add books

3 files changed, 653 insertions, 0 deletions

diff --git a/sample_notebooks/AjaySatish/Sample_H.S._Fogler.ipynb b/sample_notebooks/AjaySatish/Sample_H.S._Fogler.ipynb
new file mode 100755
index 00000000..51134ef9
--- /dev/null
+++ b/sample_notebooks/AjaySatish/Sample_H.S._Fogler.ipynb
@@ -0,0 +1,231 @@
+{
+ "metadata": {
+  "celltoolbar": "Raw Cell Format",
+  "name": "",
+  "signature": "sha256:ef32575f9668e7c75384fec9d19e3d17f6260e600de2d26c9157520e2a39253b"
+ },
+ "nbformat": 3,
+ "nbformat_minor": 0,
+ "worksheets": [
+  {
+   "cells": [
+    {
+     "cell_type": "heading",
+     "level": 1,
+     "metadata": {},
+     "source": [
+      "ELEMENTS OF CHEMICAL ENGINEERING BY H.S. FOGLER"
+     ]
+    },
+    {
+     "cell_type": "heading",
+     "level": 1,
+     "metadata": {},
+     "source": [
+      "CHAPTER NUMBER 1 : MOLE BALANCES"
+     ]
+    },
+    {
+     "cell_type": "heading",
+     "level": 2,
+     "metadata": {},
+     "source": [
+      "EXAMPLE NUMBER 1.3"
+     ]
+    },
+    {
+     "cell_type": "code",
+     "collapsed": false,
+     "input": [
+      "import math\n",
+      "k = 0.23; #min**-1\n",
+      "v0 = 10;#dm**3/min\n",
+      "#CA = 0.1*CA0;\n",
+      "V = (v0/k)*math.log(1/0.1);\n",
+      "print \"V =\",round(V,4),\"dm**3\""
+     ],
+     "language": "python",
+     "metadata": {},
+     "outputs": [
+      {
+       "output_type": "stream",
+       "stream": "stdout",
+       "text": [
+        "V = 100.1124 dm**3\n"
+       ]
+      }
+     ],
+     "prompt_number": 9
+    },
+    {
+     "cell_type": "heading",
+     "level": 2,
+     "metadata": {},
+     "source": [
+      "CHAPTER NUMBER 2 : CONVERSION AND REACTOR SIZING"
+     ]
+    },
+    {
+     "cell_type": "heading",
+     "level": 2,
+     "metadata": {},
+     "source": [
+      "EXAMPLE NUMBER 2.1"
+     ]
+    },
+    {
+     "cell_type": "code",
+     "collapsed": false,
+     "input": [
+      "  \n",
+      "import math\n",
+      " \n",
+      "P0 = 10; #atm\n",
+      "yA0 = 0.5;\n",
+      "T0 = 422.2;#K\n",
+      "R = 0.082;# dm**3.atm/mol.K\n",
+      "v0 = 6;#dm**3/s\n",
+      "CA0=(yA0*P0)/(R*T0);\n",
+      "FA0 = CA0*v0;\n",
+      "print \"CA0 =\",round(CA0,4),\"mol/dm**3\"\n",
+      "print \"FA0 =\",round(FA0,4),\"mol/s\""
+     ],
+     "language": "python",
+     "metadata": {},
+     "outputs": [
+      {
+       "output_type": "stream",
+       "stream": "stdout",
+       "text": [
+        "CA0 = 0.1444 mol/dm**3\n",
+        "FA0 = 0.8665 mol/s\n"
+       ]
+      }
+     ],
+     "prompt_number": 10
+    },
+    {
+     "cell_type": "heading",
+     "level": 2,
+     "metadata": {},
+     "source": [
+      "EXAMPLE NUMBER 2.2"
+     ]
+    },
+    {
+     "cell_type": "code",
+     "collapsed": false,
+     "input": [
+      "import math\n",
+      "P0 = 10; #atm\n",
+      "yA0 = 0.5;\n",
+      "T0 = 422.2;#K\n",
+      "R = 0.082;# dm**3.atm/mol.K\n",
+      "v0 = 6;#dm**3/s\n",
+      "X = 0.8;\n",
+      "rA = -1/800;#1/-rA = 800#dm**3.s/mol\n",
+      "CA0=(yA0*P0)/(R*T0);\n",
+      "FA0 = CA0*v0;\n",
+      "V = FA0*X*(1/-rA)\n",
+      "print \"FA0 =\",round(FA0,4),\"mol/s\"\n",
