Added(A)/Deleted(D) following books

 A  1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter10_1.ipynb
A  1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter12_1.ipynb
A  1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter13_1.ipynb
A  1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter14_1.ipynb
A  1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter15_1.ipynb
A  1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter16_1.ipynb
A  1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter1_1.ipynb
A  1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter2_1.ipynb
A  1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter6_1.ipynb
A  1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter7_1.ipynb
A  1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter8_1.ipynb
A  1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/chapter9_1.ipynb
A  1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/screenshots/Screenshot_from_2016-01-14_17:01:00_1.png
A  1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/screenshots/Screenshot_from_2016-01-14_17:01:25_1.png
A  1000_solved_Problems_in_Fluid_Mechanics_includes_Hydraulic_machines_by_K.Subramanya/screenshots/Screenshot_from_2016-01-14_17:02:44_1.png
A  Applied_Chemistry_by_Dr._Mrs.Trupti_Paradkar/chapter1.ipynb
A  Applied_Chemistry_by_Dr._Mrs.Trupti_Paradkar/chapter3.ipynb
A  Applied_Chemistry_by_Dr._Mrs.Trupti_Paradkar/screenshots/1.png
A  Applied_Chemistry_by_Dr._Mrs.Trupti_Paradkar/screenshots/2.png
A  Applied_Chemistry_by_Dr._Mrs.Trupti_Paradkar/screenshots/3.png
A  Basic_Mathematics_for_Electricity_and_Electronics_by_Arthur_Beiser/chapter10_1.ipynb
A  Basic_Mathematics_for_Electricity_and_Electronics_by_Arthur_Beiser/chapter11_1.ipynb
A  Basic_Mathematics_for_Electricity_and_Electronics_by_Arthur_Beiser/chapter12_1.ipynb
A  Basic_Mathematics_for_Electricity_and_Electronics_by_Arthur_Beiser/chapter13_1.ipynb
A  Basic_Mathematics_for_Electricity_and_Electronics_by_Arthur_Beiser/chapter14_1.ipynb
A  Basic_Mathematics_for_Electricity_and_Electronics_by_Arthur_Beiser/chapter15_1.ipynb
A  Basic_Mathematics_for_Electricity_and_Electronics_by_Arthur_Beiser/chapter1_1.ipynb
A  Basic_Mathematics_for_Electricity_and_Electronics_by_Arthur_Beiser/chapter2_1.ipynb
A  Basic_Mathematics_for_Electricity_and_Electronics_by_Arthur_Beiser/chapter3_1.ipynb
A  Basic_Mathematics_for_Electricity_and_Electronics_by_Arthur_Beiser/chapter4_1.ipynb
A  Basic_Mathematics_for_Electricity_and_Electronics_by_Arthur_Beiser/chapter5_1.ipynb
A  Basic_Mathematics_for_Electricity_and_Electronics_by_Arthur_Beiser/chapter6_1.ipynb
A  Basic_Mathematics_for_Electricity_and_Electronics_by_Arthur_Beiser/chapter7_1.ipynb
A  Basic_Mathematics_for_Electricity_and_Electronics_by_Arthur_Beiser/screenshots/Screenshot_from_2016-03-09_13:50:16.png
A  Basic_Mathematics_for_Electricity_and_Electronics_by_Arthur_Beiser/screenshots/Screenshot_from_2016-03-09_13:52:27.png
A  Basic_Mathematics_for_Electricity_and_Electronics_by_Arthur_Beiser/screenshots/Screenshot_from_2016-03-09_13:53:23.png
