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| author | debashisdeb | 2014-06-21 00:52:25 +0530 |
|---|---|---|
| committer | debashisdeb | 2014-06-21 00:52:25 +0530 |
| commit | 7c756fcc12d21693818e58f6936cab5b7c112868 (patch) | |
| tree | 009cb02ec85f4a75ac7b64239751f15361df2bfe /Physical_And_Chemical_Equilibrium_For_Chemical_Engineers/ch11.ipynb | |
| parent | 83c1bfceb1b681b4bb7253b47491be2d8b2014a1 (diff) | |
| download | Python-Textbook-Companions-7c756fcc12d21693818e58f6936cab5b7c112868.tar.gz Python-Textbook-Companions-7c756fcc12d21693818e58f6936cab5b7c112868.tar.bz2 Python-Textbook-Companions-7c756fcc12d21693818e58f6936cab5b7c112868.zip | |
Removed Problem Statements Completely
Diffstat (limited to 'Physical_And_Chemical_Equilibrium_For_Chemical_Engineers/ch11.ipynb')
| -rw-r--r-- | Physical_And_Chemical_Equilibrium_For_Chemical_Engineers/ch11.ipynb | 46 |
1 files changed, 9 insertions, 37 deletions
diff --git a/Physical_And_Chemical_Equilibrium_For_Chemical_Engineers/ch11.ipynb b/Physical_And_Chemical_Equilibrium_For_Chemical_Engineers/ch11.ipynb index 24212b64..f7d878eb 100644 --- a/Physical_And_Chemical_Equilibrium_For_Chemical_Engineers/ch11.ipynb +++ b/Physical_And_Chemical_Equilibrium_For_Chemical_Engineers/ch11.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:60047896579d8db89aebcb768a47215eec82ab7f225717125cd44a8e3788cb2b" }, "nbformat": 3, "nbformat_minor": 0, @@ -108,12 +109,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "'''\n", - "find\n", - "Mol water\n", - "Mol ethanol\n", - "Mol benzene\n", - "'''\n", + "\n", "import math \n", "\n", "Temp = 25. #[C]\n", @@ -168,11 +164,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "'''\n", - "find\n", - "Activity coefficient of benzene in water\n", - "Activity coefficient of water in benzene\n", - "'''\n", + "\n", "import math \n", "\n", "Temp = 25. #[C]\n", @@ -367,11 +359,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "'''\n", - "find\n", - "Heat of mixing of water-in-benzene\n", - "Heat of mixing of benzene-in-water\n", - "'''\n", + "\n", "import math \n", "\n", "R = 8.314 #[J/(ml*K)]\n", @@ -456,11 +444,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "'''\n", - "find\n", - "Ethanol's 0.1 mol distributed in the water rich phase\n", - "Ethanol's 0.1 mol distributed in the benzene rich phase\n", - "'''\n", + "\n", "\n", "from numpy import *\n", "from matplotlib.pyplot import *\n", @@ -527,11 +511,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "'''\n", - "find\n", - "Weight fraction of the NaCl in the saturated solution \n", - "Mol fraction of the NaCl in the saturated solution\n", - "'''\n", + "\n", "\n", "import math \n", "\n", @@ -577,11 +557,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "'''\n", - "find\n", - "Total amount of the solid left behind in the heater\n", - "Total amount of the solid left behind in the heater\n", - "'''\n", + "\n", "\n", "import math \n", "\n", @@ -630,11 +606,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "'''\n", - "find\n", - "Activity coefficient in benzene corresponding to practically ideal solution \n", - "Activity coefficient in CCl4 corresponding to mild type II behavior \n", - "'''\n", + "\n", "\n", "import math \n", "\n", |