+      "print \"V =\",round(V,4),\"dm**3\"\n"
+     ],
+     "language": "python",
+     "metadata": {},
+     "outputs": [
+      {
+       "output_type": "stream",
+       "stream": "stdout",
+       "text": [
+        "FA0 = 0.8665 mol/s\n",
+        "V = 0.6932 dm**3\n"
+       ]
+      }
+     ],
+     "prompt_number": 11
+    },
+    {
+     "cell_type": "heading",
+     "level": 2,
+     "metadata": {},
+     "source": [
+      "EXAMPLE NUMBER 2.3"
+     ]
+    },
+    {
+     "cell_type": "code",
+     "collapsed": false,
+     "input": [
+      "import math\n",
+      " \n",
+      "P0 = 10; #atm\n",
+      "yA0 = 0.5;\n",
+      "T0 = 422.2;#K\n",
+      "R = 0.082;# dm**3.atm/mol.K\n",
+      "v0 = 6;#dm**3/s\n",
+      "X = [0,0.1,0.2,0.3,0.4,0.5,0.6,0.7,0.8];\n",
+      "p = [189,192,200,222,250,303,400,556,800];#1/-rA = 800#dm**3.s/mols\n",
+      "CA0=(yA0*P0)/(R*T0);\n",
+      "FA0 = CA0*v0;\n",
+      "#V = FA0*X*(1/-rA)\n",
+      "\n",
+      "V = FA0*np.interp(0.42,X,p)\n",
+      "print \"FA0 =\",FA0,\"mol/s\"\n",
+      "print \"V =\",V,\"dm**3\""
+     ],
+     "language": "python",
+     "metadata": {},
+     "outputs": [
+      {
+       "output_type": "stream",
+       "stream": "stdout",
+       "text": [
+        "FA0 = 0.866541114487 mol/s\n",
+        "V = 225.820614435 dm**3\n"
+       ]
+      }
+     ],
+     "prompt_number": 21
+    },
+    {
+     "cell_type": "heading",
+     "level": 2,
+     "metadata": {},
+     "source": [
+      "EXAMPLE NUMBER 2.4"
+     ]
+    },
+    {
+     "cell_type": "code",
+     "collapsed": false,
+     "input": [
+      "import math\n",
+      "FA0 = 5; # mol/s\n",
+      "rAat=-0.0025;\n",
+      "X = [0,0.1,0.2,0.3,0.4,0.5,0.6];\n",
+      "p = [189,192,200,222,250,303,400];#1/-rA = 800#dm**3.s/mols\n",
+      "\n",
+      "VCSTR = FA0*X[6]*(1/-rAat);\n",
+      "VPFR = FA0*np.interp(0.00017,X,p)\n",
+      "print \"VCSTR =\",VCSTR,\"dm**3\"\n",
+      "print \"VPFR =\",VPFR,\"dm**3\""
+     ],
+     "language": "python",
+     "metadata": {},
+     "outputs": [
+      {
+       "output_type": "stream",
+       "stream": "stdout",
+       "text": [
+        "VCSTR = 1200.0 dm**3\n",
+        "VPFR = 945.0255 dm**3\n"
+       ]
+      }
+     ],
+     "prompt_number": 37
+    }
+   ],
+   "metadata": {}
+  }
+ ]
+}
\ No newline at end of file
diff --git a/sample_notebooks/AjaySatish/Sample_H.S._Fogler_UPDATED.ipynb b/sample_notebooks/AjaySatish/Sample_H.S._Fogler_UPDATED.ipynb
new file mode 100755
index 00000000..a2bda001
--- /dev/null
+++ b/sample_notebooks/AjaySatish/Sample_H.S._Fogler_UPDATED.ipynb
@@ -0,0 +1,231 @@
+{
+ "metadata": {
+  "celltoolbar": "Raw Cell Format",
+  "name": "",
+  "signature": "sha256:37859c50b0a22beb7e2005b729edef7d0375ee40d0e34f554e83e84af89eab44"
+ },
+ "nbformat": 3,
+ "nbformat_minor": 0,
+ "worksheets": [
+  {
+   "cells": [
+    {
+     "cell_type": "heading",
+     "level": 1,
+     "metadata": {},
+     "source": [
+      "ELEMENTS OF CHEMICAL ENGINEERING BY H.S. FOGLER"
+     ]
+    },
+    {
+     "cell_type": "heading",
+     "level": 1,
+     "metadata": {},
+     "source": [
+      "CHAPTER NUMBER 1 : MOLE BALANCES"