A  Introduction_To_Chemical_Engineering_Thermodynamics_by_G._Halder/Ch1.ipynb
A  Introduction_To_Chemical_Engineering_Thermodynamics_by_G._Halder/Ch10.ipynb
A  Introduction_To_Chemical_Engineering_Thermodynamics_by_G._Halder/Ch11.ipynb
A  Introduction_To_Chemical_Engineering_Thermodynamics_by_G._Halder/Ch12.ipynb
A  Introduction_To_Chemical_Engineering_Thermodynamics_by_G._Halder/Ch2.ipynb
A  Introduction_To_Chemical_Engineering_Thermodynamics_by_G._Halder/Ch3.ipynb
A  Introduction_To_Chemical_Engineering_Thermodynamics_by_G._Halder/Ch4.ipynb
A  Introduction_To_Chemical_Engineering_Thermodynamics_by_G._Halder/Ch5.ipynb
A  Introduction_To_Chemical_Engineering_Thermodynamics_by_G._Halder/Ch6.ipynb
A  Introduction_To_Chemical_Engineering_Thermodynamics_by_G._Halder/Ch7.ipynb
A  Introduction_To_Chemical_Engineering_Thermodynamics_by_G._Halder/Ch8.ipynb
A  Introduction_To_Chemical_Engineering_Thermodynamics_by_G._Halder/Ch9.ipynb
A  Introduction_To_Chemical_Engineering_Thermodynamics_by_G._Halder/screenshots/Ch9MolFracNMolVol.png
A  Introduction_To_Chemical_Engineering_Thermodynamics_by_G._Halder/screenshots/Ch9_molarFracNMolVol.png
A  Introduction_To_Chemical_Engineering_Thermodynamics_by_G._Halder/screenshots/ch10_consistency.png
A  Machine_Design_by_T._H._Wentzell,_P._E/README.txt
A  Microwaves_and_Radar_Principles_and_Applications_by_A._K._Maini/README.txt
A  Network_Analysis_and_Synthesis_by_B_R_Gupta/README.txt

1 files changed, 557 insertions, 0 deletions

diff --git a/Introduction_To_Chemical_Engineering_Thermodynamics_by_G._Halder/Ch4.ipynb b/Introduction_To_Chemical_Engineering_Thermodynamics_by_G._Halder/Ch4.ipynb
new file mode 100644
index 00000000..c3a0a66f
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+++ b/Introduction_To_Chemical_Engineering_Thermodynamics_by_G._Halder/Ch4.ipynb
@@ -0,0 +1,557 @@
+{
+ "cells": [
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "# Chapter 4  - Heat effects"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Example: 4.1 Page: 118"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 2,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "Example: 4.1 - Page: 118\n",
+      "\n",
+      "\n",
+      "Value of Qv is -326.40 kcal\n",
+      "\n"
+     ]
+    }
+   ],
+   "source": [
+    "from __future__ import division\n",
+    "print \"Example: 4.1 - Page: 118\\n\\n\"\n",
+    "\n",
+    "# Solution\n",
+    "\n",
+    "#*****Data*****#\n",
+    "Qp = -327## [kcal]\n",
+    "T = 27 + 273## [K]\n",
+    "R = 2*10**(-3)## [kcal/K mol]\n",
+    "#*************#\n",
+    "\n",
+    "# The reaction involved is:\n",
+    "# C2H5OH(l) + 3O2(g) = 2CO2(g) + 3H2O(l)\n",
+    "deltan = 2 - 3#\n",
+    "Qv = Qp - deltan*R*T## [kcal]\n",
+    "print \"Value of Qv is %.2f kcal\\n\"%(Qv)#"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Example: 4.2 Page: 119"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 3,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "Example: 4.2 - Page: 119\n",
+      "\n",
+      "\n",
+      "Heat produced in the reaction is -1019.9 kcal\n",
+      "\n"
+     ]
+    }
+   ],
+   "source": [
