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-rw-r--r--Fluidization_Engineering/ch7.ipynb16
1 files changed, 5 insertions, 11 deletions
diff --git a/Fluidization_Engineering/ch7.ipynb b/Fluidization_Engineering/ch7.ipynb
index d666d2ab..aafc2f66 100644
--- a/Fluidization_Engineering/ch7.ipynb
+++ b/Fluidization_Engineering/ch7.ipynb
@@ -1,6 +1,7 @@
{
"metadata": {
- "name": ""
+ "name": "",
+ "signature": "sha256:8eb00dc3983a05f0d88bd9a81e8b022860563cdbf1df8dacf4157210feb1c3ce"
},
"nbformat": 3,
"nbformat_minor": 0,
@@ -27,9 +28,8 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "#Entrainment from Fine Particle Beds with High Freeboard\n",
"\n",
- "#Variable declaration\n",
+ "\n",
"rhog=5.51; #Density of gas in kg/m**3\n",
"rhos=1200; #Density of solid in kg/m**3\n",
"dpbar=130; #Average size of particles in micrometer\n",
@@ -72,9 +72,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "#Entrainment from Large Particle Beds with High Freeboard\n",
"\n",
- "#Variable declaration\n",
"x=0.2; #Fraction of fines in the bed\n",
"Gsstar=4.033320 #Rate of entrainment in kg/m**2s(from Exa.1)\n",
"\n",
@@ -110,9 +108,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "#Entrainment from Beds with a Wide Size Distribution of Solids\n",
"\n",
- "#Variable declaration\n",
"rhog=5.51; #Density of gas in kg/m**3\n",
"rhos=1200; #Density of solid in kg/m**3\n",
"uo=0.61; #Superficial gas velocity in m/s\n",
@@ -176,9 +172,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "#k* from Steady State Experiments\n",
"\n",
- "#Variable declaration\n",
"dp=[40,60,80,100,120]; #Diameter of particle in micrometer\n",
"uo=0.381; #Superficial gas velocity in m/s\n",
"\n",
@@ -242,7 +236,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "#Comparing Predictions for k*\n",
+ "\n",
"\n",
"import math\n",
"\n",
@@ -349,7 +343,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "#Entrainment from a Short Vessel Ht<TDH\n",
+ "\n",
"import math\n",
"\n",
"#Variable declaration\n",