diff options
Diffstat (limited to 'Elements_Of_Mass_Transfer_Part_1/ch3.ipynb')
| -rw-r--r-- | Elements_Of_Mass_Transfer_Part_1/ch3.ipynb | 27 |
1 files changed, 10 insertions, 17 deletions
diff --git a/Elements_Of_Mass_Transfer_Part_1/ch3.ipynb b/Elements_Of_Mass_Transfer_Part_1/ch3.ipynb index ab9df3da..42c74db2 100644 --- a/Elements_Of_Mass_Transfer_Part_1/ch3.ipynb +++ b/Elements_Of_Mass_Transfer_Part_1/ch3.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:3744cb249ffd9e10c950b9110990dfac9cd54ad63b8fe61f5671a88b4822fb4c" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,7 +28,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# rate of sublimation\n", "\n", "# Variable Declaration \n", "v=6.; #velocity in m/s\n", @@ -80,8 +80,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# rate of sublimation of solid naphthalene\n", - "\n", + " \n", "# Variable Declaration \n", "v=0.30; #velocity of parallelair in m/s\n", "t=300; #temperature of air in kelvin\n", @@ -134,8 +133,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#rate of absorption and mass transfer coefficient\n", - "# Variable Declaration \n", + " \n", "\n", "# a is CO2 and b is water\n", "p=2.; #total pressure at 1 in atm \n", @@ -192,8 +190,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# mass transfer coefficient and film thickness\n", - "# Variable Declaration \n", + " \n", "NA=7.5*10**-7; #mass flux in gmol/cm**2*s\n", "Dab=1.7*10**-5; #diffusivity if SO2 in water in cm**2/s\n", "c=1./18.02; #concentration is density/molecular weight in gmol/cm**2*s\n", @@ -241,8 +238,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# value of liquid and gas film coefficient\n", - "# Variable Declaration \n", + "\n", "Kg=2.72*10**-4; #overall gas phase mass transfer coefficient in kmol/m**2*S*atm\n", "r_gas=0.85*(1/Kg); #given that gas phase resisitance is 0.85 times overall resistance\n", "kg=1.0/r_gas; \n", @@ -304,10 +300,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# concentration of ammonia and interfacial partial pressure\n", - "# Variable Declaration \n", - "#kg/kl=0.9=t \n", - "#Pai=0.3672*Cai so; \n", + " \n", "m=0.3672;\n", "t=.9;\n", " #Pai and Cai indicates interfacial pressure and conc.\n", @@ -358,7 +351,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# diffusivity of gas overall transfer cofficient\n", + " \n", "# Variable Declaration \n", "D=.1;\n", "l=3; # l is length of bubble in cm\n", @@ -418,7 +411,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# overall gas phase mass transfer flux\n", + " \n", "# Variable Declaration \n", "Kg=7.36*10**-10;\n", "p=1.013*10**5;\n", @@ -543,7 +536,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# concentration of acid at outlet\n", + " \n", "# Variable Declaration \n", "Cas=1.521*10**-7;\n", "v=1525; #velocity in m/s\n", |