{ "metadata": { "name": "", "signature": "sha256:9350c41424c136ffdcb61a367641cc78b39d6999ad3a13b8f61c623099d55d5b" }, "nbformat": 3, "nbformat_minor": 0, "worksheets": [ { "cells": [ { "cell_type": "heading", "level": 1, "metadata": {}, "source": [ "Chapter 6: The Ideal Gas" ] }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 6.1, page no. 101" ] }, { "cell_type": "code", "collapsed": false, "input": [ "\n", "import scipy.integrate\n", "\n", "#intialization of variables\n", "T1 = 40+460.0 #temperature(R)\n", "T2 = 340+460.0 #temperature(R)\n", "\n", "#calculation\n", "def Cv(T):\n", "\tcv = 0.162+0.00046*T\n", "\treturn cv\n", "\t\n", "du = scipy.integrate.quadrature(Cv, T1, T2)[0]\n", "\n", "#result\n", "print \"Change in specific internal energy = %.1f B/lbm\" %du" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "Change in specific internal energy = 138.3 B/lbm\n" ] } ], "prompt_number": 1 }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 6.2, page no. 103" ] }, { "cell_type": "code", "collapsed": false, "input": [ "\n", "#initialization\n", "\n", "cp = 0.24 #B/lbm F\n", "R = 53.3 #ft-lb/lbm F\n", "\n", "#calculation\n", "cv = cp-R/778.0\n", "\n", "#result\n", "print \"Specific heat at constant volume = %.3f B/lbm F\" %cv" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "Specific heat at constant volume = 0.171 B/lbm F\n" ] } ], "prompt_number": 2 }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 6.3, page no. 104" ] }, { "cell_type": "code", "collapsed": false, "input": [ "\n", "import scipy.integrate\n", "\n", "#initialization\n", "T1 = 1400+460.0 #temperature(R)\n", "T2 = 1200+460.0 #temperature(R)\n", "\n", "#calculation\n", "def Cp(T):\n", "\tcp = 0.317- 1.2*100/T + 4*10**4/T**2\n", "\treturn cp\n", "\n", "dh = scipy.integrate.quadrature(Cp, T1, T2)[0]\n", "\n", "#result\n", "print \"Change in stagnation enthalpy = %.1f B/lbm\" %dh" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "Change in stagnation enthalpy = -52.3 B/lbm\n" ] } ], "prompt_number": 3 }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 6.4, page no. 106" ] }, { "cell_type": "code", "collapsed": false, "input": [ "\n", "import scipy.integrate\n", "\n", "#initialization\n", "T1 = 100+460.0 #temperature(R)\n", "T2 = 300+460.0 #temperature(R)\n", "P1 = 15.0 #pressure(lb/in^2)\n", "P2 = 30.0 #pressure(lb/in^2)\n", "Cp = 0.3 #constant pressure(B/lbm F)\n", "R = 40.0 #gas constant(ft-lb/lbm R)\n", "\n", "#calculation\n", "def fun(f):\n", "\ts=Cp/f\n", "\treturn s\n", "def fun1(f):\n", "\ts2=R/(f*778)\n", "\treturn s2\n", "\n", "ds1 = scipy.integrate.quadrature(fun, T1, T2)[0]\n", "ds2 = scipy.integrate.quadrature(fun1, P1, P2)[0]\n", "ds = ds1 - ds2\n", "\n", "#result\n", "print \"Change in entropy = %.4f B/lbm R\" %ds" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "Change in entropy = 0.0560 B/lbm R\n" ] } ], "prompt_number": 4 }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 6.5, page no. 108" ] }, { "cell_type": "code", "collapsed": false, "input": [ "\n", "#initialization\n", "\n", "T1 = 40+460.0 #temperature(R)\n", "T2 = 340+460.0 #temperature(R)\n", "P1 = 15.0 #pressure(lb/in^2)\n", "cp = 0.24\n", "cv = 0.171\n", "\n", "#calculation\n", "gamma=cp/cv\n", "P2=P1 *((T2/T1)**(gamma/(gamma-1)))\n", "\n", "#result\n", "print \"Final pressure = %.1f lb/in^2\" %P2" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "Final pressure = 76.9 lb/in^2\n" ] } ], "prompt_number": 7 }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 6.6, page no. 110" ] }, { "cell_type": "code", "collapsed": false, "input": [ "\n", "import math\n", "\n", "#initialization\n", "P1 = 16.0 #lb/in^2\n", "P2 = 14.0 #lb/in^2\n", "Tt = 83+460.0 #R\n", "gamma = 1.4\n", "cp = 0.24 #B/lbm F\n", "\n", "#calculation\n", "T = Tt *(P2/P1)**((gamma-1)/gamma)\n", "dh = cp*(Tt-T)\n", "V = math.sqrt(2*32.2*778*dh)\n", "\n", "#result\n", "print \"Actual temperature in the flow = %d R\" %T\n", "print \"Flow velocity = %d ft/sec\" %V\n", "\n", "#difference in answeres is due to internal rounding off in Python" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "Actual temperature in the flow = 522 R\n", "Flow velocity = 494 ft/sec\n" ] } ], "prompt_number": 7 }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 6.7, page no. 111" ] }, { "cell_type": "code", "collapsed": false, "input": [ "\n", "import math\n", "import scipy.integrate\n", "\n", "#initialization\n", "T1 = 400.0+460.0 #R\n", "P1 = 100.0 #lb/in^2\n", "P2 = 20.0 #lb/in^2\n", "T2 = 140.0+460.0 #R\n", "Cp = 50.0\n", "\n", "#calculation\n", "Pratio = P1/P2\n", "Tratio = T1/T2\n", "C = math.log(Tratio)/math.log(Pratio)\n", "n=1/(1-C)\n", "v1=Cp*T1/(144*P1)\n", "v2=Cp*T2/(144*P2)\n", "w=144*P1*v1**n\n", "def fun(v):\n", "\tp=w/v**n\n", "\treturn p\n", "\n", "Work = scipy.integrate.quadrature(fun, v1, v2)[0]\n", "\n", "#result\n", "print \"Work done = %f ft-lb/lbm\" %Work" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "Work done = 45118.149895 ft-lb/lbm\n" ] } ], "prompt_number": 9 }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 6.8, page no. 113" ] }, { "cell_type": "code", "collapsed": false, "input": [ "\n", "import math\n", "\n", "#initialization\n", "P1 = 15.0 #lb/in^2\n", "P2 = 20.0 #lb/in^2\n", "T1 = 40+460 #R\n", "T2 = 540+460 #R\n", "\n", "#calculation\n", "#From table 6 at the two temperatures\"\n", "phi1 = 0.58233\n", "phi2 = 0.75042\n", "ds = phi2-phi1-53.3*math.log(P2/P1)/778.0\n", "\n", "#result\n", "print \"Entropy change = %.5f B/lbm R\" %ds" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "Entropy change = 0.14838 B/lbm R\n" ] } ], "prompt_number": 10 }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 6.9, page no. 115" ] }, { "cell_type": "code", "collapsed": false, "input": [ "\n", "#part a\n", "\n", "P2 = 1460.0 #pressure 2\n", "P1 = 1900.0 #pressure 1\n", "V2 = 1900.0 #volume 1\n", "V1 = 1460.0 #volume 2\n", "\n", "pratio = (P2/P1)**3.5\n", "vratio = (V2/V1)**2.5\n", "\n", "print \"Pressure ratio is \", round(pratio,2)\n", "print \"Volume ratio is \", round(vratio,2)\n", "\n", "#part b\n", "#from table 6\n", "Pr2 = 50.34 #pressure 2\n", "Pr1 = 141.51 #pressure 1\n", "Vr2 = 10.743 #volume 1\n", "Vr1 = 4.974 #volume 2\n", "\n", "pratio = (Pr2/Pr1)\n", "vratio = (Vr2/Vr1)\n", "\n", "print \"Pressure ratio is \", round(pratio,2)\n", "print \"Volume ratio is \", round(vratio,2)" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "Pressure ratio is 0.4\n", "Volume ratio is 1.93\n", "Pressure ratio is 0.36\n", "Volume ratio is 2.16\n" ] } ], "prompt_number": 1 } ], "metadata": {} } ] }