diff options
author | hardythe1 | 2014-07-25 12:35:04 +0530 |
---|---|---|
committer | hardythe1 | 2014-07-25 12:35:04 +0530 |
commit | 6846da7f30aadc7b3812538d1b1c9ef2e465a922 (patch) | |
tree | 0ac5e382d6515013c6a1f23d3529dc46e03d0015 /Stoichiometry_And_Process_Calculations/ch2.ipynb | |
parent | dccd504f6bd2f5e97c54d1f0b0d2a99f83497ce5 (diff) | |
download | Python-Textbook-Companions-6846da7f30aadc7b3812538d1b1c9ef2e465a922.tar.gz Python-Textbook-Companions-6846da7f30aadc7b3812538d1b1c9ef2e465a922.tar.bz2 Python-Textbook-Companions-6846da7f30aadc7b3812538d1b1c9ef2e465a922.zip |
removing unwanted:
Diffstat (limited to 'Stoichiometry_And_Process_Calculations/ch2.ipynb')
-rwxr-xr-x | Stoichiometry_And_Process_Calculations/ch2.ipynb | 436 |
1 files changed, 0 insertions, 436 deletions
diff --git a/Stoichiometry_And_Process_Calculations/ch2.ipynb b/Stoichiometry_And_Process_Calculations/ch2.ipynb deleted file mode 100755 index 9894afe0..00000000 --- a/Stoichiometry_And_Process_Calculations/ch2.ipynb +++ /dev/null @@ -1,436 +0,0 @@ -{ - "metadata": { - "name": "" - }, - "nbformat": 3, - "nbformat_minor": 0, - "worksheets": [ - { - "cells": [ - { - "cell_type": "heading", - "level": 1, - "metadata": {}, - "source": [ - "Chapter 2 : Units and Dimensions" - ] - }, - { - "cell_type": "heading", - "level": 3, - "metadata": {}, - "source": [ - "Example 2.1 page no : 24" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "\n", - "import math \n", - "\n", - "# Variables \n", - "V1 = 15. #ft**3/min volumetric flow rate\n", - "ft = 0.3048 #m relationship\n", - "min = 60. #secs relationship\n", - "\n", - "# Calculation \n", - "V = V1*ft**3/min;\n", - "\n", - "# Result \n", - "print \"Volumetric flowrate = %.3e m**3/s\"%V\n", - "D = 1000 #kg/m**3\n", - "M = V * D;\n", - "print \"mass flowrate = %.3f kg/s\"%M\n" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "Volumetric flowrate = 7.079e-03 m**3/s\n", - "mass flowrate = 7.079 kg/s\n" - ] - } - ], - "prompt_number": 1 - }, - { - "cell_type": "heading", - "level": 3, - "metadata": {}, - "source": [ - "Example 2.2 page no : 24" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "\n", - "# Variables \n", - "ft = 0.3048; #m \n", - "lb = 0.4536; #kg\n", - "\n", - "# Calculation \n", - "P = ft*lb;\n", - "\n", - "# Result \n", - "print \"1 poundal is 1 ft*lb/s**2 = %.4f N\"%P\n" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "1 poundal is 1 ft*lb/s**2 = 0.1383 N\n" - ] - } - ], - "prompt_number": 1 - }, - { - "cell_type": "heading", - "level": 3, - "metadata": {}, - "source": [ - "Example 2.3 page no : 24" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "\n", - "# Variables \n", - "kgf = 9.80665; #N KGF\n", - "\n", - "# Calculation and Result \n", - "cm = 10**-2; #m\n", - "P = kgf/cm**2;\n", - "print \"1 kgf/cm**2 = %0.3e N/m**2\"%P\n", - "lbf = 32.174; #lb*ft#s**2\n", - "lb = 0.4535924; #kg\n", - "ft = 0.3048; #m\n", - "in_ = 0.0254; #m\n", - "P1 = lbf*lb*ft/in_**2;\n", - "print \"1 lbf/in**2 = %.2f N/m**2\"%P1\n" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "1 