removing problem statements

1 files changed, 5 insertions, 27 deletions

diff --git a/Transport_Phenomena/ch10.ipynb b/Transport_Phenomena/ch10.ipynb
index 4df43e2b..46cf9990 100644
--- a/Transport_Phenomena/ch10.ipynb
+++ b/Transport_Phenomena/ch10.ipynb
@@ -1,6 +1,7 @@
 {
  "metadata": {
-  "name": ""
+  "name": "",
+  "signature": "sha256:d6e9db7edbf67f47d9db227a91c9a3e69bd0ea385086a570b1e5ec45fa366eb2"
  },
  "nbformat": 3,
  "nbformat_minor": 0,
@@ -27,7 +28,7 @@
      "cell_type": "code",
      "collapsed": false,
      "input": [
-      "# Compute the viscosity in CP.\n",
+      "\n",
       "\n",
       "import math \n",
       "\n",
@@ -82,7 +83,6 @@
      "cell_type": "code",
      "collapsed": false,
      "input": [
-      "# Compute the pressure drop for the same 0.032%in \n",
       "\n",
       "# Variables\n",
       "Nreold = 1214.;\n",
@@ -135,7 +135,7 @@
      "cell_type": "code",
      "collapsed": false,
      "input": [
-      "# Calculate the pressure drop in a pipe of 6-cm inside diameter for water flowing\n",
+      "\n",
       "\n",
       "# Variables\n",
       "u = 1./60;  \t\t\t #[m/sec] - velocity\n",
@@ -182,10 +182,7 @@
      "cell_type": "code",
      "collapsed": false,
      "input": [
-      "'''\n",
-      "Repeat the previous example for Reynolds numbers of 10 000 and\n",
-      "100 000. Contrast smooth pipe with commercial steel pipe and cast iron pipe.\n",
-      "'''\n",
+      "\n",
       "\n",
       "from numpy import *\n",
       "\n",
@@ -276,7 +273,6 @@
      "cell_type": "code",
      "collapsed": false,
      "input": [
-      "# Find, the maximum flow velocity by trial and error.\n",
       "\n",
       "# Variables\n",
       "L = 300.;  \t\t\t #[m] - length of pipe\n",
@@ -337,7 +333,6 @@
      "cell_type": "code",
      "collapsed": false,
      "input": [
-      "# Repeat Example 10.5 using the von Karman plot, Fig. 10.5.\n",
       "\n",
       "# Variables\n",
       "L = 300.;  \t\t\t #[m] - length of pipe\n",
@@ -385,7 +380,6 @@
      "cell_type": "code",
      "collapsed": false,
      "input": [
-      "# estimate the pressure drop in a 0.06-m ID commercial steel pipe at Reynolds numbers of 104 and 16\n",
       "\n",
       "# Variables\n",
       "L = 300.;  \t\t\t #[m] - length of pipe\n",
@@ -436,7 +430,6 @@
      "cell_type": "code",
      "collapsed": false,
      "input": [
-      "# Compute p, by (a) the equivalent length method and (b) the loss coefficient method.\n",
       "\n",
       "# Variables\n",
       "mu = 6.72*10**-4;  \t\t #[lb/ft*sec] - vismath.cosity\n",
@@ -510,7 +503,6 @@
      "cell_type": "code",
      "collapsed": false,
      "input": [
-      "# Determine the total flow rate of water through the pipe system.\n",
       "\n",
       "# Variables\n",
       "L1 = 50.;  \t\t\t #[m] - length of first pipe\n",
@@ -578,7 +570,6 @@
      "cell_type": "code",
      "collapsed": false,
      "input": [
-      "# find flow rate\n",
       "\n",
       "import math\n",
       "\n",
@@ -631,10 +622,6 @@
      "cell_type": "code",
      "collapsed": false,
      "input": [
-      "'''\n",
-      "Determine the pump size necessary to maintain a spray\n",
-      "velocity of 15 ft s-\u2019 and a flow rate of 400 gpm if the pump is 60 percent efficient.\n",
-      "'''\n",
       "\n",
       "# Variables\n",
       "sp = 1.1;\n",
@@ -741,7 +728,6 @@
      "cell_type": "code",
      "collapsed": false,
      "input": [
-      "# Estimate the power required in the previous problem by using the velocity head approximation\n",
       "\n",
       "# Variables\n",
       "kexit = 1.;\n",
@@ -819,8 +805,6 @@
      "cell_type": "code",
      "collapsed": false,
      "input": [
-      "# Determine the pressure drop over a length of 300 m if the flow velocity is 1.667 m\n",
-      "\n",
       "\n",
       "# Variables\n",
       "l = 0.09238;\n",
@@ -864,10 +848,6 @@
      "cell_type": "code",
      "collapsed": false,
      "input": [
-      "'''\n",
-      "Size a sharp-edged, corner-tap orifice meter for the 4-in. leg in\n",
-      "Fig. 10.17 if the flow rate and fluid are unchanged from Example 10.11.\n",
-      "'''\n",
       "\n",
       "# Variables\n",
       "Q = 400.;         \t\t\t #[gpm]\n",
@@ -934,7 +914,6 @@
      "cell_type": "code",
      "collapsed": false,
      "input": [
-      "# Size a venturi meter for the application cited in Example 10.15\n",
       "\n",
       "# Variables\n",
       "Q = 400.;     \t    \t\t        #[gpm]\n",
@@ -992,7 +971,6 @@
      "cell_type": "code",
      "collapsed": false,
      "input": [
-      "# Then compute the average velocity by Eq. (10.88) and compare with the 2.778 ft s-l as given.\n",
       "\n",
       "# Variables\n",
       "Uzmax = 3.455;  \t\t\t #[ft/sec]\n",