{ "metadata": { "name": "", "signature": "sha256:0f5ebffba7421842791b4539c2f380869e20570438cc6f427747cc5e01bc6228" }, "nbformat": 3, "nbformat_minor": 0, "worksheets": [ { "cells": [ { "cell_type": "heading", "level": 1, "metadata": {}, "source": [ "Chapter 6 : pumping of liquids\n" ] }, { "cell_type": "heading", "level": 3, "metadata": {}, "source": [ "example 6.1 page no : 115" ] }, { "cell_type": "code", "collapsed": false, "input": [ "\n", "\n", "import math \n", "from numpy import *\n", "\n", "# Initialization of Variable\n", "atp = 100.2*1000.\n", "g = 9.81\n", "rho_w = 996.\n", "rho_toluene = 867.\n", "vap_pre_toluene = 4.535*1000\n", "viscosity_toluene = 5.26/10000\n", "\n", "#calculation\n", "m = (atp-vap_pre_toluene)/rho_toluene/g\n", "print \"Max. height of toluene supported by atm. pressure (in m): %.4f\"%m\n", "\n", "#part(1)\n", "hopw = 0.650 #head of pump in terms of water\n", "hopt = hopw*rho_w/rho_toluene #head of pump in terms of toluene\n", "Q = 1.8*10**-3 #flow in m**3/s\n", "d = 2.3*10**-2 #diameter of pipe\n", "pi = 3.14127\n", "\n", "#u = 4*Q/pi/d**2\n", "#substituting this for reynolds no.\n", "Re = 4*Q*rho_toluene/pi/d/viscosity_toluene #reynolds no.\n", "print \"reynolds no : %.4f\"%Re\n", "phi = 0.0396*Re**-0.25\n", "\n", "\n", "#since both LHS and RHS are function of x(max. ht. ab. toluene) \n", "#we define a new variable to solve the eqn\n", "#y = (atp/rho_toluene/g)-(vap_pre_toluene/rho_toluene/g)-(4*phi*16*Q**2*x/pi**2/d**5/g)-hopt\n", "#y = x \n", "#these are two equations\n", "\n", "b = array([0,((atp/rho_toluene/g)-(vap_pre_toluene/rho_toluene/g)-hopt)])\n", "A = array([[1, -1],[1, 4*phi*16*Q**2/pi**2/d**5/g]])\n", "x = linalg.solve(A ,b)\n", "print \"the maximum height above toulene in the tank the pump can be \\\n", "located without risk while flow rate is 1.80dm**3/s (in m): %.4f\"%x[0]\n", "\n", "#solution of part(2)\n", "l = 9. #length \n", "u = math.sqrt(((atp/rho_toluene/g)-(vap_pre_toluene/rho_toluene/g)-hopt-l)*d*g/4/phi/l) #fluid velocity in pipes\n", "Q = pi*d**2*u/4\n", "print \"Maximum delivery rate if pump is located 9m above toluene tank(in m**3/s) %.4f\"%Q\n", "\n", "#solution of part(3)\n", "#clubing d together we get\n", "Q = 1.8/1000.\n", "a = (atp/rho_toluene/g)-(vap_pre_toluene/rho_toluene/g)-hopt-l\n", "b = a*pi**2*g/4./9./16./Q**2/0.0396/(4*Q*rho_toluene/pi/viscosity_toluene)**-0.25\n", "d = (1./b)**(1./4.75)\n", "print \"minimum smooth diameter of suction pipe which will have flow \\\n", "rate as (1.8 dm**3/s) for pump kept at 9 m high (in m):\",d\n" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "Max. height of toluene supported by atm. pressure (in m): 11.2477\n", "reynolds no : 164260.3512\n", "the maximum height above toulene in the tank the pump can be located without risk while flow rate is 1.80dm**3/s (in m): 6.3463\n", "Maximum delivery rate if pump is located 9m above toluene tank(in m**3/s) 0.0009\n", "minimum smooth diameter of suction pipe which will have flow rate