Revised list of TBCs

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diff --git a/Thermodynamics,_Statistical_Thermodynamics,_&_Kinetics/Chapter17.ipynb b/Thermodynamics,_Statistical_Thermodynamics,_&_Kinetics/Chapter17.ipynb
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--- a/Thermodynamics,_Statistical_Thermodynamics,_&_Kinetics/Chapter17.ipynb
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@@ -1,509 +0,0 @@
-{

- "metadata": {

-  "name": "",

-  "signature": "sha256:28b1b127871a242526fc780b7f95bfe7e107178dbbf2ff194eb0ee46817a771a"

- },

- "nbformat": 3,

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- "worksheets": [

-  {

-   "cells": [

-    {

-     "cell_type": "heading",

-     "level": 1,

-     "metadata": {},

-     "source": [

-      "Chapter 17: Transport Phenomena"

-     ]

-    },

-    {

-     "cell_type": "heading",

-     "level": 2,

-     "metadata": {},

-     "source": [

-      "Example Problem 17.1, Page Number 417"

-     ]

-    },

-    {

-     "cell_type": "code",

-     "collapsed": false,

-     "input": [

-      "from scipy import constants\n",

-      "from math import sqrt,pi\n",

-      "\n",

-      "#Variable Declaration\n",

-      "M = 0.040                  #Molecualar wt of Argon, kh/mol\n",

-      "P, T = 101325.0, 298.0     #Pressure and Temperature, Pa, K\n",

-      "sigm = 3.6e-19  #\n",

-      "R = 8.314                  #Molar Gas constant,  mol^-1 K^-1\n",

-      "N_A = 6.02214129e+23       #mol^-1\n",

-      "#Calculations\n",

-      "DAr = (1./3)*sqrt(8*R*T/(pi*M))*(R*T/(P*N_A*sqrt(2)*sigm))\n",

-      "\n",

-      "#Results\n",

-      "print 'Diffusion coefficient of Argon %3.1e m2/s'%DAr"

-     ],

-     "language": "python",

-     "metadata": {},

-     "outputs": [

-      {

-       "output_type": "stream",

-       "stream": "stdout",

-       "text": [

-        "Diffusion coefficient of Argon 1.1e-05 m2/s\n"

-       ]

-      }

-     ],

-     "prompt_number": 17

-    },

-    {

-     "cell_type": "heading",

-     "level": 2,

-     "metadata": {},

-     "source": [

-      "Example Problem 17.2, Page Number 418"

-     ]

-    },

-    {

-     "cell_type": "code",

-     "collapsed": false,

-     "input": [

-      "from scipy import constants\n",

-      "from math import sqrt,pi\n",

-      "\n",

-      "#Variable Declaration\n",

-      "DHebyAr = 4.0 \n",

-      "MAr, MHe = 39.9, 4.0       #Molecualar wt of Argon and Neon, kg/mol\n",

-      "P, T = 101325.0, 298.0     #Pressure and Temperature, Pa, K\n",

-      "sigm = 3.6e-19  #\n",

-      "R = 8.314                  #Molar Gas constant,  mol^-1 K^-1\n",

-      "N_A = 6.02214129e+23       #mol^-1\n",

-      "#Calculations\n",

-      "sigHebyAr = (1./DHebyAr)*sqrt(MAr/MHe)\n",

-      "\n",

-      "#Results\n",

-      "print 'Ratio of collision cross sections of Helium to Argon %4.3f'%sigHebyAr"

-     ],

-     "language": "python",

-     "metadata": {},

-     "outputs": [

-      {

-       "output_type": "stream",

-       "stream": "stdout",

-       "text": [

-        "Ratio of collision cross sections of Helium to Argon 0.790\n"

-       ]

-      }

-     ],

-     "prompt_number": 20

-    },

-    {

-     "cell_type": "heading",

-     "level": 2,

-     "metadata": {},

-     "source": [

-      "Example Problem 17.3, Page Number 420"

-     ]

-    },

-    {

-     "cell_type": "code",

-     "collapsed": false,

-     "input": [

-      "from math import sqrt,pi\n",

-      "\n",

-      "#Variable Declaration\n",

-      "D = 1.0e-5                 #Diffusion coefficient, m2/s \n",

-      "t1 = 1000                  #Time, s\n",

-      "t10 = 10000                #Time, s\n",

-      "\n",

-      "#Calculations\n",

-      "xrms1 = sqrt(2*D*t1)\n",

-      "xrms10 = sqrt(2*D*t10)\n",

-      "\n",

-      "#Results\n",

-      "print 'rms displacement at %4d and %4d is  %4.3f and %4.3f m respectively'%(t1,t10,xrms1,xrms10)"

