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"cells": [
{
"cell_type": "heading",
"level": 1,
"metadata": {},
"source": [
"Chapter 12 : Compartment Models"
]
},
{
"cell_type": "heading",
"level": 2,
"metadata": {},
"source": [
"Example 12.1 page no : 289"
]
},
{
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"input": [
"\n",
"# Variables\n",
"tg = (8.*(9.-6)*(0.5)+11.*(15.-9)*(0.5))/((15.-6)*0.5) #sec\n",
"tl = 40. #sec\n",
"vg = 0.5\n",
"vl = 0.1;\n",
"\n",
"# Calculations\n",
"Vg = tg*vg;\n",
"Vl = tl*vl;\n",
"G = Vg*10\n",
"L = Vl*10\n",
"Stagnant = (100-G-L)\n",
"\n",
"# Results\n",
"print \" fraction of gas is %.f %%\"%(G)\n",
"print \" fraction of liquid is %.f %%\"%(L)\n",
"print \" fraction of Stangnant liquid is %.f %%\"%(Stagnant)\n"
],
"language": "python",
"metadata": {},
"outputs": [
{
"output_type": "stream",
"stream": "stdout",
"text": [
" fraction of gas is 50 %\n",
" fraction of liquid is 40 %\n",
" fraction of Stangnant liquid is 10 %\n"
]
}
],
"prompt_number": 1
},
{
"cell_type": "heading",
"level": 2,
"metadata": {},
"source": [
"Example 12.2 page no : 290"
]
},
{
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"collapsed": false,
"input": [
"\n",
"# Variables\n",
"CAo = 1.;\n",
"XA = 0.75 #present\n",
"CA = 1-XA;\n",
"\n",
"# Calculations\n",
"kt1 = (CAo-CA)/CA;\n",
"kt2 = 3*kt1; #volume is reduced by 1/3\n",
"CA_unconverted = 1./(kt2+1);\n",
"XA = 1-CA_unconverted #New XA after replacing the stirrer\n",
"\n",
"# Results\n",
"print \" New Conversion expected is %.1f %%\"%(XA*100)\n"
],
"language": "python",
"metadata": {},
"outputs": [
{
"output_type": "stream",
"stream": "stdout",
"text": [
" New Conversion expected is 90.0 %\n"
]
}
],
"prompt_number": 3
},
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"input": [],
"language": "python",
"metadata": {},
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