2"
]
}
- ],
+ ],
"prompt_number": 4
- },
+ },
{
- "cell_type": "markdown",
+ "cell_type": "markdown",
+ "metadata": {},
"source": [
"<h3>Example 5.5, Page Number: 312<h3>"
]
- },
+ },
{
- "cell_type": "code",
- "collapsed": false,
+ "cell_type": "code",
+ "collapsed": false,
"input": [
- "'''volume flow rate for orifice and venturi Tubes'''",
- "",
- "import math",
- "",
- "#variable declaration",
- "Cd=0.6 # discharge coefficient",
- "D=150.0*10**-3 # Diameter of pipe",
- "d=75.0*10**-3 # Diameter of Orifice ",
- "p=250.0 # pressure recorded",
- "g=9.8 # acceleration due to gravity",
- "rho=1000.0 # Water density ",
- "s=75.0*10**-3 # venturi tube size",
- "",
- "#(a)",
- "",
- "#calculation",
- "Q=Cd*math.pi*s**2*math.sqrt(2*g*p/rho)/(4*math.sqrt(1-(d/D)**4)) ",
- "",
- "#result",
- "print('(a) For orifice plate\\nQ=%f m^3/sec = %.3f litres/sec'%(Q,Q*1000))",
- "",
- "#calculation",
- "Cd1=0.99",
- "Q2=Cd1*math.pi*s**2*math.sqrt(2*g*p/rho)/(4*math.sqrt(1-(d/D)**4))",
- "",
- "#result",
- "print('\\n\\n(b)For venturi tube\\nQ=%f m^3/sec = %.2f litres/sec'%(Q2,Q2*1000))",
- "#Answer slightly deviates from answer given in the book because of pi value.",
+ "\n",
+ "\n",
+ "import math\n",
+ "\n",
+ "#variable declaration\n",
+ "Cd=0.6 # discharge coefficient\n",
+ "D=150.0*10**-3 # Diameter of pipe\n",
+ "d=75.0*10**-3 # Diameter of Orifice \n",
+ "p=250.0 # pressure recorded\n",
+ "g=9.8 # acceleration due to gravity\n",
+ "rho=1000.0 # Water density \n",
+ "s=75.0*10**-3 # venturi tube size\n",
+ "\n",
+ "#(a)\n",
+ "\n",
+ "#calculation\n",
+ "Q=Cd*math.pi*s**2*math.sqrt(2*g*p/rho)/(4*math.sqrt(1-(d/D)**4)) \n",
+ "\n",
+ "#result\n",
+ "print('(a) For orifice plate\\nQ=%f m^3/sec = %.3f litres/sec'%(Q,Q*1000))\n",
+ "\n",
+ "#calculation\n",
+ "Cd1=0.99\n",
+ "Q2=Cd1*math.pi*s**2*math.sqrt(2*g*p/rho)/(4*math.sqrt(1-(d/D)**4))\n",
+ "\n",
+ "#result\n",
+ "print('\\n\\n(b)For venturi tube\\nQ=%f m^3/sec = %.2f litres/sec'%(Q2,Q2*1000))\n",
+ "#Answer slightly deviates from answer given in the book because of pi value.\n",
"#if pi=3.14, then answer is same as in textbook "
- ],
- "language": "python",
+ ],
+ "language": "python",
+ "metadata": {},
"outputs": [
{
- "output_type": "stream",
- "stream": "stdout",
+ "output_type": "stream",
+ "stream": "stdout",
"text": [
- "(a) For orifice plate",
- "Q=0.006060 m^3/sec = 6.060 litres/sec",
- "",
- "",
- "(b)For venturi tube",
+ "(a) For orifice plate\n",
+ "Q=0.006060 m^3/sec = 6.060 litres/sec\n",
+ "\n",
+ "\n",
+ "(b)For venturi tube\n",
"Q=0.009999 m^3/sec = 10.00 litres/sec"
]
}
- ],
+ ],
"prompt_number": 5
- },
+ },
{
- "cell_type": "markdown",
+ "cell_type": "markdown",
+ "metadata": {},
"source": [
"<h3>Example 5.6, Page Number: 312<h3>"
]
- },
+ },
{
- "cell_type": "code",
- "collapsed": false,
+ "cell_type": "code",
+ "collapsed": false,
"input": [
- "'''determination of Reynolds number'''",
- "",
- "import math",
- "",
- "#(i)",
- "",
- "#variable declaration",