-     ],

-     "language": "python",

-     "metadata": {},

-     "outputs": [

-      {

-       "output_type": "stream",

-       "stream": "stdout",

-       "text": [

-        "rms displacement at 1000 and 10000 is  0.141 and 0.447 m respectively\n"

-       ]

-      }

-     ],

-     "prompt_number": 23

-    },

-    {

-     "cell_type": "heading",

-     "level": 2,

-     "metadata": {},

-     "source": [

-      "Example Problem 17.4, Page Number 421"

-     ]

-    },

-    {

-     "cell_type": "code",

-     "collapsed": false,

-     "input": [

-      "from math import sqrt,pi\n",

-      "\n",

-      "#Variable Declaration\n",

-      "D = 2.2e-5                 #Diffusion coefficient of benzene, cm2/s \n",

-      "x0 = 0.3                   #molecular diameter of benzene, nm\n",

-      "\n",

-      "#Calculations\n",

-      "t = (x0*1e-9)**2/(2*D*1e-4)\n",

-      "\n",

-      "#Results\n",

-      "print 'Time per random walk is %4.3e s or %4.2f ps'%(t,t/1e-12)"

-     ],

-     "language": "python",

-     "metadata": {},

-     "outputs": [

-      {

-       "output_type": "stream",

-       "stream": "stdout",

-       "text": [

-        "Time per random walk is 2.045e-11 s or 20.45 ps\n"

-       ]

-      }

-     ],

-     "prompt_number": 29

-    },

-    {

-     "cell_type": "heading",

-     "level": 2,

-     "metadata": {},

-     "source": [

-      "Example Problem 17.5, Page Number 424"

-     ]

-    },

-    {

-     "cell_type": "code",

-     "collapsed": false,

-     "input": [

-      "from math import sqrt,pi\n",

-      "\n",

-      "#Variable Declaration\n",

-      "P = 101325                  #Pressure, Pa\n",

-      "kt = 0.0177                 #Thermal conductivity, J/(K.m.s)\n",

-      "T = 300.0                   #Temperature, K\n",

-      "k = 1.3806488e-23           #Boltzmanconstant,J K^-1\n",

-      "sigm = 3.6e-19  #\n",

-      "R = 8.314                  #Molar Gas constant,  mol^-1 K^-1\n",

-      "NA = 6.02214129e+23        #mol^-1\n",

-      "M = 39.9                   #Molecualar wt of Argon and Neon, kg/mol\n",

-      "#Calculations\n",

-      "CvmbyNA = 3.*k/2\n",

-      "nuavg = sqrt(8*R*T/(pi*M*1e-3))\n",

-      "N = NA*P/(R*T)\n",

-      "labda = 3*kt/(CvmbyNA*nuavg*N)\n",

-      "sigm = 1/(sqrt(2)*N*labda)\n",

-      "\n",

-      "#Results\n",

-      "print 'Mean free path %4.3e m and collisional cross section %4.2e m2'%(labda, sigm)"

-     ],

-     "language": "python",

-     "metadata": {},

-     "outputs": [

-      {

-       "output_type": "stream",

-       "stream": "stdout",

-       "text": [

-        "Mean free path 2.627e-07 m and collisional cross section 1.10e-19 m2\n"

-       ]

-      }

-     ],

-     "prompt_number": 34

-    },

-    {

-     "cell_type": "heading",

-     "level": 2,

-     "metadata": {},

-     "source": [

-      "Example Problem 17.6, Page Number 427"

-     ]

-    },

-    {

-     "cell_type": "code",

-     "collapsed": false,

-     "input": [

-      "from math import sqrt,pi\n",

-      "\n",

-      "#Variable Declaration\n",

-      "eta = 227.                  #Viscosity of Ar, muP\n",

-      "P = 101325                  #Pressure, Pa\n",

-      "kt = 0.0177                 #Thermal conductivity, J/(K.m.s)\n",

-      "T = 300.0                   #Temperature, K\n",

-      "k = 1.3806488e-23           #Boltzmanconstant,J K^-1\n",

-      "R = 8.314                   #Molar Gas constant,  mol^-1 K^-1\n",

-      "NA = 6.02214129e+23         #mol^-1\n",

-      "M = 39.9                    #Molecualar wt of Argon and Neon, kg/mol\n",

-      "\n",

-      "#Calculations\n",

-      "nuavg = sqrt(8*R*T/(pi*M*1e-3))\n",

-      "N = NA*P/(R*T)\n",

-      "m = M*1e-3/NA\n",

-      "labda = 3.*eta*1e-7/(nuavg*N*m)          #viscosity in kg m s units\n",

-      "sigm = 1./(sqrt(2)*N*labda)\n",

-      "\n",

-      "#Results\n",

-      "print 'Collisional cross section %4.2e m2'%(sigm)"