+     ]
+    },
+    {
+     "cell_type": "heading",
+     "level": 2,
+     "metadata": {},
+     "source": [
+      "EXAMPLE NUMBER 1.3 : PAGE NUMBER 15"
+     ]
+    },
+    {
+     "cell_type": "code",
+     "collapsed": false,
+     "input": [
+      "import math\n",
+      "k = 0.23; #min**-1\n",
+      "v0 = 10;#dm**3/min\n",
+      "#CA = 0.1*CA0;\n",
+      "V = (v0/k)*math.log(1/0.1);\n",
+      "print \"V =\",round(V,4),\"dm**3\""
+     ],
+     "language": "python",
+     "metadata": {},
+     "outputs": [
+      {
+       "output_type": "stream",
+       "stream": "stdout",
+       "text": [
+        "V = 100.1124 dm**3\n"
+       ]
+      }
+     ],
+     "prompt_number": 9
+    },
+    {
+     "cell_type": "heading",
+     "level": 1,
+     "metadata": {},
+     "source": [
+      "CHAPTER NUMBER 2 : CONVERSION AND REACTOR SIZING"
+     ]
+    },
+    {
+     "cell_type": "heading",
+     "level": 2,
+     "metadata": {},
+     "source": [
+      "EXAMPLE NUMBER 2.1 : PAGE NUMBER 38"
+     ]
+    },
+    {
+     "cell_type": "code",
+     "collapsed": false,
+     "input": [
+      "  \n",
+      "import math\n",
+      " \n",
+      "P0 = 10; #atm\n",
+      "yA0 = 0.5;\n",
+      "T0 = 422.2;#K\n",
+      "R = 0.082;# dm**3.atm/mol.K\n",
+      "v0 = 6;#dm**3/s\n",
+      "CA0=(yA0*P0)/(R*T0);\n",
+      "FA0 = CA0*v0;\n",
+      "print \"CA0 =\",round(CA0,4),\"mol/dm**3\"\n",
+      "print \"FA0 =\",round(FA0,4),\"mol/s\""
+     ],
+     "language": "python",
+     "metadata": {},
+     "outputs": [
+      {
+       "output_type": "stream",
+       "stream": "stdout",
+       "text": [
+        "CA0 = 0.1444 mol/dm**3\n",
+        "FA0 = 0.8665 mol/s\n"
+       ]
+      }
+     ],
+     "prompt_number": 10
+    },
+    {
+     "cell_type": "heading",
+     "level": 2,
+     "metadata": {},
+     "source": [
+      "EXAMPLE NUMBER 2.2 : PAGE NUMBER 42"
+     ]
+    },
+    {
+     "cell_type": "code",
+     "collapsed": false,
+     "input": [
+      "import math\n",
+      "P0 = 10; #atm\n",
+      "yA0 = 0.5;\n",
+      "T0 = 422.2;#K\n",
+      "R = 0.082;# dm**3.atm/mol.K\n",
+      "v0 = 6;#dm**3/s\n",
+      "X = 0.8;\n",
+      "rA = -1/800;#1/-rA = 800#dm**3.s/mol\n",
+      "CA0=(yA0*P0)/(R*T0);\n",
+      "FA0 = CA0*v0;\n",
+      "V = FA0*X*(1/-rA)\n",
+      "print \"FA0 =\",round(FA0,4),\"mol/s\"\n",
+      "print \"V =\",round(V,4),\"dm**3\"\n"
+     ],
+     "language": "python",
+     "metadata": {},
+     "outputs": [
+      {
+       "output_type": "stream",
+       "stream": "stdout",
+       "text": [
+        "FA0 = 0.8665 mol/s\n",
+        "V = 0.6932 dm**3\n"
+       ]
+      }
+     ],
+     "prompt_number": 11
+    },
+    {
+     "cell_type": "heading",
+     "level": 2,
+     "metadata": {},
+     "source": [
+      "EXAMPLE NUMBER 2.3 : PAGE NUMBER 44"
+     ]
+    },
+    {
+     "cell_type": "code",
+     "collapsed": false,
+     "input": [
+      "import math\n",
+      " \n",
+      "P0 = 10; #atm\n",
+      "yA0 = 0.5;\n",
+      "T0 = 422.2;#K\n",
+      "R = 0.082;# dm**3.atm/mol.K\n",
+      "v0 = 6;#dm**3/s\n",
+      "X = [0,0.1,0.2,0.3,0.4,0.5,0.6,0.7,0.8];\n",