- "V=0.02 # volumetric flow rate",
- "d=10*10**-2 # Diameter of pipe",
- "",
- "#calculation",
- "A=math.pi*d**2/4",
- "v=V/A",
- "rho=1000.0",
- "Re=rho*v*d/10**-3",
- "Re=Re/100000.0",
- "",
- "#result",
- "print('(i)\\nReynolds number(Re) = %.3f * 10^5'%Re)",
- "",
- "#(ii)",
- "",
- "#variable declaration",
- "Cd=0.98 # discharge coefficient ",
- "D=20*10**-2 # Diameter of pipe ",
- "d=10*10**-2 # Diameter of orifice",
- "",
- "#calculation",
- "M=1/math.sqrt(1-(d/D)**4)",
- "a2=math.pi*d**2/4",
- "Q=0.02",
- "g=9.8",
- "X=Q*math.sqrt(rho)/(M*Cd*a2*math.sqrt(2*g))",
- "p_diff=math.ceil(X**2)",
- "",
- "#result",
- "print('\\n(ii)\\nPressur_difference = %d kg/m^2 = %.4f kg/cm^2'%(p_diff,p_diff/10000))",
- "#Answer slightly deviates from answer given in the book because of pi value.",
+ "\n",
+ "\n",
+ "import math\n",
+ "\n",
+ "#(i)\n",
+ "\n",
+ "#variable declaration\n",
+ "V=0.02 # volumetric flow rate\n",
+ "d=10*10**-2 # Diameter of pipe\n",
+ "\n",
+ "#calculation\n",
+ "A=math.pi*d**2/4\n",
+ "v=V/A\n",
+ "rho=1000.0\n",
+ "Re=rho*v*d/10**-3\n",
+ "Re=Re/100000.0\n",
+ "\n",
+ "#result\n",
+ "print('(i)\\nReynolds number(Re) = %.3f * 10^5'%Re)\n",
+ "\n",
+ "#(ii)\n",
+ "\n",
+ "#variable declaration\n",
+ "Cd=0.98 # discharge coefficient \n",
+ "D=20*10**-2 # Diameter of pipe \n",
+ "d=10*10**-2 # Diameter of orifice\n",
+ "\n",
+ "#calculation\n",
+ "M=1/math.sqrt(1-(d/D)**4)\n",
+ "a2=math.pi*d**2/4\n",
+ "Q=0.02\n",
+ "g=9.8\n",
+ "X=Q*math.sqrt(rho)/(M*Cd*a2*math.sqrt(2*g))\n",
+ "p_diff=math.ceil(X**2)\n",
+ "\n",
+ "#result\n",
+ "print('\\n(ii)\\nPressur_difference = %d kg/m^2 = %.4f kg/cm^2'%(p_diff,p_diff/10000))\n",
+ "#Answer slightly deviates from answer given in the book because of pi value.\n",
"#if pi=3.14, then answer is same as in textbook "
- ],
- "language": "python",
+ ],
+ "language": "python",
+ "metadata": {},
"outputs": [
{
- "output_type": "stream",
- "stream": "stdout",
+ "output_type": "stream",
+ "stream": "stdout",
"text": [
- "(i)",
- "Reynolds number(Re) = 2.546 * 10^5",
- "",
- "(ii)",
+ "(i)\n",
+ "Reynolds number(Re) = 2.546 * 10^5\n",
+ "\n",
+ "(ii)\n",
"Pressur_difference = 323 kg/m^2 = 0.0323 kg/cm^2"
]
}
- ],
+ ],
"prompt_number": 6
- },
+ },
{
- "cell_type": "markdown",
+ "cell_type": "markdown",
+ "metadata": {},
"source": [
"<h3>Example 5.7, Page Number: 313<h3>"
]
- },
+ },
{
- "cell_type": "code",
- "collapsed": false,
+ "cell_type": "code",
+ "collapsed": false,
"input": [
- "'''Fluid velocity and Volumetric flow rate'''",
- "",
- "import math",
- "",
- "#1kg/m^2=10 meters water head",
- "",
- "#variable declaration",
- "g=9.81 #acceleration due to gravity",
- "h=20.0 #height",
- "",
- "#calculation",
- "v=math.sqrt(2*g*h)",
- "d=300.0*10**-3",
- "A=(math.pi*d**2)/4",
- "A=math.floor(A*1000)",
- "A=A/1000.0",
- "Q=A*v",
- "",
- "#result",
+ "\n",
+ "\n",
+ "import math\n",
+ "\n",
+ "#1kg/m^2=10 meters water head\n",
+ "\n",
+ "#variable declaration\n",
