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| author | debashisdeb | 2014-06-20 15:42:42 +0530 |
|---|---|---|
| committer | debashisdeb | 2014-06-20 15:42:42 +0530 |
| commit | 83c1bfceb1b681b4bb7253b47491be2d8b2014a1 (patch) | |
| tree | f54eab21dd3d725d64a495fcd47c00d37abed004 /Fundamentals_of_Heat_and_Mass_Transfer/Chapter_11.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_11.ipynb')
| -rw-r--r-- | Fundamentals_of_Heat_and_Mass_Transfer/Chapter_11.ipynb | 16 |
1 files changed, 2 insertions, 14 deletions
diff --git a/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_11.ipynb b/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_11.ipynb index 97945574..b185ed9e 100644 --- a/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_11.ipynb +++ b/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_11.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:ab6cb233ee6afa8e8253b650d9b15125740d73ba571b9d5b3c9431dc16631f9d" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,9 +28,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#Variable Initialization\n", "\n", - "# Tube Length to achieve a desired hot fluid temperature\n", "import math\n", "#Operating Conditions\n", "Tho = 60+273 \t\t\t\t\t\t\t;#[K] Hot Fluid outlet Temperature\n", @@ -110,10 +109,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#Variable Initialization\n", "\n", - "# Exterior Dimensions of heat Exchanger\n", - "# Pressure drops within the plate-type Heat exchanger with N=60 gaps\n", "import math\n", "import numpy\n", "from numpy import linspace\n", @@ -236,7 +232,6 @@ "collapsed": false, "input": [ "\n", - "# Required gas side surface area\n", "\n", "#Operating Conditions\n", "Tho = 100+273. \t\t\t\t;#[K] Hot Fluid outlet Temperature\n", @@ -300,9 +295,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#Variable Initialization\n", "\n", - "# Heat Transfer Rate and Fluid Outlet Temperatures\n", "\n", "#Operating Conditions\n", "Thi = 250+273. \t\t\t;#[K] Hot Fluid intlet Temperature\n", @@ -375,10 +368,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#Variable Initialization\n", "\n", - "# Outlet Temperature of cooling Water\n", - "# Tube length per pass to achieve required heat transfer\n", "import math\n", "#Operating Conditions\n", "q = 2*math.pow(10,9) \t \t\t\t;#[W] Heat transfer Rate\n", @@ -448,9 +438,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#Variable Initialization\n", "\n", - "# Gas-side overall heat transfer coefficient. Heat exchanger Volume\n", "import math\n", "#Operating Conditions\n", "hc = 1500. \t\t\t\t\t\t\t\t;#[W/m^2.K] Coefficient of heat transfer for outer surface\n", |