-     ],

-     "language": "python",

-     "metadata": {},

-     "outputs": [

-      {

-       "output_type": "stream",

-       "stream": "stdout",

-       "text": [

-        "Collisional cross section 2.74e-19 m2\n"

-       ]

-      }

-     ],

-     "prompt_number": 48

-    },

-    {

-     "cell_type": "heading",

-     "level": 2,

-     "metadata": {},

-     "source": [

-      "Example Problem 17.7, Page Number 429"

-     ]

-    },

-    {

-     "cell_type": "code",

-     "collapsed": false,

-     "input": [

-      "from math import sqrt,pi\n",

-      "\n",

-      "#Variable Declaration\n",

-      "m = 22.7                    #Mass of CO2, kg\n",

-      "T = 293.0                   #Temperature, K\n",

-      "L = 1.0                     #length of the tube, m\n",

-      "d = 0.75                    #Diameter of the tube, mm\n",

-      "eta = 146                   #Viscosity of CO2, muP\n",

-      "p1 = 1.05                   #Inlet pressure, atm\n",

-      "p2 = 1.00                   #Outlet pressure, atm\n",

-      "atm2pa = 101325             #Conversion for pressure from atm to Pa \n",

-      "M = 0.044                   #Molecular wt of CO2, kg/mol\n",

-      "R = 8.314                   #Molar Gas constant,  J mol^-1 K^-1\n",

-      "\n",

-      "#Calculations\n",

-      "p1 = p1*atm2pa\n",

-      "p2 = p2*atm2pa\n",

-      "F = pi*(d*1e-3/2)**4*(p1**2-p2**2)/(16.*eta/1.e7*L*p2)\n",

-      "nCO2 = m/M\n",

-      "v = nCO2*R*T/((p1+p2)/2)\n",

-      "t = v/F\n",

-      "\n",

-      "#Results\n",

-      "print 'Flow rate is %4.3e m3/s'%(F)\n",

-      "print 'Cylinder can be used for %4.3e s nearly %3.1f days'%(t, t/(24*3600))"

-     ],

-     "language": "python",

-     "metadata": {},

-     "outputs": [

-      {

-       "output_type": "stream",

-       "stream": "stdout",

-       "text": [

-        "Flow rate is 2.762e-06 m3/s\n",

-        "Cylinder can be used for 4.381e+06 s nearly 50.7 days\n"

-       ]

-      }

-     ],

-     "prompt_number": 80

-    },

-    {

-     "cell_type": "heading",

-     "level": 2,

-     "metadata": {},

-     "source": [

-      "Example Problem 17.8, Page Number 431"

-     ]

-    },

-    {

-     "cell_type": "code",

-     "collapsed": false,

-     "input": [

-      "from math import sqrt,pi\n",

-      "\n",

-      "#Variable Declaration\n",

-      "eta = 0.891                 #Viscosity of hemoglobin in water, cP\n",

-      "T = 298.0                   #Temperature, K\n",

-      "k = 1.3806488e-23           #Boltzmanconstant,J K^-1\n",

-      "R = 8.314                   #Molar Gas constant,  mol^-1 K^-1\n",

-      "D = 6.9e-11                 #Diffusion coefficient, m2/s \n",

-      "\n",

-      "#Calculations\n",

-      "r = k*T/(6*pi*eta*1e-3*D)\n",

-      "\n",

-      "#Results\n",

-      "print 'Radius of protein is %4.3f nm'%(r/1e-9)"

-     ],

-     "language": "python",

-     "metadata": {},

-     "outputs": [

-      {

-       "output_type": "stream",

-       "stream": "stdout",

-       "text": [

-        "Radius of protein is 3.550 nm\n"

-       ]

-      }

-     ],

-     "prompt_number": 54

-    },

-    {

-     "cell_type": "heading",

-     "level": 2,

-     "metadata": {},

-     "source": [

-      "Example Problem 17.9, Page Number 432"

-     ]