+ "g=9.81 #acceleration due to gravity\n",
+ "h=20.0 #height\n",
+ "\n",
+ "#calculation\n",
+ "v=math.sqrt(2*g*h)\n",
+ "d=300.0*10**-3\n",
+ "A=(math.pi*d**2)/4\n",
+ "A=math.floor(A*1000)\n",
+ "A=A/1000.0\n",
+ "Q=A*v\n",
+ "\n",
+ "#result\n",
"print('Q = %.3f m^3/sec'%Q)"
- ],
- "language": "python",
+ ],
+ "language": "python",
+ "metadata": {},
"outputs": [
{
- "output_type": "stream",
- "stream": "stdout",
+ "output_type": "stream",
+ "stream": "stdout",
"text": [
"Q = 1.387 m^3/sec"
]
}
- ],
+ ],
"prompt_number": 7
- },
+ },
{
- "cell_type": "markdown",
+ "cell_type": "markdown",
+ "metadata": {},
"source": [
"<h3>Example 5.8, Page Number:313<h3>"
]
- },
+ },
{
- "cell_type": "code",
- "collapsed": false,
+ "cell_type": "code",
+ "collapsed": false,
"input": [
- "'''Fluid velocity calculation'''",
- "",
- "import math",
- "",
- "#variable declaration",
- "Cd=0.6 # coefficient of discharge ",
- "g=9.8 #acceleration due to gravity",
- "h=400*10**-3 #height",
- "",
- "#calculation",
- "V=Cd*math.sqrt(2*g*h)",
- "",
- "#result",
+ "\n",
+ "\n",
+ "import math\n",
+ "\n",
+ "#variable declaration\n",
+ "Cd=0.6 # coefficient of discharge \n",
+ "g=9.8 #acceleration due to gravity\n",
+ "h=400*10**-3 #height\n",
+ "\n",
+ "#calculation\n",
+ "V=Cd*math.sqrt(2*g*h)\n",
+ "\n",
+ "#result\n",
"print('V = %.2f m/sec' %V)"
- ],
- "language": "python",
+ ],
+ "language": "python",
+ "metadata": {},
"outputs": [
{
- "output_type": "stream",
- "stream": "stdout",
+ "output_type": "stream",
+ "stream": "stdout",
"text": [
"V = 1.68 m/sec"
]
}
- ],
+ ],
"prompt_number": 8
- },
+ },
{
- "cell_type": "markdown",
+ "cell_type": "markdown",
+ "metadata": {},
"source": [
"<h3>Example 5.9, Page Number: 314<h3>"
]
- },
+ },
{
- "cell_type": "code",
- "collapsed": false,
+ "cell_type": "code",
+ "collapsed": false,
"input": [
- "'''velocity measurement using pilot tube'''",
- "",
- "import math",
- "",
- "#variable declaration",
- "Cd=0.98 # coefficient of discharge",
- "g=9.8 #acceleration due to gravity",
- "h=900.0*10**-3 #height",
- "",
- "#calculation",
- "V=Cd*math.sqrt(2*g*h)",
- "V=math.floor(V*100)",
- "V=(V/100.0)",
- "",
- "#result",
+ "\n",
+ "\n",
+ "import math\n",
+ "\n",
+ "#variable declaration\n",
+ "Cd=0.98 # coefficient of discharge\n",
+ "g=9.8 #acceleration due to gravity\n",
+ "h=900.0*10**-3 #height\n",
+ "\n",
+ "#calculation\n",
+ "V=Cd*math.sqrt(2*g*h)\n",
+ "V=math.floor(V*100)\n",
+ "V=(V/100.0)\n",
+ "\n",
+ "#result\n",
"print('V = %.2f m/sec' %V)"
- ],
- "language": "python",
+ ],
+ "language": "python",
+ "metadata": {},
"outputs": [
{
- "output_type": "stream",
- "stream": "stdout",
+ "output_type": "stream",
+ "stream": "stdout",
"text": [
"V = 4.11 m/sec"
]
}
- ],
+ ],
"prompt_number": 9
- },
+ },
{
- "cell_type": "markdown",
+ "cell_type": "markdown",
+ "metadata": {},
"source": [
"<h3>Example 5.10, Page Number:314<h3>"
]
- },
+ },
{
- "cell_type": "code",
- "collapsed": false,
+ "cell_type": "code",
