Added(A)/Deleted(D) following books

 M  Introduction_to_Heat_Transfer_by_S._K._Som/Chapter1.ipynb
M  Introduction_to_Heat_Transfer_by_S._K._Som/Chapter10.ipynb
M  Introduction_to_Heat_Transfer_by_S._K._Som/Chapter11.ipynb
M  Introduction_to_Heat_Transfer_by_S._K._Som/Chapter2.ipynb
M  Introduction_to_Heat_Transfer_by_S._K._Som/Chapter3.ipynb
M  Introduction_to_Heat_Transfer_by_S._K._Som/Chapter4.ipynb
M  Introduction_to_Heat_Transfer_by_S._K._Som/Chapter5.ipynb
M  Introduction_to_Heat_Transfer_by_S._K._Som/Chapter6.ipynb
M  Introduction_to_Heat_Transfer_by_S._K._Som/Chapter7.ipynb
M  Introduction_to_Heat_Transfer_by_S._K._Som/Chapter8.ipynb
M  Introduction_to_Heat_Transfer_by_S._K._Som/Chapter9.ipynb
M  Introduction_to_Heat_Transfer_by_S._K._Som/chapter12.ipynb

1 files changed, 19 insertions, 30 deletions

diff --git a/Introduction_to_Heat_Transfer_by_S._K._Som/Chapter1.ipynb b/Introduction_to_Heat_Transfer_by_S._K._Som/Chapter1.ipynb
index b36f371b..d3b728b1 100644
--- a/Introduction_to_Heat_Transfer_by_S._K._Som/Chapter1.ipynb
+++ b/Introduction_to_Heat_Transfer_by_S._K._Som/Chapter1.ipynb
@@ -57,7 +57,7 @@
   },
   {
    "cell_type": "code",
-   "execution_count": 2,
+   "execution_count": 3,
    "metadata": {
     "collapsed": false
    },
@@ -88,7 +88,7 @@
     "#The thickness of masonry wall is Lm.\n",
     "print\"The thickness of masonry wall is Lm in m\"\n",
     "Lm=(km/kc)*(Lc/(0.8))\n",
-    "print\"Lm=\",Lm\n"
+    "print\"Lm=\",Lm"
    ]
   },
   {
@@ -100,7 +100,7 @@
   },
   {
    "cell_type": "code",
-   "execution_count": 3,
+   "execution_count": 5,
    "metadata": {
     "collapsed": false
    },
@@ -139,7 +139,7 @@
   },
   {
    "cell_type": "code",
-   "execution_count": 4,
+   "execution_count": 6,
    "metadata": {
     "collapsed": false
    },
@@ -178,7 +178,7 @@
   },
   {
    "cell_type": "code",
-   "execution_count": 5,
+   "execution_count": 14,
    "metadata": {
     "collapsed": false
    },
@@ -189,9 +189,9 @@
      "text": [
       "Introduction to heat transfer by S.K.Som, Chapter 1, Example 6\n",
       "The rate of heat transfer from the plate is given by Q=hbr*A*(Ts-Tinf)\n",
-      "Q= 16000.0\n",
+      "Q= 224.0\n",
       "The rate of heat transfer can also be written in the form of Q=m*cp*|dT/dt| from an energy balance.\n",
-      "Q= 16000.0\n",
+      "Q= 224.0\n",
       "Equating the above two equations we get hbr=(m*cp*|dT/dt|)/(A*(Ts-Tinf)) in W/(m**2°C)\n",
       "hbr= 11.2\n"
      ]
@@ -220,21 +220,7 @@
     "print\"Q=\",Q\n",
     "print\"Equating the above two equations we get hbr=(m*cp*|dT/dt|)/(A*(Ts-Tinf)) in W/(m**2°C)\"\n",
     "hbr=(m*cp*10**3*X)/(A*(Ts-Tinf))\n",
-    "print\"hbr=\",hbr\n",
-    "\n",
-    "\n",
-    "\n",
-    "\n",
-    "\n",
-    "\n",
-    "\n",
-    "\n",
-    "\n",
-    "\n",
-    "\n",
-    "\n",
-    "\n",
-    "\n"
+    "print\"hbr=\",hbr"
    ]
   },
   {
@@ -246,7 +232,7 @@
   },
   {
    "cell_type": "code",
-   "execution_count": 6,
+   "execution_count": 2,
    "metadata": {
     "collapsed": false
    },
@@ -286,7 +272,7 @@
   },
   {
    "cell_type": "code",
-   "execution_count": 7,
+   "execution_count": 4,
    "metadata": {
     "collapsed": false
    },
@@ -312,7 +298,7 @@
     "print\"The emitted radiant energy per unit surface area is given by Eb/A=sigma*T**4 in W/m**2\"\n",
     "#Let Eb/A=F\n",
     "F=sigma*(50+273.15)**4\n",
-    "print\"F=\",F\n"
+    "print\"F=\",F"
    ]
   },
   {
@@ -324,7 +310,7 @@
   },
   {
    "cell_type": "code",
-   "execution_count": 8,
+   "execution_count": 4,
    "metadata": {
     "collapsed": false
    },
@@ -381,7 +367,7 @@
   },
   {
    "cell_type": "code",
-   "execution_count": 10,
+   "execution_count": 19,
    "metadata": {
     "collapsed": false
    },
@@ -390,9 +376,11 @@
      "name": "stdout",
      "output_type": "stream",
      "text": [
-      " Introduction to heat transfer by S.K.Som, Chapter 1, Example 10\n",
+      "Introduction to heat transfer by S.K.Som, Chapter 1, Example 10\n",
       "Heat transfer from the outer surface takes place only by radiation is given by Q/A=F1=emi*sigma*(T2**4-T0**4)in W/m**2 for different values of tempratures in K\n",
+      "F1= 332.029390022\n",
       "heat transfer from the outer surface can also be written as Q/A=F2=(Ti-To)/((1/hbri)+(L/k)+(1/hr)) in W/m**2 at different tempratures in K\n",
+      "F2= 332.132667923\n",
       "The values of temprature that are considered are <298 K\n",
       "Satisfactory solutions for Temprature in K is\n",
       "T2= 292.5\n",
@@ -425,7 +413,9 @@
     "#Radiation heat transfer coefficient(hr) is defined as Q/A=hr(T2-To)\n",
     "#so hr=4.536*10**-8*T2**3\n",
     "print\"Heat transfer from the outer surface takes place only by radiation is given by Q/A=F1=emi*sigma*(T2**4-T0**4)in W/m**2 for different values of tempratures in K\"\n",
+    "print\"F1=\",F1\n",
     "print\"heat transfer from the outer surface can also be written as Q/A=F2=(Ti-To)/((1/hbri)+(L/k)+(1/hr)) in W/m**2 at different tempratures in K\"\n",
+    "print\"F2=\",F2\n",
     "print\"The values of temprature that are considered are <298 K\"\n",
     "for i in range(285,292):\n",
     "    T2=i\n",
@@ -498,8 +488,7 @@
     "print\"The total heat loss by The pipe per unit length is given by Q/L=hbr*A*(T1-T2)+sigma*emi*A*(T1**4-T2**4) in W/m\"\n",
     "#Let Q/L=F\n",
     "F=hbr*A*((T1+273.15)-(T2+273.15))+sigma*emi*A*((T1+273.15)**4-(T2+273.15)**4)\n",
-    "print\"F=\",F\n",
-    "\n"
+    "print\"F=\",F"
    ]
   }
  ],