+      "p = [189,192,200,222,250,303,400,556,800];#1/-rA = 800#dm**3.s/mols\n",
+      "CA0=(yA0*P0)/(R*T0);\n",
+      "FA0 = CA0*v0;\n",
+      "#V = FA0*X*(1/-rA)\n",
+      "\n",
+      "V = FA0*np.interp(0.42,X,p)\n",
+      "print \"FA0 =\",FA0,\"mol/s\"\n",
+      "print \"V =\",V,\"dm**3\""
+     ],
+     "language": "python",
+     "metadata": {},
+     "outputs": [
+      {
+       "output_type": "stream",
+       "stream": "stdout",
+       "text": [
+        "FA0 = 0.866541114487 mol/s\n",
+        "V = 225.820614435 dm**3\n"
+       ]
+      }
+     ],
+     "prompt_number": 21
+    },
+    {
+     "cell_type": "heading",
+     "level": 2,
+     "metadata": {},
+     "source": [
+      "EXAMPLE NUMBER 2.4 : PAGE NUMBER 46"
+     ]
+    },
+    {
+     "cell_type": "code",
+     "collapsed": false,
+     "input": [
+      "import math\n",
+      "FA0 = 5; # mol/s\n",
+      "rAat=-0.0025;\n",
+      "X = [0,0.1,0.2,0.3,0.4,0.5,0.6];\n",
+      "p = [189,192,200,222,250,303,400];#1/-rA = 800#dm**3.s/mols\n",
+      "\n",
+      "VCSTR = FA0*X[6]*(1/-rAat);\n",
+      "VPFR = FA0*np.interp(0.00017,X,p)\n",
+      "print \"VCSTR =\",VCSTR,\"dm**3\"\n",
+      "print \"VPFR =\",VPFR,\"dm**3\""
+     ],
+     "language": "python",
+     "metadata": {},
+     "outputs": [
+      {
+       "output_type": "stream",
+       "stream": "stdout",
+       "text": [
+        "VCSTR = 1200.0 dm**3\n",
+        "VPFR = 945.0255 dm**3\n"
+       ]
+      }
+     ],
+     "prompt_number": 37
+    }
+   ],
+   "metadata": {}
+  }
+ ]
+}
\ No newline at end of file
diff --git a/sample_notebooks/AjaySatish/Sample_H.S._Fogler_UPDATED_(1).ipynb b/sample_notebooks/AjaySatish/Sample_H.S._Fogler_UPDATED_(1).ipynb
new file mode 100755
index 00000000..2b950ef8
--- /dev/null
+++ b/sample_notebooks/AjaySatish/Sample_H.S._Fogler_UPDATED_(1).ipynb
@@ -0,0 +1,191 @@
+{
+ "metadata": {
+  "celltoolbar": "Raw Cell Format",
+  "name": "",
+  "signature": "sha256:6aa7321c51ecc68ee01a5bb4aa554a936a01c87ebd6725c56b8e0edb6adbcf78"
+ },
+ "nbformat": 3,
+ "nbformat_minor": 0,
+ "worksheets": [
+  {
+   "cells": [
+    {
+     "cell_type": "heading",
+     "level": 1,
+     "metadata": {},
+     "source": [
+      "ELEMENTS OF CHEMICAL ENGINEERING BY H.S. FOGLER"
+     ]
+    },
+    {
+     "cell_type": "heading",
+     "level": 1,
+     "metadata": {},
+     "source": [
+      "CHAPTER NUMBER 2 : CONVERSION AND REACTOR SIZING"
+     ]
+    },
+    {
+     "cell_type": "heading",
+     "level": 2,
+     "metadata": {},
+     "source": [
+      "EXAMPLE NUMBER 2.1 : PAGE NUMBER 38"
+     ]
+    },
+    {
+     "cell_type": "code",
+     "collapsed": false,
+     "input": [
+      "  \n",
+      "import math\n",
+      " \n",
+      "P0 = 10; #atm\n",
+      "yA0 = 0.5;\n",
+      "T0 = 422.2;#K\n",
+      "R = 0.082;# dm**3.atm/mol.K\n",
+      "v0 = 6;#dm**3/s\n",
+      "CA0=(yA0*P0)/(R*T0);\n",
+      "FA0 = CA0*v0;\n",
+      "print \"CA0 =\",round(CA0,4),\"mol/dm**3\"\n",
+      "print \"FA0 =\",round(FA0,4),\"mol/s\""
+     ],
+     "language": "python",
+     "metadata": {},
+     "outputs": [
+      {
+       "output_type": "stream",