+ "collapsed": false,
"input": [
- "'''Determination of flow velocity'''",
- "",
- "import math",
- "",
- "#Variable declaration",
- "del_p=20*10**3 #Pa",
- "dens_water=1000 #kg/m^3",
- "dens_air=1.29 #kg/m^3",
- "",
- "#calculations",
- "",
- "#(i)When flowing fluid is water",
- "v=math.sqrt(2*del_p/dens_water)",
- "",
- "#(ii)When flowing fluid is air",
- "v1=math.sqrt(2*del_p/dens_air)",
- "",
- "#result",
- "print('\\n(i)When flowing fluid is water\\n\\tV=%.3f m/sec'%v)",
+ "\n",
+ "\n",
+ "import math\n",
+ "\n",
+ "#Variable declaration\n",
+ "del_p=20*10**3 #Pa\n",
+ "dens_water=1000 #kg/m^3\n",
+ "dens_air=1.29 #kg/m^3\n",
+ "\n",
+ "#calculations\n",
+ "\n",
+ "#(i)When flowing fluid is water\n",
+ "v=math.sqrt(2*del_p/dens_water)\n",
+ "\n",
+ "#(ii)When flowing fluid is air\n",
+ "v1=math.sqrt(2*del_p/dens_air)\n",
+ "\n",
+ "#result\n",
+ "print('\\n(i)When flowing fluid is water\\n\\tV=%.3f m/sec'%v)\n",
"print('\\n(ii)When flowing fluid is air\\n\\tV=%.0f m/sec'%v1)"
- ],
- "language": "python",
+ ],
+ "language": "python",
+ "metadata": {},
"outputs": [
{
- "output_type": "stream",
- "stream": "stdout",
+ "output_type": "stream",
+ "stream": "stdout",
"text": [
- "",
- "(i)When flowing fluid is water",
- "\tV=6.325 m/sec",
- "",
- "(ii)When flowing fluid is air",
+ "\n",
+ "(i)When flowing fluid is water\n",
+ "\tV=6.325 m/sec\n",
+ "\n",
+ "(ii)When flowing fluid is air\n",
"\tV=176 m/sec"
]
}
- ],
+ ],
"prompt_number": 10
- },
+ },
{
- "cell_type": "markdown",
+ "cell_type": "markdown",
+ "metadata": {},
"source": [
"<h3>Example 5.11, Page Number: 314<h3>"
]
- },
+ },
{
- "cell_type": "code",
- "collapsed": false,
+ "cell_type": "code",
+ "collapsed": false,
"input": [
- "'''detemination of flow velocity'''",
- "",
- "import math",
- "",
- "# variable declaration",
- "dens=1026.0 # density of see water",
- "p=25.0*10**3 # pressure difference in manometer ",
- "",
- "#calculation",
- "V=math.sqrt(2*p/dens)",
- "",
- "#result",
+ "\n",
+ "\n",
+ "import math\n",
+ "\n",
+ "# variable declaration\n",
+ "dens=1026.0 # density of see water\n",
+ "p=25.0*10**3 # pressure difference in manometer \n",
+ "\n",
+ "#calculation\n",
+ "V=math.sqrt(2*p/dens)\n",
+ "\n",
+ "#result\n",
"print('V=%.2f m/sec =%.3f km/hr'%(V,V*18/5))"
- ],
- "language": "python",
+ ],
+ "language": "python",
+ "metadata": {},
"outputs": [
{
- "output_type": "stream",
- "stream": "stdout",
+ "output_type": "stream",
+ "stream": "stdout",
"text": [
"V=6.98 m/sec =25.131 km/hr"
]
}
- ],
+ ],
"prompt_number": 11
- },
+ },
{
- "cell_type": "markdown",
+ "cell_type": "markdown",
+ "metadata": {},
"source": [
"<h3>Example 5.12, Page Number: 314<h3>"
]
- },
+ },
{
- "cell_type": "code",
- "collapsed": false,
+ "cell_type": "code",
+ "collapsed": false,
"input": [
- "'''calculation of flying speed of aircraft'''",
- "import math",
- "",
- "# variable declaration",
- "dens=1.29 # air density at height ",
- "",
- "#calculation",
- "p=12.5*1000",
