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author | debashisdeb | 2014-06-20 15:42:42 +0530 |
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committer | debashisdeb | 2014-06-20 15:42:42 +0530 |
commit | 83c1bfceb1b681b4bb7253b47491be2d8b2014a1 (patch) | |
tree | f54eab21dd3d725d64a495fcd47c00d37abed004 /Fundamentals_of_Heat_and_Mass_Transfer/Chapter_3.ipynb | |
parent | a78126bbe4443e9526a64df9d8245c4af8843044 (diff) | |
download | Python-Textbook-Companions-83c1bfceb1b681b4bb7253b47491be2d8b2014a1.tar.gz Python-Textbook-Companions-83c1bfceb1b681b4bb7253b47491be2d8b2014a1.tar.bz2 Python-Textbook-Companions-83c1bfceb1b681b4bb7253b47491be2d8b2014a1.zip |
removing problem statements
Diffstat (limited to 'Fundamentals_of_Heat_and_Mass_Transfer/Chapter_3.ipynb')
-rw-r--r-- | Fundamentals_of_Heat_and_Mass_Transfer/Chapter_3.ipynb | 29 |
1 files changed, 5 insertions, 24 deletions
diff --git a/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_3.ipynb b/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_3.ipynb index 80e4f209..4cf59010 100644 --- a/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_3.ipynb +++ b/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_3.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:ca8839cd8008ad44590694ea2ad13ce425811997673bf9c8b6a013454026c154" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,9 +28,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#Variable Initialization\n", "\n", - "# Find Skin Temperature & Aerogel Insulation Thickness \n", "import math\n", "A=1.8; \t\t\t\t\t# [m^2] Area for Heat transfer i.e. both surfaces\n", "Ti = 35+273.; \t\t\t\t#[K] - Inside Surface Temperature of Body\n", @@ -104,9 +103,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "#Variable Initialization\n", - "\n", - "# Chip Operating Temperature\n", "import math\n", "Tf = 25+273.; \t\t\t#[K] - Temperature of Fluid Flow\n", "L=.008; \t\t\t\t#[m] - Thickness of Aluminium \n", @@ -155,9 +151,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#Variable Initialization\n", "\n", - "# Find Thermal conductivity of Carbon Nanotube\n", "import math\n", "D = 14 * math.pow(10,-9); \t\t\t# [m]Dia of Nanotube\n", "s = 5*math.pow(10,-6); \t\t\t# [m]Distance between the islands\n", @@ -227,9 +221,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#Variable Initialization\n", "\n", - "# Temperature Distribution And Heat rate\n", "import math\n", "import numpy\n", "from numpy import linspace\n", @@ -287,9 +279,8 @@ "cell_type": "code", "collapsed": false, "input": [ - "#Variable Initialization\n", + "\n", "%pylab inline\n", - "# Critical Thickness\n", "import math\n", "import numpy\n", "from numpy import linspace\n", @@ -367,9 +358,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#Variable Initialization\n", - "\n", - "# Heat conduction through Spherical Container \n", + " \n", "import math\n", "k = .0017; \t\t\t\t\t\t#[W/m.K] From Table A.3, Silica Powder at Temp 300K\n", "h = 5; \t\t\t\t\t\t#[W/m^2.K]\n", @@ -430,9 +419,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#Variable Initialization\n", "\n", - "# Composite Plane wall\n", "import math\n", "\n", "Tsurr = 30+273.; \t\t\t\t\t\t#[K] Temperature of surrounding Water\n", @@ -489,7 +476,7 @@ "input": [ "#Variable Initialization\n", "%pylab inline\n", - "# Heat conduction through Rod\n", + "\n", "import math\n", "import numpy\n", "from numpy import linalg\n", @@ -595,9 +582,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#Variable Initialization\n", "\n", - "# Study of motorcycle finned cylinder\n", "import math\n", "H = .15; \t\t\t\t\t\t#[m] height\n", "k = 186; \t\t\t\t\t#[W/m.K] alumunium at 400K\n", @@ -659,9 +644,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#Variable Initialization\n", "\n", - "# Study of Fuel-cell fan system\n", "import math\n", "Wc =.05; \t\t\t\t#[m] width\n", "H = .026; \t \t\t\t\t#[m] height\n", @@ -737,9 +720,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#Variable Initialization\n", "\n", - "# Heat loss from body & temp at inner surface\n", "import math\n", "hair = 2.; \t\t\t#[W/m^2.K] Heat convection coefficient air\n", "hwater = 200.; \t\t#[W/m^2.K] Heat convection coefficient water\n", |