as (1.8 dm**3/s) for pump kept at 9 m high (in m): 0.0306728431855\n" ] } ], "prompt_number": 2 }, { "cell_type": "heading", "level": 3, "metadata": {}, "source": [ "example 6.2 pageno : 118" ] }, { "cell_type": "code", "collapsed": false, "input": [ "\n", "\n", "import math \n", "# Initialization of Variable\n", "Q1 = 24.8/1000 #flow in pump 1\n", "d1 = 11.8/100 #diameter of impeller 1\n", "H1 = 14.7 #head of pump 1\n", "N1 = 1450. #frequency of motor 1\n", "Q2 = 48/1000. #flow in pump 2\n", "\n", "#calculation\n", "H2 = 1.15*H1 #head of pump 2\n", "specific_speed = N1*Q1**0.5/H1**0.75\n", "N2 = specific_speed*H2**0.75/Q2**0.5 #frequency of motor 2\n", "print \"frequency of motor 2 in rpm %.4f\"%N2 \n", "d2 = math.sqrt(N2**2*H1/H2/N1**2/d1**2)\n", "print \"diametr of impeller 2 (in m) %.4f\"%(1/d2 )\n", "\n" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "frequency of motor 2 in rpm 1157.4350\n", "diametr of impeller 2 (in m) 0.1585\n" ] } ], "prompt_number": 4 }, { "cell_type": "heading", "level": 3, "metadata": {}, "source": [ "example 6.3 page no : 120" ] }, { "cell_type": "code", "collapsed": false, "input": [ "\n", "\n", "from matplotlib.pyplot import *\n", "import math \n", "%pylab inline\n", "\n", "# Initialization of Variable\n", "Q = [0, 0.01, 0.02, 0.03 ,0.04, 0.05] #discharge\n", "effi_hyd = [65.4 ,71, 71.9, 67.7, 57.5, 39.2]\n", "effi_over = [0 ,36.1, 56.0, 61.0, 54.1, 37.0]\n", "H_sys = [0 ,0, 0, 0, 0, 0]\n", "d = 0.114 #diameter of pipe\n", "d_o = 0.096 #diameter of impeller\n", "h = 8.75 #elevation\n", "g = 9.81 #acc. of gravity\n", "rho = 999. #denisity of water\n", "l = 60. #length of pipe\n", "theta = 0.611 #angle in radians\n", "B = 0.0125 #width of blades\n", "pi = 3.1412\n", "mu = 1.109/1000 #viscosity of water\n", "omega = 2*pi*1750/60.\n", "H_theor = []\n", "# calculation\n", "for i in range(6):\n", " if i == 0:\n", " H_sys[i] = h\n", " else:\n", " H_sys[i] = h+8.*Q[i]**2./pi**2/d**4/g*(1+8*l*0.0396/d*(4*rho*Q[i]/pi/d/mu)**-0.25)\n", " H_theor.append(omega**2*d_o**2/g-omega*Q[i]/2/pi/g/B/math.tan(theta))\n", "\n", "#H_theor = omega**2*d_o**2/g-omega*Q/2/pi/g/B/math.tan(theta)\n", "#print (H_sys\"head of system (in m)\")\n", "#print (H_theor)\n", "H_eff = [0,0,0,0,0,0]\n", "for i in range(6):\n", " H_eff[i] = effi_hyd[i]*H_theor[i]/100.\n", "\n", "#print (H_eff)\n", "plot(Q,effi_hyd, 'r--d')\n", "plot(Q,effi_over, 'g')\n", "plot(Q,H_eff,'k')\n", "plot(Q,H_theor)\n", "plot(Q,H_sys ,'c-')\n", "title('system characteritics')\n", "ylabel('Head(m)or Efficiency(%)')\n", "xlabel('volumetric flow rate(m**3/s)')\n", "show()\n", "\n", "#calculation of power\n", "#at intersecting point using datatrip b/w H_sys &H_eff\n", "Q = 0.0336\n", "effi_over = 59.9\n", "H_eff = 13.10\n", "P = H_eff*rho*g*Q/effi_over/10\n", "print \"Power required to pump fluid at this rate(in KW): %.4f\"%P \n", "\n" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "Populating the interactive namespace from numpy and