- "V=math.sqrt(2*p/dens)",
- "",
- "",
- "#result",
+ "\n",
+ "import math\n",
+ "\n",
+ "# variable declaration\n",
+ "dens=1.29 # air density at height \n",
+ "\n",
+ "#calculation\n",
+ "p=12.5*1000\n",
+ "V=math.sqrt(2*p/dens)\n",
+ "\n",
+ "\n",
+ "#result\n",
"print('V=%.2f m/sec =%.2f km/hr'%(V,V*18/5))"
- ],
- "language": "python",
+ ],
+ "language": "python",
+ "metadata": {},
"outputs": [
{
- "output_type": "stream",
- "stream": "stdout",
+ "output_type": "stream",
+ "stream": "stdout",
"text": [
"V=139.21 m/sec =501.16 km/hr"
]
}
- ],
+ ],
"prompt_number": 12
- },
+ },
{
- "cell_type": "markdown",
+ "cell_type": "markdown",
+ "metadata": {},
"source": [
"<h3>Example 5.13, Page Number: 315<h3>"
]
- },
+ },
{
- "cell_type": "code",
- "collapsed": false,
+ "cell_type": "code",
+ "collapsed": false,
"input": [
- "'''Maximum fluid handling capacity of Rotameter'''",
- "",
- "import math",
- "",
- "#variable declaration",
- "Cd=0.6 # discharge coefficient",
- "Dp=0.05 # inside diameter of metering tube ",
- "Df=0.035 # diameter of rotameter ",
- "g=9.8 # acceleration due to gravity",
- "rho_f=3.9*10**3 # density of cylindrical float",
- "rho=1000.0 # water density ",
- "Vf=3.36*10**-5 # volume of the float",
- "",
- "#calculation",
- "Q=Cd*((Dp**2-Df**2)/Df)*math.sqrt(math.pi*g*Vf*(rho_f-rho)/(2*rho))",
- "Q=Q*10000.0",
- "",
- "#result",
- "print('Volumetric flow Q=%.4f *10^-4 m^3/sec' %Q)",
- "#Answer slightly deviates from answer given in the book because of pi value.",
+ "\n",
+ "\n",
+ "import math\n",
+ "\n",
+ "#variable declaration\n",
+ "Cd=0.6 # discharge coefficient\n",
+ "Dp=0.05 # inside diameter of metering tube \n",
+ "Df=0.035 # diameter of rotameter \n",
+ "g=9.8 # acceleration due to gravity\n",
+ "rho_f=3.9*10**3 # density of cylindrical float\n",
+ "rho=1000.0 # water density \n",
+ "Vf=3.36*10**-5 # volume of the float\n",
+ "\n",
+ "#calculation\n",
+ "Q=Cd*((Dp**2-Df**2)/Df)*math.sqrt(math.pi*g*Vf*(rho_f-rho)/(2*rho))\n",
+ "Q=Q*10000.0\n",
+ "\n",
+ "#result\n",
+ "print('Volumetric flow Q=%.4f *10^-4 m^3/sec' %Q)\n",
+ "#Answer slightly deviates from answer given in the book because of pi value.\n",
"#if pi=3.14, then answer is same as in textbook "
- ],
- "language": "python",
+ ],
+ "language": "python",
+ "metadata": {},
"outputs": [
{
- "output_type": "stream",
- "stream": "stdout",
+ "output_type": "stream",
+ "stream": "stdout",
"text": [
"Volumetric flow Q=8.4652 *10^-4 m^3/sec"
]
}
- ],
+ ],
"prompt_number": 13
- },
+ },
{
- "cell_type": "markdown",
+ "cell_type": "markdown",
+ "metadata": {},
"source": [
"<h3>Example 5.14, Page number: 315<h3>"
]
- },
+ },
{
- "cell_type": "code",
- "collapsed": false,
+ "cell_type": "code",
+ "collapsed": false,
"input": [
- "'''Determination of range of flow for ratameter'''",
- "",
- "import math",
- "# variable declaration",
- "Cd=1 # discharge coefficient",
- "Dp=0.018 # inside diameter of metering tube ",
- "Df=0.015 # diameter of rotameter ",