+    "print \"Example: 4.2 - Page: 119\\n\\n\"\n",
+    "\n",
+    "# Solution\n",
+    "\n",
+    "#*****Data*****#\n",
+    "# Mg + (1/2)O2 = MgO ...............(1)\n",
+    "deltaH1 = -610.01## [kcal]\n",
+    "# 2Fe + (3/2)O2 = Fe2O3 ............(2)\n",
+    "deltaH2 = -810.14## [kcal]\n",
+    "#*************#\n",
+    "\n",
+    "# 3Mg + Fe2O3 = 3MgO + 2Fe .........(3)\n",
+    "# Multiplying (1) by 3 and substracting from (2), we get (3):\n",
+    "deltaH = 3*deltaH1 - deltaH2## [kcal]\n",
+    "print \"Heat produced in the reaction is %.1f kcal\\n\"%(deltaH)#"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Example: 4.3 Page: 121"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 4,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "Example: 4.3 - Page: 121\n",
+      "\n",
+      "\n",
+      "The standard heat of formation of methane is -74.75 kJ/gmol\n",
+      "\n"
+     ]
+    }
+   ],
+   "source": [
+    "print \"Example: 4.3 - Page: 121\\n\\n\"\n",
+    "\n",
+    "# Solution\n",
+    "\n",
+    "#*****Data*****#\n",
+    "# 2H2(g) + O2(g) ---------------> 2H2O .....................(1)\n",
+    "deltaH1 = -241.8*2## [kJ/gmol H2]\n",
+    "# C(graphite) + O2(g) =---------> CO2(g) ...................(2)\n",
+    "deltaH2 = -393.51## [kJ/gmol C]\n",
+    "# CH4(g) + 2O2(g) ---------------> CO2(g) + 2H2O(l) ........(3)\n",
+    "deltaH3 = -802.36## [kJ/mol CH4]\n",
+    "#*************#\n",
+    "\n",
+    "# For standard heat of formation of methane, (a) + (b) - (c)\n",
+    "# C + 2H2 ------------------------> CH4\n",
+    "deltaHf = deltaH1 + deltaH2 - deltaH3## [kJ/gmol]\n",
+    "print \"The standard heat of formation of methane is %.2f kJ/gmol\\n\"%(deltaHf)#"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Example: 4.4 Page: 122"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 5,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "Example: 4.4 - Page: 122\n",
+      "\n",
+      "\n",
+      "Energy supplied by reaction A is -69.2 kJ\n",
+      "\n",
+      "Energy supplied by reaction B is -2802.8 kJ\n",
+      "\n",
+      "Reaction B supplies more energy to the organism\n",
+      "\n"
+     ]
+    }
+   ],
+   "source": [
+    "print \"Example: 4.4 - Page: 122\\n\\n\"\n",
+    "\n",
+    "# Solution\n",
+    "\n",
+    "#*****Data*****#\n",
+    "deltaH_C6H12O6 = -1273## [kcal]\n",
+    "deltaH_C2H5OH = -277.6## [kcal]\n",
+    "deltaH_CO2 = -393.5## [kcal]\n",
+    "deltaH_H2O = -285.8## [kcal]\n",
+    "#**************#\n",
+    "\n",
+    "# C6H12O6(s) = 2C2H5OH(l) + 2CO2(g) ..........................(A)\n",
+    "deltaH_A = 2*deltaH_C2H5OH + 2*deltaH_CO2 - deltaH_C6H12O6## [kJ]\n",
+    "# C6H12O6(s) + 6O2(g) = 6CO2(g) + 6H2O(l) ...................(B)\n",
+    "deltaH_B = 6*deltaH_CO2 + 6*deltaH_H2O - deltaH_C6H12O6## [kJ]\n",
+    "print \"Energy supplied by reaction A is %.1f kJ\\n\"%(deltaH_A)#\n",
+    "print \"Energy supplied by reaction B is %.1f kJ\\n\"%(deltaH_B)#\n",
+    "if deltaH_A < deltaH_B:\n",
+    "    print \"Reaction A supplies more energy to the organism\\n\"\n",
+    "else:\n",