matplotlib\n" ] }, { "output_type": "stream", "stream": "stderr", "text": [ "WARNING: pylab import has clobbered these variables: ['draw_if_interactive', 'pi', 'new_figure_manager']\n", "`%pylab --no-import-all` prevents importing * from pylab and numpy\n" ] }, { "metadata": {}, "output_type": "display_data", "png": 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7gVUvPH06oKkJDB4MHDsGvPeeXGsl0lVri4ExhoyMDPHzjIwMCMqds52ov//d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\nw+PNmzdo3bp1jeFhYWEBTU31ue61Oqp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"text": [ "" ] }, { "output_type": "stream", "stream": "stdout", "text": [ "Power required to pump fluid at this rate(in KW): 7.2014\n" ] } ], "prompt_number": 5 }, { "cell_type": "heading", "level": 3, "metadata": {}, "source": [ "example 6.4 pageno : 123" ] }, { "cell_type": "code", "collapsed": false, "input": [ "\n", "import math \n", "from matplotlib.pyplot import *\n", "\n", "# Initialization of Variable\n", "#each is increased by five units to make each compatible for graph plotting\n", "Q = [0, 0.01, 0.02, 0.03, 0.04, 0.05, 0.06, 0.07, 0.08, 0.09, 0.1] #flow rate\n", "HeffA = [20.63 ,19.99, 17.80, 14.46, 10.33, 5.71, 0, 0, 0, 0, 0 ] #Heff of pump A\n", "HeffB = [18 ,17, 14.95, 11.90, 8.10, 3.90, 0, 0, 0, 0, 0] #Heff of pump B\n", "alpha = 1.\n", "h = 10.4\n", "d = 0.14\n", "l = 98.\n", "pi = 3.1412\n", "g = 9.81\n", "rho = 999.\n", "mu = 0.001109\n", "H_sys = [0,0,0,0,0,0,0,0,0,0,0]\n", "for i in range(11):\n", " if i == 0:\n", " H_sys[i] = h\n", " else:\n", " H_sys[i] = h+8*Q[i]**2/pi**2/d**4/g*(1+8*l*0.0396/d*(4*rho*Q[i]/pi/d/mu)**-0.25)\n", "\n", "#H_sys is head of the system\n", "print \"the head of system in terms of height of water : \",H_sys\n", "plot(Q,H_sys,'r--d')\n", "plot(Q,HeffA ,'-c')\n", "plot(Q,HeffB)\n", "show()\n", "\n", "#at intersecting point using datatrip b/w H_sys &H_effA\n", "print \"the flow rate at which H_sys takes over HeffA \",0.03339\n", "\n", "\n", "\n" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "the head of system in terms of height of water : [10.4, 10.703503558535079, 11.434551925145852, 12.522017190713953, 13.934570851357016, 15.652293146483034, 17.66081196342499, 19.949010875049055, 22.507899154909985, 25.329974605787854, 28.4088306047139]\n" ] }, { "metadata": {}, "output_type": "display_data", "png": 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"text": [ "" ] }, { "output_type": "stream", "stream": "stdout", "text": [ "the flow rate at which H_sys takes over HeffA 0.03339\n" ] } ], "prompt_number": 7 }, { "cell_type": "heading", "level": 3, "metadata": {}, "source": [ "example 6.5 pageno : 126" ] }, { "cell_type": "code", "collapsed": false, "input": [ "\n", "\n", "import math\n", "from numpy import *\n", "\n", "# Initialization of Variable\n", "rho = 1000.