kgf/cm**2 = 9.807e+04 N/m**2\n", - "1 lbf/in**2 = 6894.75 N/m**2\n" - ] - } - ], - "prompt_number": 2 - }, - { - "cell_type": "heading", - "level": 3, - "metadata": {}, - "source": [ - "Example 2.4 page no : 25" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "\n", - "# Variables \n", - "Q1 = 10000. #kJ/hr rate of heat transfer\n", - "kJ = 1000. #J \n", - "hr = 3600. #s \n", - "\n", - "# Calculation \n", - "Q = Q1*kJ/hr; #J/s\n", - "print \"Q = %.2f J/s\"%Q\n", - "x = 0.1; #m\n", - "A = 1. #m**2\n", - "T = 800. #K\n", - "k = x*Q/(A*T);\n", - "\n", - "# Result \n", - "print \"thermal conductivity = %.3f W/(m*k)\"%k\n", - "J = 1/4.1868 #cal\n", - "k1 = k*J*hr/1000\n", - "print \"thermal conductivity = %.3F kcal/(h*m*C)\"%k1\n", - "\n", - "# note : answers may vary because of rounding off error." - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "Q = 2777.78 J/s\n", - "thermal conductivity = 0.347 W/(m*k)\n", - "thermal conductivity = 0.299 kcal/(h*m*C)\n" - ] - } - ], - "prompt_number": 4 - }, - { - "cell_type": "heading", - "level": 3, - "metadata": {}, - "source": [ - "Example 2.5 page no : 26" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "\n", - "# Variables \n", - "F = 300. #N weight of object\n", - "a = 9.81; #m/s**2 gravity\n", - "\n", - "# Calculation \n", - "m = F/a; #kg\n", - "\n", - "# Result \n", - "print \"mass in kg = %.2f kg\"%m\n", - "lb = 4.535924/10; #kG\n", - "m1 = m/lb\n", - "print \"mass in pounds = %.2f LB\"%m1\n" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "mass in kg = 30.58 kg\n", - "mass in pounds = 67.42 LB\n" - ] - } - ], - "prompt_number": 4 - }, - { - "cell_type": "heading", - "level": 3, - "metadata": {}, - "source": [ - "Example 2.6 page no : 26" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "\n", - "# Variables \n", - "z = 15. #m height\n", - "PE = 2000.; #J potential energy\n", - "g = 9.8067; #m/s**2 \n", - "\n", - "# Calculation \n", - "m = PE/(z*g);\n", - "\n", - "# Result \n", - "print \"mass = %.3f kg\"%m\n", - "v = 50; #m/s\n", - "KE = 1./2*m*(v**2)/1000.;\n", - "print \"kinetic energy = %.3f kj\"%KE\n" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "mass = 13.596 kg\n", - "kinetic energy = 16.995 kj\n" - ] - } - ], - "prompt_number": 6 - }, - { - "cell_type": "heading", - "level": 3, - "metadata": {}, - "source": [ - "Example 2.7 page no : 26" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "\n", - "\n", - "# Variables \n", - "g = 9.81; #m/s**2 gravity\n", - "m = 100 * 0.4536; #kg weight \n", - "P = 101325.; #N/m**2 standard atomosphere\n", - "D1 = 4.; #inch\n", - "\n", - "# Calculation \n", - "D = D1 * 2.54 * 10**-2; #m\n", - "A = 3.1415 * (D**2)/4; #m**2\n", - "F1 = P * A; #N\n", - "F2 = m * g; #N\n", - "F = F1 + F2;\n", - "\n", - "# Result \n", - "print \"Total force acting on the gas = %.2f N\"%F\n", - "P1 = F / A; #N/m**2\n", - "P2 = P1/100000.; #bar\n", - "P3 = P1/(6.894757 * 10**3); #psi\n", - "print \"Pressure in N/m**2 = %.3e N/m**2\"%P1\n", - "print \"Pressure in bar = %.3f bar\"%P2\n", - "print \"Pressure in psi = %.2f psi\"%P3\n", - "d = 0.4; #m\n", - "W = F * d;\n", - "print \"Work done = %.2f J\"%W\n", - "PE = m * g * d;\n", - "print \"Change in potential energy = %.2f J\"%PE\n" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "Total force acting on the gas = 1266.43 N\n", - "Pressure in N/m**2 = 1.562e+05 N/m**2\n", - "Pressure in bar = 1.562 bar\n", - "Pressure in psi = 22.66 psi\n", - "Work done = 506.57 J\n", - "Change in potential energy = 177.99 J\n" - ] - } - ], - "prompt_number": 7 - }, - { - "cell_type": "heading", - "level": 3, - "metadata": {}, - "source": [ - "Example 2.8 page no : 28" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "# Variables \n", - "#kG = (6.7 * 10**-4) * (( G * (ds + dt) / ds)**0.8) / ((ds**0.4)*(dG**0.2))\n", - "\n", - "#kG - lbmol/(h ft**2 atm), G - lb/(ft**2 h), ds, dG, dt - feet\n", - "#kG1 - kmol/(m**2 h atm), G1 - kg/(m**2 h), ds1, dG1, dt1 - m\n", - "G = 0.2048; #G1 * lb/(ft**2 h) velocity\n", - "d = 3.2808; #d1 * ft clearance between grids\n", - "ds = d; # clearance between grids\n", - "dt = d; # clearance between grids\n", - "dG = d; # clearance between grids\n", - "kG = 4.885; #kG1 (lbmol/(h ft**2 atm) = 4.885 * kmol/(m**2 h atm))\n", - "\n", - "# Calculation \n", - "C = (6.7 * 10**-4) * (( G * d / ds)**0.8) / ((ds**0.4)*(dG**0.2))* kG;\n", - "\n", - "# Result \n", - "print \"Co-efficient = %.2e (kmol)(kg)**-0.8 (m)**0.2 (h)**-0.2 (atm)**-1\"%C\n", - "# this is the constant for the equation\n", - "# the equation thus becomes,\n", - "# kG1 = C * (( G1 * (ds1 + dt1) / ds1)**0.8) / ((ds1**0.4)*(dG1**0.2))\n" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "Co-efficient = 4.51e-04 (kmol)(kg)**-0.8 (m)**0.2 (h)**-0.2 (atm)**-1\n" - ] - } - ], - "prompt_number": 7 - }, - { - "cell_type": "heading", - "level": 3, - "metadata": {}, - "source": [ - "Example 2.9 page no : 29" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "\n", - "from sympy import Symbol\n", - "\n", - "# Variables \n", - "#Cp = 7.13 + 0.577 * (10**-3) * t + 0.0248 * (10**-6) * t**2 \n", - "\n", - "#Cp - Btu/lb-mol F, t - F\n", - "#Cp1 - kJ/kmol K , t1 - K\n", - "a = 7.13 # first term\n", - "b = 0.577 * 10**-3 # second term\n", - "c = 0.0248 * 10**-6 # third term\n", - "#t = 1.8 * t1 - 459.67\n", - "Cp = 4.1868; #Cp1 (Btu/lb-mol F = 4.1868 * (kJ/kmol K) )\n", - "t = Symbol('T')\n", - "#substituting the above, we get,\n", - "#Cp1 = 28.763 + 4.763 * (10**-3) * t1 + 0.3366 * (10**-6) * t**2\n", - "a1 = 28.763\n", - "\n", - "# Calculation \n", - "b1 = 4.763 * (10**-3)\n", - "c1 = 0.3366 * (10**-6)\n", - "\n", - "Cp = a1 + b1*t + c1*t**2\n", - "# Result \n", - "print \"a1 = \",a1\n", - "print \"b1 = \",b1\n", - "print \"c1 = \",c1\n", - "# this are the co efficents for the following equation;\n", - "# Cp1 = a1 + b1 * t1 + c1 * (t1)**2\n", - "print \"Equation Cp = \",Cp" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "a1 = 28.763\n", - "b1 = 0.004763\n", - "c1 = 3.366e-07\n", - "Equation Cp = 3.366e-7*T**2 + 0.004763*T + 28.763\n" - ] - } - ], - "prompt_number": 10 - } - ], - "metadata": {} - } - ] -}
\ No newline at end of file |