+    "     print \"Reaction B supplies more energy to the organism\\n\"\n"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Example: 4.5 Page: 122"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 6,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "Example: 4.5 - Page: 122\n",
+      "\n",
+      "\n",
+      "Heat of formation of ZnSO4 is -233.48 kcal/kmol\n",
+      "\n"
+     ]
+    }
+   ],
+   "source": [
+    "print \"Example: 4.5 - Page: 122\\n\\n\"\n",
+    "\n",
+    "# Solution\n",
+    "\n",
+    "#*****Data*****#\n",
+    "# Zn + S = ZnS ....................................................(A)\n",
+    "deltaH_A = -44## [kcal/kmol]\n",
+    "# ZnS + 3O2 = 2ZnO + 2SO2 .........................................(B)\n",
+    "deltaH_B = -221.88## [kcal/kmol]\n",
+    "# 2SO2 + O2 = 2SO3 ................................................(C)\n",
+    "deltaH_C = -46.88## [kcal/kmol]\n",
+    "# ZnO + SO3 = ZnSO4 ...............................................(D)\n",
+    "deltaH_D = -55.10## [kcal/kmol]\n",
+    "#***************#\n",
+    "\n",
+    "# Multiplying (A) by 2 & (D) by (2) and adding (A), (B), (C) & (D)\n",
+    "# Zn + S + 2O2 = ZnSO4\n",
+    "deltaH = 2*deltaH_A + deltaH_B + deltaH_C + 2*deltaH_D## [kcal/kmol for 2 kmol of ZnSO4]\n",
+    "print \"Heat of formation of ZnSO4 is %.2f kcal/kmol\\n\"%(deltaH/2)#"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Example: 4.6 Page: 124"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 7,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "Example: 4.6 - Page: 124\n",
+      "\n",
+      "\n",
+      "Standard Heat of formation of NH3 is -11.8 kcal\n"
+     ]
+    }
+   ],
+   "source": [
+    "print \"Example: 4.6 - Page: 124\\n\\n\"\n",
+    "\n",
+    "# Solution\n",
+    "\n",
+    "#*****Data*****#\n",
+    "# HC : Heat of Combustion\n",
+    "HC_NH3 = -90.6## [kcal]\n",
+    "HC_H2 = -68.3## [kcal]\n",
+    "#*************#\n",
+    "\n",
+    "# Heat of combustion of NH3:\n",
+    "# 2NH3 + 3O = N2 + 3H2O ............................ (A)\n",
+    "# Heat of combustion of H2:\n",
+    "# H2 + O = H2O ..................................... (B)\n",
+    "# Multiplying (B) by 3 & substracting from (A), we get:\n",
+    "# 2NH3 = N2 + 3H2 .................................. (C)\n",
+    "# Hf : Heat of Formation\n",
+    "Hf_NH3 = -(2*HC_NH3 - 3*HC_H2)/2## [kcal]\n",
+    "print \"Standard Heat of formation of NH3 is %.1f kcal\"%(Hf_NH3)#"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Example: 4.7 Page: 125"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 8,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "Example: 4.7 - Page: 125\n",
+      "\n",
+      "\n",
+      "The maximum attainable temperature is 2566.2 K\n"
+     ]
+    }
+   ],
+   "source": [
+    "print \"Example: 4.7 - Page: 125\\n\\n\"\n",
+    "\n",
+    "# Solution\n",
+    "\n",
+    "#*****Data*****#\n",
+    "# HC : Heat of Combustion\n",
+    "HC_C2H2 = -310600# # [cal]\n",
+    "#**************#\n",
+    "\n",
+    "# C2H2 + (5/2)O2 = 2CO2 + H2O\n",
+    "Q = -HC_C2H2## [cal]\n",