-    },

-    {

-     "cell_type": "code",

-     "collapsed": false,

-     "input": [

-      "from math import sqrt,pi\n",

-      "\n",

-      "#Variable Declaration\n",

-      "s = 1.91e-13                #Sedimentation constant, s\n",

-      "NA = 6.02214129e+23         #mol^-1\n",

-      "M = 14100.0                 #Molecualr wt of lysozyme, g/mol\n",

-      "rho = 0.998                 #Density of water, kg/m3\n",

-      "eta = 1.002                 #Viscosity lysozyme in water, cP\n",

-      "T = 293.15                  #Temperature, K\n",

-      "vbar = 0.703                #Specific volume of cm3/g\n",

-      "\n",

-      "#Calculations\n",

-      "m = M/NA\n",

-      "f = m*(1.-vbar*rho)/s\n",

-      "r = f/(6*pi*eta)\n",

-      "\n",

-      "#Results\n",

-      "print 'Radius of Lysozyme particle is %4.3f nm'%(r/1e-9)"

-     ],

-     "language": "python",

-     "metadata": {},

-     "outputs": [

-      {

-       "output_type": "stream",

-       "stream": "stdout",

-       "text": [

-        "Radius of Lysozyme particle is 1.937 nm\n"

-       ]

-      }

-     ],

-     "prompt_number": 56

-    },

-    {

-     "cell_type": "heading",

-     "level": 2,

-     "metadata": {},

-     "source": [

-      "Example Problem 17.10, Page Number 433"

-     ]

-    },

-    {

-     "cell_type": "code",

-     "collapsed": false,

-     "input": [

-      "from numpy import arange,array,ones,linalg,log, exp\n",

-      "from pylab import plot,show\n",

-      "\n",

-      "\n",

-      "#Variable Declaration\n",

-      "t = array([0.0,30.0,60.0,90.0,120.0,150.0])       #Time, min\n",

-      "xb = array([6.00,6.07,6.14,6.21,6.28,6.35])       #Location of boundary layer, cm\n",

-      "rpm = 55000.                                      #RPM of centrifuge \n",

-      "\n",

-      "#Calculations\n",

-      "nx = xb/xb[0]\n",

-      "lnx = log(nx)\n",

-      "A = array([ t, ones(size(t))])\n",

-      "# linearly generated sequence\n",

-      "[slope, intercept] = linalg.lstsq(A.T,lnx)[0] # obtaining the parameters\n",

-      "# Use w[0] and w[1] for your calculations and give good structure to this ipython notebook\n",

-      "# plotting the line\n",

-      "line = slope*t+intercept # regression line\n",

-      "#Results\n",

-      "plot(t,line,'-',t,lnx,'o')\n",

-      "xlabel('Time, min')\n",

-      "ylabel('log(xb/xb0)')\n",

-      "show()\n",

-      "sbar = (slope/60)/(rpm*2*pi/60)**2\n",

-      "print 'Slope is %6.2e 1/min or %4.3e 1/s '%(slope, slope/60)\n",

-      "print 'Sedimentation factor is %4.3e s'%(sbar)"

-     ],

-     "language": "python",

-     "metadata": {},

-     "outputs": [

-      {

-       "metadata": {},

-       "output_type": "display_data",

-       "png": 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-       "text": [

-        "<matplotlib.figure.Figure at 0x850c3d0>"

-       ]

-      },

-      {

-       "output_type": "stream",

-       "stream": "stdout",

-       "text": [

-        "Slope is 3.78e-04 1/min or 6.299e-06 1/s \n",

-        "Sedimentation factor is 1.899e-13 s\n"

-       ]

-      }

-     ],

-     "prompt_number": 67

-    },

-    {

-     "cell_type": "heading",

-     "level": 2,

-     "metadata": {},

-     "source": [

-      "Example Problem 17.11, Page Number 439"

-     ]

-    },

-    {

-     "cell_type": "code",

-     "collapsed": false,

-     "input": [

-      "from math import sqrt,pi\n",

-      "\n",

-      "#Variable Declaration\n",

-      "LMg = 0.0106                #Ionic conductance for Mg, S.m2/mol\n",

-      "LCl = 0.0076                #Ionic conductance for Cl, S.m2/mol\n",

-      "nMg, nCl = 1, 2             #Coefficients of Mg and Cl  \n",

-      "\n",

-      "\n",

-      "#Calculations\n",

-      "LMgCl2 = nMg*LMg + nCl*LCl\n",

-      "\n",

-      "#Results\n",

-      "print 'Molar conductivity of MgCl2 on infinite dilution is %5.4f S.m2/mol'%(LMgCl2)"

-     ],

-     "language": "python",

-     "metadata": {},

-     "outputs": [

-      {

-       "output_type": "stream",

-       "stream": "stdout",

-       "text": [

-        "Molar conductivity of MgCl2 on infinite dilution is 0.0258 S.m2/mol\n"

-       ]

-      }

-     ],

-     "prompt_number": 59

-    }

-   ],

-   "metadata": {}

-  }

- ]

-}
\ No newline at end of file