{ "metadata": { "name": "" }, "nbformat": 3, "nbformat_minor": 0, "worksheets": [ { "cells": [ { "cell_type": "heading", "level": 1, "metadata": {}, "source": [ "Chapter 10 - Tabulated Properties : Steam Tables" ] }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 1 - Pg 155" ] }, { "cell_type": "code", "collapsed": false, "input": [ "#Calculate the work and heat of vaporization of water\n", "#initialization of varaibles\n", "P=100. #psia\n", "hfg=888.8 #B/lb\n", "#calculations\n", "print '%s' %(\"From steam tables,\")\n", "vg=4.432 #cu ft/lb\n", "vf=0.001774 #cu ft/lb\n", "W=P*(vg-vf)*144\n", "ufg=807.1 #B/lb\n", "W=hfg-ufg\n", "sfg=1.1286\n", "Q=788*sfg #Heat\n", "#results\n", "print '%s %.1f %s' %(\"Work done = \",W,\"B/lb\")\n", "print '%s %d %s' %(\"\\n Heat of vaporization of water =\",Q,\"B/lb\")\n" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "From steam tables,\n", "Work done = 81.7 B/lb\n", "\n", " Heat of vaporization of water = 889 B/lb\n" ] } ], "prompt_number": 1 }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 2 - Pg 156" ] }, { "cell_type": "code", "collapsed": false, "input": [ "#caclulate the pressure, temperature and enthalpy\n", "#initialization of varaibles\n", "s=1.6315 #B/lb R\n", "#calculations\n", "print '%s' %(\"From table 1 \")\n", "h=1180.6 #B/lb\n", "t=302.92 #F\n", "p=70 #psia\n", "#results\n", "print '%s %d %s' %(\"Pressure = \",p,\"psia\")\n", "print '%s %.2f %s' %(\"\\n Temperature =\",t,\"F\")\n", "print '%s %.1f %s' %(\"\\n Enthalpy =\",h,\"B/lb\")\n" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "From table 1 \n", "Pressure = 70 psia\n", "\n", " Temperature = 302.92 F\n", "\n", " Enthalpy = 1180.6 B/lb\n" ] } ], "prompt_number": 2 }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 3 - Pg 156" ] }, { "cell_type": "code", "collapsed": false, "input": [ "#calculate the Internal energy of the gas\n", "#initialization of varaibles\n", "T=250. #F\n", "print '%s' %(\"From table 1,\")\n", "p=29.825 #psia\n", "hg=1164 #B/lb\n", "vg=13.821 #cu ft/lb\n", "#calculations\n", "ug=hg-(p)*144*vg/778.\n", "#results\n", "print '%s %.1f %s' %(\"Internal energy of the gas = \",ug,\"B/lb\")\n" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "From table 1,\n", "Internal energy of the gas = 1087.7 B/lb\n" ] } ], "prompt_number": 3 }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 4 - Pg 158" ] }, { "cell_type": "code", "collapsed": false, "input": [ "#Calculate the specific volume, Enthalpy and Entropy of the gas\n", "#initialization of varaibles\n", "x=0.4\n", "P=100. #psia\n", "#calculations\n", "y=1-x\n", "print '%s' %(\"From table 2,\")\n", "vf=0.01774\n", "vg=4.432\n", "vx=x*vf+y*vg\n", "hf=298.4\n", "hfg=888.8\n", "hx=hf+y*hfg\n", "sg=1.6026\n", "sfg=1.1286\n", "sx=sg-x*sfg\n", "#results\n", "print '%s %.3f %s' %(\"Specific volume = \",vx,\"cu ft/lb\")\n", "print '%s %.1f %s' %(\"\\n Enthalpy =\",hx,\"B/lb\")\n", "print '%s %.4f %s' %(\"\\n Entropy = \",sx,\"B/lb R\")\n" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "From table 2,\n", "Specific volume = 2.666 cu ft/lb\n", "\n", " Enthalpy = 831.7 B/lb\n", "\n", " Entropy = 1.1512 B/lb R\n" ] } ], "prompt_number": 4 }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 5 - Pg 158" ] }, { "cell_type": "code", "collapsed": false, "input": [ "#Calculate the enthalpy of the gas\n", "#initialization of varaibles\n", "x=0.97\n", "P=100. #psia\n", "#calculations\n", "print '%s' %(\"From table 2,\")\n", "hf=298.4\n", "hfg=888.8\n", "hx=hf+x*hfg\n", "hg=1187.2\n", "hx2=hg-(1-x)*hfg\n", "#results\n", "print '%s %d %s' %(\"\\n Enthalpy =\",hx,\"B/lb\")\n", "print '%s %.1f %s' %(\"\\n Accurate Enthalpy =\",hx2,\"B/lb\")" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "From table 2,\n", "\n", " Enthalpy = 1160 B/lb\n", "\n", " Accurate Enthalpy = 1160.5 B/lb\n" ] } ], "prompt_number": 5 }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 6 - Pg 159" ] }, { "cell_type": "code", "collapsed": false, "input": [ "#Calculate the specific volume and enthalpy of the process\n", "#initialization of varaibles\n", "s=1.7050 #B/lb R\n", "#calculations\n", "print '%s' %(\"From table 2,\")\n", "sx=1.7050\n", "sg=1.7549\n", "sfg=1.4415\n", "dx=(sg-sx)/sfg\n", "hg=1150.8\n", "hfg=969.7\n", "hx=hg-dx*hfg\n", "vg=26.29\n", "vfg=26.27\n", "vx=vg-dx*vfg\n", "#results\n", "print '%s %.2f %s' %(\"Specific volume = \",vx,\"cu ft/lb\")\n", "print '%s %.1f %s' %(\"\\n Enthalpy =\",hx,\"B/lb\")\n" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "From table 2,\n", "Specific volume = 25.38 cu ft/lb\n", "\n", " Enthalpy = 1117.2 B/lb\n" ] } ], "prompt_number": 1 }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 7 - Pg 159" ] }, { "cell_type": "code", "collapsed": false, "input": [ "#calculate the enthalpy required\n", "#initialization of varaibles\n", "P=150 #psia\n", "T=400 #F\n", "#calculations\n", "print '%s' %(\"From table 3,\")\n", "h=1219.4 #B/lb\n", "#results\n", "print '%s %.1f %s' %(\"Enthalpy =\",h,\"B/lb\")\n" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "From table 3,\n", "Enthalpy = 1219.4 B/lb\n" ] } ], "prompt_number": 7 }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 8 - Pg 159" ] }, { "cell_type": "code", "collapsed": false, "input": [ "#Calculate the temperature of steam\n", "#initialization of varaibles\n", "en=1303.7 #B/lb\n", "P=300 #psia\n", "#calculations\n", "print '%s' %(\"Given hg is less than h, steam is superheated. T=580 F\")\n", "T=580 #F\n", "#results\n", "print '%s %d %s' %(\"Temperature =\",T,\"F\")\n" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "Given hg is less than h, steam is superheated. T=580 F\n", "Temperature = 580 F\n" ] } ], "prompt_number": 8 }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 9 - Pg 160" ] }, { "cell_type": "raw", "metadata": {}, "source": [ "This is a theoretical example." ] }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 10 - Pg 161" ] }, { "cell_type": "code", "collapsed": false, "input": [ "#Calculate the Enthalpy and Volume of the gas\n", "#initialization of varaibles\n", "import math\n", "T=100. #F\n", "P=1000. #psia\n", "#calculations\n", "print '%s' %(\"From table 4\")\n", "dvf=-5.1*math.pow(10,-5)\n", "dhf=2.7\n", "vf=0.01613\n", "hf=67.97\n", "v=vf+dvf\n", "h=hf+dhf\n", "#results\n", "print '%s %.2f %s' %(\"Enthalpy =\",h,\"B/lb\")\n", "print '%s %.5f %s' %(\"\\n Volume = \",v,\"cu ft/lb\")\n" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "From table 4\n", "Enthalpy = 70.67 B/lb\n", "\n", " Volume = 0.01608 cu ft/lb\n" ] } ], "prompt_number": 10 }, { "cell_type": "heading", "level": 2, "metadata": {}, "source": [ "Example 11 - Pg 164" ] }, { "cell_type": "code", "collapsed": false, "input": [ "#calculate the Quality of steam\n", "#initialization of varaibles\n", "h1=1183.2 #B/lb\n", "hg=1198.4 #B/lb\n", "hfg=843.\n", "#calculations\n", "x=1- (hg-h1)/hfg\n", "#results\n", "print '%s %.3f' %(\"Quality =\",x)\n" ], "language": "python", "metadata": {}, "outputs": [ { "output_type": "stream", "stream": "stdout", "text": [ "Quality = 0.982\n" ] } ], "prompt_number": 11 } ], "metadata": {} } ] }