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"source": [
"Chapter 4 : Introduction to Reactor Design"
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"metadata": {},
"source": [
"Example 4.1 page no : 88"
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"input": [
"\n",
"# Variables\n",
"a = 1.\n",
"b = 3.\n",
"c = 6.\n",
"#Initial concentrations\n",
"CAo = 100. # feed\n",
"CBo = 200. # feed\n",
"Cio = 100. # feed\n",
"#Final concentrations\n",
"CA = 40. # reacter exit\n",
"\n",
"# Calculations\n",
"# Find CB,XA,XB\n",
"ea = (6.-4.)/4;\n",
"XA = (CAo-CA)/(CAo+ea*CA);\n",
"eb = (ea*CBo)/(b*CAo);\n",
"XB = b*CAo*XA/CBo;\n",
"CB = CBo*(1-XB)/(1+eb*XB);\n",
"\n",
"# Results\n",
"print \"The final concentration of BCB is %.f\"%(CB)\n",
"print \" XA and XB are %.2f ,%.2f\"%(XA,XB)\n",
" \n"
],
"language": "python",
"metadata": {},
"outputs": [
{
"output_type": "stream",
"stream": "stdout",
"text": [
"The final concentration of BCB is 40\n",
" XA and XB are 0.50 ,0.75\n"
]
}
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