+    "# The gases present in the flame zone after combustion are carbon dioxide, water vapor and the unreacted nitrogen of the air.\n",
+    "# Since (5/2) mole of oxygen were required for combustion, nitrogen required would be 10 mol.\n",
+    "# Hence the composition of the resultant gas would be 2 mol CO2, 1  ol H2 & 10 mol N2.\n",
+    "# Q = integrate('Cp(T)','T',T,298)#\n",
+    "# On integrating we get:\n",
+    "# Q = 84.52*(T - 298) + 18.3*10**(-3)*(T**2 - 298**2)\n",
+    "#deff('[y] = f(T)','y = Q - 84.52*(T - 298) - 18.3*10**(-3)*(T**2 - 298**2)')#\n",
+    "def f(T):\n",
+    "    y = Q - 84.52*(T - 298) - 18.3*10**(-3)*(T**2 - 298**2)\n",
+    "    return y\n",
+    "from scipy.optimize import fsolve\n",
+    "T = fsolve(f,7)## [K]\n",
+    "print \"The maximum attainable temperature is %.1f K\"%(T)#"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Example: 4.8 Page: 126"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 9,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "Example: 4.8 - Page: 126\n",
+      "\n",
+      "\n",
+      "The theoretical temperature of combustion is 1906 degree Celsius\n"
+     ]
+    }
+   ],
+   "source": [
+    "print \"Example: 4.8 - Page: 126\\n\\n\"\n",
+    "\n",
+    "# Solution\n",
+    "\n",
+    "#*****Data*****#\n",
+    "Cp_CO2 = 54.56## [kJ/mol K]\n",
+    "Cp_O2 = 35.20## [kJ/mol K]\n",
+    "Cp_steam = 43.38## [kJ/mol K]\n",
+    "Cp_N2 = 33.32## [kJ/mol K]\n",
+    "# 2C2H6(g) + 7O2(g) = 4CO2(g) + 6H2O(g)\n",
+    "deltaH_273 = -1560000## [kJ/kmol]\n",
+    "#************#\n",
+    "\n",
+    "# Since the air is 25% in excess of the amount required,the combustion may be written as:\n",
+    "# C2H6(g) + (7/2)O2(g) = 2CO2(g) + 3H2O(g)\n",
+    "# 25% excess air is supplied.\n",
+    "# Since the air contains N2 = 79% and O2 = 21%\n",
+    "# C2H6(g) + 3.5O2(g) + 0.25*3.5O2(g) + (4.375*(79/21))N2 = 2CO2 + 3H2O + 0.875O2 + 16.46N2 .................. (A)\n",
+    "# Considering the reaction (A),\n",
+    "# Amount of O2:\n",
+    "O2 = 3.5 + 3.5*0.25## [mol]\n",
+    "# Amount of N2 required:\n",
+    "N2 = 4.375*(79/21)## [mol]\n",
+    "# Let the initial temperature of ethane and air be 0 OC and the temperature of products of combustion be T OC\n",
+    "# Since heat librated by combustion = heat accumulated by combustion products\n",
+    "Q = -deltaH_273## [kJ/mol K]\n",
+    "T = Q/(2*Cp_CO2 + 3*Cp_steam + 0.875*Cp_O2 + N2*Cp_N2)## [OC]\n",
+    "print \"The theoretical temperature of combustion is %d degree Celsius\"%(T)#"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Example: 4.9 Page: 129"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 10,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "Example: 4.9 - Page: 129\n",
+      "\n",
+      "\n",
+      "Laten heat of ice at -20 OC is 1266 cal/mol\n",
+      "\n"
+     ]
+    }
+   ],
+   "source": [
+    "print \"Example: 4.9 - Page: 129\\n\\n\"\n",
+    "\n",
+    "# Solution\n",
+    "\n",
+    "#*****Data*****#\n",
+    "T1 = 273## [K]\n",
+    "T2 = 253## [K]\n",
+    "deltaH_273 = 1440## [cal/mol]\n",
+    "Cp = 8.7## [cal/mol]\n",