+       "stream": "stdout",
+       "text": [
+        "CA0 = 0.1444 mol/dm**3\n",
+        "FA0 = 0.8665 mol/s\n"
+       ]
+      }
+     ],
+     "prompt_number": 10
+    },
+    {
+     "cell_type": "heading",
+     "level": 2,
+     "metadata": {},
+     "source": [
+      "EXAMPLE NUMBER 2.2 : PAGE NUMBER 42"
+     ]
+    },
+    {
+     "cell_type": "code",
+     "collapsed": false,
+     "input": [
+      "import math\n",
+      "P0 = 10; #atm\n",
+      "yA0 = 0.5;\n",
+      "T0 = 422.2;#K\n",
+      "R = 0.082;# dm**3.atm/mol.K\n",
+      "v0 = 6;#dm**3/s\n",
+      "X = 0.8;\n",
+      "rA = -1/800;#1/-rA = 800#dm**3.s/mol\n",
+      "CA0=(yA0*P0)/(R*T0);\n",
+      "FA0 = CA0*v0;\n",
+      "V = FA0*X*(1/-rA)\n",
+      "print \"FA0 =\",round(FA0,4),\"mol/s\"\n",
+      "print \"V =\",round(V,4),\"dm**3\"\n"
+     ],
+     "language": "python",
+     "metadata": {},
+     "outputs": [
+      {
+       "output_type": "stream",
+       "stream": "stdout",
+       "text": [
+        "FA0 = 0.8665 mol/s\n",
+        "V = 0.6932 dm**3\n"
+       ]
+      }
+     ],
+     "prompt_number": 11
+    },
+    {
+     "cell_type": "heading",
+     "level": 2,
+     "metadata": {},
+     "source": [
+      "EXAMPLE NUMBER 2.3 : PAGE NUMBER 44"
+     ]
+    },
+    {
+     "cell_type": "code",
+     "collapsed": false,
+     "input": [
+      "import math\n",
+      " \n",
+      "P0 = 10; #atm\n",
+      "yA0 = 0.5;\n",
+      "T0 = 422.2;#K\n",
+      "R = 0.082;# dm**3.atm/mol.K\n",
+      "v0 = 6;#dm**3/s\n",
+      "X = [0,0.1,0.2,0.3,0.4,0.5,0.6,0.7,0.8];\n",
+      "p = [189,192,200,222,250,303,400,556,800];#1/-rA = 800#dm**3.s/mols\n",
+      "CA0=(yA0*P0)/(R*T0);\n",
+      "FA0 = CA0*v0;\n",
+      "#V = FA0*X*(1/-rA)\n",
+      "\n",
+      "V = FA0*np.interp(0.42,X,p)\n",
+      "print \"FA0 =\",FA0,\"mol/s\"\n",
+      "print \"V =\",V,\"dm**3\""
+     ],
+     "language": "python",
+     "metadata": {},
+     "outputs": [
+      {
+       "output_type": "stream",
+       "stream": "stdout",
+       "text": [
+        "FA0 = 0.866541114487 mol/s\n",
+        "V = 225.820614435 dm**3\n"
+       ]
+      }
+     ],
+     "prompt_number": 21
+    },
+    {
+     "cell_type": "heading",
+     "level": 2,
+     "metadata": {},
+     "source": [
+      "EXAMPLE NUMBER 2.4 : PAGE NUMBER 46"
+     ]
+    },
+    {
+     "cell_type": "code",
+     "collapsed": false,
+     "input": [
+      "import math\n",
+      "FA0 = 5; # mol/s\n",
+      "rAat=-0.0025;\n",
+      "X = [0,0.1,0.2,0.3,0.4,0.5,0.6];\n",
+      "p = [189,192,200,222,250,303,400];#1/-rA = 800#dm**3.s/mols\n",
+      "\n",
+      "VCSTR = FA0*X[6]*(1/-rAat);\n",
+      "VPFR = FA0*np.interp(0.00017,X,p)\n",
+      "print \"VCSTR =\",VCSTR,\"dm**3\"\n",
+      "print \"VPFR =\",VPFR,\"dm**3\""
+     ],
+     "language": "python",
+     "metadata": {},
+     "outputs": [
+      {
+       "output_type": "stream",
+       "stream": "stdout",
+       "text": [
+        "VCSTR = 1200.0 dm**3\n",
+        "VPFR = 945.0255 dm**3\n"
+       ]
+      }
+     ],
+     "prompt_number": 37
+    }
+   ],
+   "metadata": {}
+  }
+ ]
+}
\ No newline at end of file