\n", "dc = .15\n", "l = 7.8\n", "g = 9.81\n", "pi = 3.1428\n", "atp = 105.4*1000\n", "vap_pre = 10.85*1000\n", "sl = .22\n", "dp = 0.045\n", "h = 4.6\n", "\n", "#(\"x(t) = sl/2*cos(2*pi*N*t)\" \"the function of print lcement\")\n", "#\"since we have to maximize the acceleration double derivate the terms\")\n", "#since double derivation have the term cos(kt) \n", "#finding it maxima\n", "t = linspace(0,5,100)\n", "k = 1.\n", "\n", "def maximacheckerforcosine():\n", " h = 0.00001\n", " a = 0.00\n", " for i in range(1,401): \n", " if (math.cos(a+h)-math.cos(a-h))/2*h == 0 and math.cos(i-1)>0:\n", " break\n", " else:\n", " a = 0.01+a\n", " m = i-1\n", " v = math.cos(i-1)\n", " return m,v\n", "\n", "a, b = maximacheckerforcosine()\n", "\n", "print \"time t when the acceleration will be maximum(s)\",a\n", "\n", "#double derivative will result in a square of value of N\n", "#lets consider its coefficient all will be devoid of N**2 \n", "k = sl/2*(2*pi)**2 #accn max of piston\n", "kp = k*1./4*pi*dc**2/1.*4/pi/dp**2 #accn coeff. ofsuction pipe\n", "f = 1./4*pi*dp**2*l*rho*kp #force exerted by piston\n", "p = f/1.*4./pi/dp**2 #pressure exerted by piston\n", "\n", "#calculation\n", "o = atp-h*rho*g-vap_pre\n", "#constant term of quadratic eqn\n", "y = poly1d([-p, 0,o],False)\n", "a = roots(y)\n", "print \"Maximum frequency of oscillation if cavitation o be avoided(in Hz) %.4f\"%abs(a[0])\n" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "time t when the acceleration will be maximum(s) 0\n", "Maximum frequency of oscillation if cavitation o be avoided(in Hz) 0.3622\n" ] } ], "prompt_number": 8 }, { "cell_type": "heading", "level": 3, "metadata": {}, "source": [ "example 6.6 pageno : 128" ] }, { "cell_type": "code", "collapsed": false, "input": [ "\n", "\n", "import math \n", "\n", "# Initialization of Variable\n", "rhos = 1830. #density of acid\n", "atp = 104.2*1000 #atmospheric pressure\n", "temp = 11.+273 #temp in kelvin\n", "M = 28.8/1000 #molar mass of air\n", "R = 8.314 #universal gas constant\n", "g = 9.81 #acceleration of gravity\n", "pi = 3.14\n", "d = 2.45 #diameter of tank\n", "l = 10.5 #length of tank\n", "h_s = 1.65 #height of surface of acid from below\n", "effi = 0.93 #efficiency\n", "\n", "#calculation\n", "mliq = pi*d**2*l*rhos/4\n", "h_atm = atp/rhos/g #height conversion of atp\n", "h_r = 4.3-1.65 #height difference\n", "mair = g*h_r*mliq*M/(effi*R*temp*math.log(h_atm/(h_atm+h_s))) #mass of air\n", "print \"mass of air required to lift the sulphuric acid tank %.4f\"%mair\n", "print \"The negative sign indicates air is expanding & work done is magnitude of value in kg:\"\n", "m = abs(mair/mliq)\n", "print \"The mass of air required for per kilo of acid transferred: %.4f\"%m\n", "\n" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "mass of air required to lift the sulphuric acid tank -123.3851\n", "The negative sign indicates air is expanding & work done is magnitude of value in kg:\n", "The mass of air required for per kilo of acid transferred: 0.0014\n" ] } ], "prompt_number": 9 }, { "cell_type": "code", "collapsed": false, "input": [], "language": "python", "metadata": {}, "outputs": [] } ], "metadata": {} } ] }