+    "#**************#\n",
+    "\n",
+    "deltaH_253 = deltaH_273 + Cp*(T2 - T1)## [cal/mol]\n",
+    "print \"Laten heat of ice at -20 OC is %d cal/mol\\n\"%(deltaH_253)#"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Example: 4.10 Page: 129"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 11,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "Example: 4.10 - Page: 129\n",
+      "\n",
+      "\n",
+      "Heat of formation at 1273 K is -11172 cal\n"
+     ]
+    }
+   ],
+   "source": [
+    "print \"Example: 4.10 - Page: 129\\n\\n\"\n",
+    "\n",
+    "# Solution\n",
+    "\n",
+    "#*****Data*****#\n",
+    "T2 = 1273## [K]\n",
+    "T1 = 300## [K]\n",
+    "deltaH_300 = -11030## [cal/mol]\n",
+    "#*************#\n",
+    "\n",
+    "# The chemical reaction involved is:\n",
+    "# N2 + 3H2 = 2NH3\n",
+    "# (1/2)N2 + (3/2)H2 = NH3\n",
+    "# deltaH_1273 = deltaH_300 + integrate('Cp_NH3(T) - (1/2)*Cp_N2(T) - (1/2)*Cp_H2(T)','T',1273,300)#\n",
+    "from sympy.mpmath import quad\n",
+    "deltaH_1273 = deltaH_300 + quad(lambda T:(6.2 + 7.8*10**(-3)*T - 7.2*10**(-6)*T**2) - (1/2)*(6.45 + 1.4*10**(-3)*T) - (1/2)*(6.94 - 0.2*10**(-3)*T),[1273,300])## [cal]\n",
+    "print \"Heat of formation at 1273 K is %d cal\"%(deltaH_1273)#"
+   ]
+  },
+  {
+   "cell_type": "markdown",
+   "metadata": {},
+   "source": [
+    "## Example: 4.11 Page: 130"
+   ]
+  },
+  {
+   "cell_type": "code",
+   "execution_count": 12,
+   "metadata": {
+    "collapsed": false
+   },
+   "outputs": [
+    {
+     "name": "stdout",
+     "output_type": "stream",
+     "text": [
+      "Example: 4.11 - Page: 130\n",
+      "\n",
+      "\n",
+      "Percent of excess air supplied is 39.9 %\n"
+     ]
+    }
+   ],
+   "source": [
+    "print \"Example: 4.11 - Page: 130\\n\\n\"\n",
+    "\n",
+    "# Solution\n",
+    "\n",
+    "#*****Data*****#\n",
+    "CO2 = 13.4## [percent by volume]\n",
+    "N2 = 80.5## [percent by volume]\n",
+    "O2 = 6.1## [percent by volume]\n",
+    "#*************#\n",
+    "\n",
+    "# Basis : 100 cubic m of flue gas.\n",
+    "Vol_N2_flue = N2## [Volume of Nitrogen in flue gas, cubic m]\n",
+    "Vol_O2_flue = O2## [Volume of O2 in flue gas, cubic m]\n",
+    "Vol_Air = N2/0.79## [Volume of air supplied, cubic m]\n",
+    "Vol_O2 = Vol_Air*0.21## [Volume of O2 in air supply, cubic m]\n",
+    "Vol_O2_cumbustion = Vol_O2 - Vol_O2_flue## [Volume of O2 used up in cumbustion of the fuel, cubic m]\n",
+    "Excess_Air = Vol_O2_flue/Vol_O2_cumbustion * 100## [percent of excess air supplied]\n",
+    "print \"Percent of excess air supplied is %.1f %%\"%(Excess_Air)#"
+   ]
+  }
+ ],
+ "metadata": {
+  "kernelspec": {
+   "display_name": "Python 2",
+   "language": "python",
+   "name": "python2"
+  },
+  "language_info": {
+   "codemirror_mode": {
+    "name": "ipython",
+    "version": 2
+   },
+   "file_extension": ".py",
+   "mimetype": "text/x-python",
+   "name": "python",
+   "nbconvert_exporter": "python",
+   "pygments_lexer": "ipython2",
+   "version": "2.7.9"
+  }
+ },
+ "nbformat": 4,
+ "nbformat_minor": 0
+}