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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 /Fluidization_Engineering/ch17.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 'Fluidization_Engineering/ch17.ipynb')
| -rw-r--r-- | Fluidization_Engineering/ch17.ipynb | 9 |
1 files changed, 2 insertions, 7 deletions
diff --git a/Fluidization_Engineering/ch17.ipynb b/Fluidization_Engineering/ch17.ipynb index a51249d4..77951e94 100644 --- a/Fluidization_Engineering/ch17.ipynb +++ b/Fluidization_Engineering/ch17.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "ch17" + "name": "", + "signature": "sha256:82e0373b19da96ab8fd50304caf9cd3e08cf8bad10412b0998bf9110f7a5ae63" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,9 +28,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#Reactor Development Program\n", "\n", - "#Variable Declaration\n", "dt=[0.081,0.205,3.6]; #Reactor diameter for the three reactors in m\n", "dte=[0.04,0.12,0.70]; #Equivalent diameters for the three reactors in m\n", "db=[0.05,0.057,0.07]; #Estimated bubble size in the three reactors in m\n", @@ -201,9 +200,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#Design of a Commercial Acrylonitrile Reactor\n", "\n", - "#Variable Declaration\n", "deltaHr=5.15E8; #Heat of reaction in J/k mol\n", "W=5E4; #Weight of acrylonitirle produced per 334-day year in tonnes\n", "db=0.07; #Estimated bubble size in m\n", @@ -287,9 +284,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#Reactor-Regenerator with Circulating Catalyst: Catalytic Cracking\n", "\n", - "#Variable Declaration\n", "db=0.08; #Estimated bubble size in m\n", "dte=2; #Equivalent diameter in m\n", "F1=55.6; #Feed rate of oil in kg/s\n", |