- "g=9.81 # acceleration due to gravity",
- "rho_f=2.7 # density of cylindrical float",
- "rho=0.8 # water density ",
- "Vf=520.0*10**-9 # volume of the float",
- "",
- "#case 1",
- "",
- "#caculation",
- "Qmin=Cd*((Dp**2-Df**2)/Df)*math.sqrt(math.pi*g*Vf*(rho_f-rho)/(2*rho))",
- "Qmin=Qmin*100000.0",
- "",
- "#result",
- "print('Case 1: When float is at the bottom\\n Volumetric flow Qmin=%.3f *10^-5 m^3/sec'%Qmin)",
- "",
- "#case 2",
- "",
- "#calculation",
- "Dp2=0.0617",
- "Qmax=Cd*((Dp2**2-Df**2)/Df)*math.sqrt(math.pi*g*Vf*(rho_f-rho)/(2*rho))",
- "Qmax=Qmax*100000",
- "",
- "#result",
+ "\n",
+ "\n",
+ "import math\n",
+ "# variable declaration\n",
+ "Cd=1 # discharge coefficient\n",
+ "Dp=0.018 # inside diameter of metering tube \n",
+ "Df=0.015 # diameter of rotameter \n",
+ "g=9.81 # acceleration due to gravity\n",
+ "rho_f=2.7 # density of cylindrical float\n",
+ "rho=0.8 # water density \n",
+ "Vf=520.0*10**-9 # volume of the float\n",
+ "\n",
+ "#case 1\n",
+ "\n",
+ "#caculation\n",
+ "Qmin=Cd*((Dp**2-Df**2)/Df)*math.sqrt(math.pi*g*Vf*(rho_f-rho)/(2*rho))\n",
+ "Qmin=Qmin*100000.0\n",
+ "\n",
+ "#result\n",
+ "print('Case 1: When float is at the bottom\\n Volumetric flow Qmin=%.3f *10^-5 m^3/sec'%Qmin)\n",
+ "\n",
+ "#case 2\n",
+ "\n",
+ "#calculation\n",
+ "Dp2=0.0617\n",
+ "Qmax=Cd*((Dp2**2-Df**2)/Df)*math.sqrt(math.pi*g*Vf*(rho_f-rho)/(2*rho))\n",
+ "Qmax=Qmax*100000\n",
+ "\n",
+ "#result\n",
"print('\\n\\nCase 2: When float is at the bottom\\n Volumetric flow Qmax=%.2f *10^-5 m^3/sec'%Qmax)"
- ],
- "language": "python",
+ ],
+ "language": "python",
+ "metadata": {},
"outputs": [
{
- "output_type": "stream",
- "stream": "stdout",
+ "output_type": "stream",
+ "stream": "stdout",
"text": [
- "Case 1: When float is at the bottom",
- " Volumetric flow Qmin=2.879 *10^-5 m^3/sec",
- "",
- "",
- "Case 2: When float is at the bottom",
+ "Case 1: When float is at the bottom\n",
+ " Volumetric flow Qmin=2.879 *10^-5 m^3/sec\n",
+ "\n",
+ "\n",
+ "Case 2: When float is at the bottom\n",
" Volumetric flow Qmax=104.17 *10^-5 m^3/sec"
]
}
- ],
+ ],
"prompt_number": 14
- },
+ },
{
- "cell_type": "markdown",
+ "cell_type": "markdown",
+ "metadata": {},
"source": [
"<h3>Example 5.15, Page Number:316<h3>"
]
- },
+ },
{
- "cell_type": "code",
- "collapsed": false,
+ "cell_type": "code",
+ "collapsed": false,
"input": [
- "'''calculation of coal delivery for coal conveyor system'''",
- "",
- "# variable declaration",
- "W=165.0 # weight of material on section of length",
- "R=328.0 # Conveyor speed m/min",
- "L=16.0 # Length of weighting platform in m",
- "",
- "#calculation",
- "Q=W*R/L",
- "",
- "#result",
+ "\n",
+ "\n",
+ "# variable declaration\n",
+ "W=165.0 # weight of material on section of length\n",
+ "R=328.0 # Conveyor speed m/min\n",
+ "L=16.0 # Length of weighting platform in m\n",
+ "\n",
+ "#calculation\n",
+ "Q=W*R/L\n",
+ "\n",
+ "#result\n",
"print('Flow Rate Q=%.2f kg/min =%.1f kg/hour'%(Q,Q/60))"
