summaryrefslogtreecommitdiff
path: root/sample_notebooks/AjaySatish/Sample_H.S._Fogler_UPDATED_(1).ipynb
diff options
context:
space:
mode:
authorThomas Stephen Lee2015-08-28 16:53:23 +0530
committerThomas Stephen Lee2015-08-28 16:53:23 +0530
commitdb0855dbeb41ecb8a51dde8587d43e5d7e83620f (patch)
treeb95975d958cba9af36cb1680e3f77205354f6512 /sample_notebooks/AjaySatish/Sample_H.S._Fogler_UPDATED_(1).ipynb
parent5a86a20b9de487553d4ef88719fb0fd76a5dd6a7 (diff)
downloadPython-Textbook-Companions-db0855dbeb41ecb8a51dde8587d43e5d7e83620f.tar.gz
Python-Textbook-Companions-db0855dbeb41ecb8a51dde8587d43e5d7e83620f.tar.bz2
Python-Textbook-Companions-db0855dbeb41ecb8a51dde8587d43e5d7e83620f.zip
add books
Diffstat (limited to 'sample_notebooks/AjaySatish/Sample_H.S._Fogler_UPDATED_(1).ipynb')
-rwxr-xr-xsample_notebooks/AjaySatish/Sample_H.S._Fogler_UPDATED_(1).ipynb191
1 files changed, 191 insertions, 0 deletions
diff --git a/sample_notebooks/AjaySatish/Sample_H.S._Fogler_UPDATED_(1).ipynb b/sample_notebooks/AjaySatish/Sample_H.S._Fogler_UPDATED_(1).ipynb
new file mode 100755
index 00000000..2b950ef8
--- /dev/null
+++ b/sample_notebooks/AjaySatish/Sample_H.S._Fogler_UPDATED_(1).ipynb
@@ -0,0 +1,191 @@
+{
+ "metadata": {
+ "celltoolbar": "Raw Cell Format",
+ "name": "",
+ "signature": "sha256:6aa7321c51ecc68ee01a5bb4aa554a936a01c87ebd6725c56b8e0edb6adbcf78"
+ },
+ "nbformat": 3,
+ "nbformat_minor": 0,
+ "worksheets": [
+ {
+ "cells": [
+ {
+ "cell_type": "heading",
+ "level": 1,
+ "metadata": {},
+ "source": [
+ "ELEMENTS OF CHEMICAL ENGINEERING BY H.S. FOGLER"
+ ]
+ },
+ {
+ "cell_type": "heading",
+ "level": 1,
+ "metadata": {},
+ "source": [
+ "CHAPTER NUMBER 2 : CONVERSION AND REACTOR SIZING"
+ ]
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "EXAMPLE NUMBER 2.1 : PAGE NUMBER 38"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ " \n",
+ "import math\n",
+ " \n",
+ "P0 = 10; #atm\n",
+ "yA0 = 0.5;\n",
+ "T0 = 422.2;#K\n",
+ "R = 0.082;# dm**3.atm/mol.K\n",
+ "v0 = 6;#dm**3/s\n",
+ "CA0=(yA0*P0)/(R*T0);\n",
+ "FA0 = CA0*v0;\n",
+ "print \"CA0 =\",round(CA0,4),\"mol/dm**3\"\n",
+ "print \"FA0 =\",round(FA0,4),\"mol/s\""
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "CA0 = 0.1444 mol/dm**3\n",
+ "FA0 = 0.8665 mol/s\n"
+ ]
+ }
+ ],
+ "prompt_number": 10
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "EXAMPLE NUMBER 2.2 : PAGE NUMBER 42"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "import math\n",
+ "P0 = 10; #atm\n",
+ "yA0 = 0.5;\n",
+ "T0 = 422.2;#K\n",
+ "R = 0.082;# dm**3.atm/mol.K\n",
+ "v0 = 6;#dm**3/s\n",
+ "X = 0.8;\n",
+ "rA = -1/800;#1/-rA = 800#dm**3.s/mol\n",
+ "CA0=(yA0*P0)/(R*T0);\n",
+ "FA0 = CA0*v0;\n",
+ "V = FA0*X*(1/-rA)\n",
+ "print \"FA0 =\",round(FA0,4),\"mol/s\"\n",
+ "print \"V =\",round(V,4),\"dm**3\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "FA0 = 0.8665 mol/s\n",
+ "V = 0.6932 dm**3\n"
+ ]
+ }
+ ],
+ "prompt_number": 11
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "EXAMPLE NUMBER 2.3 : PAGE NUMBER 44"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "import math\n",
+ " \n",
+ "P0 = 10; #atm\n",
+ "yA0 = 0.5;\n",
+ "T0 = 422.2;#K\n",
+ "R = 0.082;# dm**3.atm/mol.K\n",
+ "v0 = 6;#dm**3/s\n",
+ "X = [0,0.1,0.2,0.3,0.4,0.5,0.6,0.7,0.8];\n",
+ "p = [189,192,200,222,250,303,400,556,800];#1/-rA = 800#dm**3.s/mols\n",
+ "CA0=(yA0*P0)/(R*T0);\n",
+ "FA0 = CA0*v0;\n",
+ "#V = FA0*X*(1/-rA)\n",
+ "\n",
+ "V = FA0*np.interp(0.42,X,p)\n",
+ "print \"FA0 =\",FA0,\"mol/s\"\n",
+ "print \"V =\",V,\"dm**3\""
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "FA0 = 0.866541114487 mol/s\n",
+ "V = 225.820614435 dm**3\n"
+ ]
+ }
+ ],
+ "prompt_number": 21
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "EXAMPLE NUMBER 2.4 : PAGE NUMBER 46"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "import math\n",
+ "FA0 = 5; # mol/s\n",
+ "rAat=-0.0025;\n",
+ "X = [0,0.1,0.2,0.3,0.4,0.5,0.6];\n",
+ "p = [189,192,200,222,250,303,400];#1/-rA = 800#dm**3.s/mols\n",
+ "\n",
+ "VCSTR = FA0*X[6]*(1/-rAat);\n",
+ "VPFR = FA0*np.interp(0.00017,X,p)\n",
+ "print \"VCSTR =\",VCSTR,\"dm**3\"\n",
+ "print \"VPFR =\",VPFR,\"dm**3\""
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "VCSTR = 1200.0 dm**3\n",
+ "VPFR = 945.0255 dm**3\n"
+ ]
+ }
+ ],
+ "prompt_number": 37
+ }
+ ],
+ "metadata": {}
+ }
+ ]
+} \ No newline at end of file