diff options
Diffstat (limited to 'Introduction_to_Heat_Transfer_by_S._K._Som/Chapter5.ipynb')
| -rw-r--r-- | Introduction_to_Heat_Transfer_by_S._K._Som/Chapter5.ipynb | 102 |
1 files changed, 94 insertions, 8 deletions
diff --git a/Introduction_to_Heat_Transfer_by_S._K._Som/Chapter5.ipynb b/Introduction_to_Heat_Transfer_by_S._K._Som/Chapter5.ipynb index 5b3d46e7..1751c7ce 100644 --- a/Introduction_to_Heat_Transfer_by_S._K._Som/Chapter5.ipynb +++ b/Introduction_to_Heat_Transfer_by_S._K._Som/Chapter5.ipynb @@ -38,6 +38,7 @@ } ], "source": [ + " \n", "import math \n", "from scipy.integrate import quad\n", " \n", @@ -73,7 +74,23 @@ "#Q is the rate of heat transfer\n", "print\"The rate of heat transfer in W/m of width is\"\n", "Q=hbarL*L*(T2-T1)\n", - "print\"Q=\",Q" + "print\"Q=\",Q\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n" ] }, { @@ -85,7 +102,7 @@ }, { "cell_type": "code", - "execution_count": 27, + "execution_count": 2, "metadata": { "collapsed": false }, @@ -102,6 +119,7 @@ } ], "source": [ + " \n", "import math\n", " \n", "print\"Introduction to heat transfer by S.K.Som, Chapter 5, Example 4\"\n", @@ -126,7 +144,18 @@ "#from an enrgy balance we can write as E=27.063*U**0.85*L*B*(Ts-Tinf)\n", "print\"The minimum flow velocity in m/s is\"\n", "U=(E/(27.063*L*B*(Ts-Tinf)))**(1/0.85)\n", - "print\"U=\",U" + "print\"U=\",U\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n" ] }, { @@ -138,7 +167,7 @@ }, { "cell_type": "code", - "execution_count": 1, + "execution_count": 3, "metadata": { "collapsed": false }, @@ -161,8 +190,10 @@ } ], "source": [ + " \n", "import math\n", " \n", + " \n", "print\"Introduction to heat transfer by S.K.Som, Chapter 5, Example 6\"\n", "#Air at 1atm pressure and temprature(Tin)=30°C enters a tube of 25mm diameter(D) with a velocity(U) of 10m/s\n", "D=0.025;#in metre\n", @@ -200,7 +231,25 @@ "k=0.0285;\n", "print\"Overall Nusselt number is \"\n", "NuL=hx*D/k\n", - "print\"NuL=\",NuL" + "print\"NuL=\",NuL\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n" ] }, { @@ -212,7 +261,7 @@ }, { "cell_type": "code", - "execution_count": 3, + "execution_count": 4, "metadata": { "collapsed": false }, @@ -236,6 +285,7 @@ } ], "source": [ + " \n", "import math\n", " \n", "print\"Introduction to heat transfer by S.K.Som, Chapter 5, Example 7\"\n", @@ -274,7 +324,21 @@ "#Q is the heat loss from the plate\n", "print\"The heat loss from the plate in W is\"\n", "Q=hbar*A*(Ts-Tinf)\n", - "print\"Q=\",Q" + "print\"Q=\",Q\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n" ] }, { @@ -306,6 +370,7 @@ } ], "source": [ + " \n", "import math\n", " \n", "print\"Introduction to heat transfer by S.K.Som, Chapter 5, Example 8\"\n", @@ -333,7 +398,28 @@ "#I is the current flow.\n", "print\"The current in Ampere is\"\n", "I=(Q/(R*L))**0.5\n", - "print\"I=\",I" + "print\"I=\",I\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n", + "\n" ] } ], |