- ],
- "language": "python",
+ ],
+ "language": "python",
+ "metadata": {},
"outputs": [
{
- "output_type": "stream",
- "stream": "stdout",
+ "output_type": "stream",
+ "stream": "stdout",
"text": [
"Flow Rate Q=3382.50 kg/min =56.4 kg/hour"
]
}
- ],
+ ],
"prompt_number": 15
- },
+ },
{
- "cell_type": "markdown",
+ "cell_type": "markdown",
+ "metadata": {},
"source": [
"<h3>Example 5.16, Page Number:316<h3>"
]
- },
+ },
{
- "cell_type": "code",
- "collapsed": false,
+ "cell_type": "code",
+ "collapsed": false,
"input": [
- "'''Fluid velocity calculation'''",
- "",
- "import math",
- "",
- "#variable declaration",
- "f=100.0 # beat frequency",
- "d=300.0*10**-3 # Sound path",
- "a=45.0 #angle between transmeter and receiver in degrees",
- "",
- "#calculation",
- "a_rad=45.0*math.pi/180.0",
- "v=f*d/(2*math.cos(a_rad))",
- "",
- "#Result",
+ "\n",
+ "\n",
+ "import math\n",
+ "\n",
+ "#variable declaration\n",
+ "f=100.0 # beat frequency\n",
+ "d=300.0*10**-3 # Sound path\n",
+ "a=45.0 #angle between transmeter and receiver in degrees\n",
+ "\n",
+ "#calculation\n",
+ "a_rad=45.0*math.pi/180.0\n",
+ "v=f*d/(2*math.cos(a_rad))\n",
+ "\n",
+ "#Result\n",
"print('Fluid Velocity V=%.1f m/sec'%v)"
- ],
- "language": "python",
+ ],
+ "language": "python",
+ "metadata": {},
"outputs": [
{
- "output_type": "stream",
- "stream": "stdout",
+ "output_type": "stream",
+ "stream": "stdout",
"text": [
"Fluid Velocity V=21.2 m/sec"
]
}
- ],
+ ],
"prompt_number": 16
- },
+ },
{
- "cell_type": "markdown",
+ "cell_type": "markdown",
+ "metadata": {},
"source": [
"<h3>Example 5.17, Page Number: 316<h3>"
]
- },
+ },
{
- "cell_type": "code",
- "collapsed": false,
+ "cell_type": "code",
+ "collapsed": false,
"input": [
- "'''volume flow rate'''",
- "",
- "# variable declaration",
- "r=150.0 # speed of rotation",
- "v=120.0 # volume trapped between gears and casting",
- "",
- "#clculation",
- "Q=4.0*v*r",
- "",
- "#result",
+ "\n",
+ "\n",
+ "# variable declaration\n",
+ "r=150.0 # speed of rotation\n",
+ "v=120.0 # volume trapped between gears and casting\n",
+ "\n",
+ "#clculation\n",
+ "Q=4.0*v*r\n",
+ "\n",
+ "#result\n",
"print('Volume flow rate Q=%d cm^3/min = %d litres/min'%(Q,Q/1000))"
- ],
- "language": "python",
+ ],
+ "language": "python",
+ "metadata": {},
"outputs": [
{
- "output_type": "stream",
- "stream": "stdout",
+ "output_type": "stream",
+ "stream": "stdout",
"text": [
"Volume flow rate Q=72000 cm^3/min = 72 litres/min"
]
}
- ],
+ ],
"prompt_number": 17
- },
+ },
{
- "cell_type": "markdown",
+ "cell_type": "markdown",
+ "metadata": {},
"source": [
"<h3>Example 5.18, Page Number: 317<h3>"
]
- },
+ },
{
- "cell_type": "code",
- "collapsed": false,
+ "cell_type": "code",
+ "collapsed": false,
"input": [
- "'''induced emf in electromagnetic flow meter'''",
- "",
- "import math",
- "",
- "# variable declaration",
- "Q=2500.0 # Quantitty flow rate",
- "d=2.75 # inner diameter",
- "",
- "#calculation",
- "a=(math.pi*d**2)/4",
- "v=Q/(60*a)",
- "B=60.0",
- "e=B*d*10**-2*v*10**-2",
- "",
- "#result",
+ "\n",
+ "\n",
+ "import math\n",
+ "\n",
+ "# variable declaration\n",
+ "Q=2500.0 # Quantitty flow rate\n",
+ "d=2.75 # inner diameter\n",
+ "\n",
+ "#calculation\n",
+ "a=(math.pi*d**2)/4\n",
+ "v=Q/(60*a)\n",
+ "B=60.0\n",
+ "e=B*d*10**-2*v*10**-2\n",
+ "\n",
+ "#result\n",
"print('Induced emf e =%.4f V=%.1f mV'%(e,e*1000))"
- ],
- "language": "python",
+ ],
+ "language": "python",
+ "metadata": {},
"outputs": [
{
- "output_type": "stream",
- "stream": "stdout",
+ "output_type": "stream",
+ "stream": "stdout",
"text": [
"Induced emf e =0.1157 V=115.7 mV"
]
}
- ],
+ ],
"prompt_number": 18
- },
+ },
{
- "cell_type": "markdown",
+ "cell_type": "markdown",
+ "metadata": {},
"source": [
"<h3>Example 5.19, Pae Number:317<h3>"
]
- },
+ },
{
- "cell_type": "code",
- "collapsed": false,
+ "cell_type": "code",
+ "collapsed": false,
"input": [
- "'''velocity of flow in electromagnetic flow meter'''",
- "",
- "# variable declaration",
- "e=0.2*10**-3 # voltage of electromagnetic flow meter",
- "B=0.08 # Flux density",
- "l=10.0*10**-2 # Diameter of pipe",
- "",
- "#calculation",
- "v=e/(B*l)",
- "",
- "#result",
+ "\n",
+ "\n",
+ "# variable declaration\n",
+ "e=0.2*10**-3 # voltage of electromagnetic flow meter\n",
+ "B=0.08 # Flux density\n",
+ "l=10.0*10**-2 # Diameter of pipe\n",
+ "\n",
+ "#calculation\n",
+ "v=e/(B*l)\n",
+ "\n",
+ "#result\n",
"print('V = %.3f m/sec = %.2f cm/sec'%(v,v*100))"
- ],
- "language": "python",
+ ],
+ "language": "python",
+ "metadata": {},
"outputs": [
{
- "output_type": "stream",
- "stream": "stdout",
+ "output_type": "stream",
+ "stream": "stdout",
"text": [
"V = 0.025 m/sec = 2.50 cm/sec"
]
}
- ],
+ ],
"prompt_number": 19
- },
+ },
{
- "cell_type": "markdown",
+ "cell_type": "markdown",
+ "metadata": {},
"source": [
"<h3>Example 5.20, Page Number: 317<h3>"
]
- },
+ },
{
- "cell_type": "code",
- "collapsed": false,
+ "cell_type": "code",
+ "collapsed": false,
"input": [
- "'''average velocity of flow in electromagnetic flow meter'''",
- "",
- "# variable declaration",
- "ei=0.15*10**-3 # peak value",
- "em=2*ei # p-p amplifier output ",
- "B=0.1 # flux density",
- "l=60.0*10**-3 # diameter of the pipe",
- "",
- "#calculation",
- "v=em/(B*l)",
- "",
- "#result",
+ "\n",
+ "\n",
+ "# variable declaration\n",
+ "ei=0.15*10**-3 # peak value\n",
+ "em=2*ei # p-p amplifier output \n",
+ "B=0.1 # flux density\n",
+ "l=60.0*10**-3 # diameter of the pipe\n",
+ "\n",
+ "#calculation\n",
+ "v=em/(B*l)\n",
+ "\n",
+ "#result\n",
"print('Velocity of flow V = %.2f m/sec = %.1f cm/sec'%(v,v*100))"
- ],
- "language": "python",
+ ],
+ "language": "python",
+ "metadata": {},
"outputs": [
{
- "output_type": "stream",
- "stream": "stdout",
+ "output_type": "stream",
+ "stream": "stdout",
"text": [
"Velocity of flow V = 0.05 m/sec = 5.0 cm/sec"
]
}
- ],
+ ],
"prompt_number": 20
}
- ]
+ ],
+ "metadata": {}
}
]
} \ No newline at end of file