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"source": [
"Chapter 23 :\n",
"\n",
"Fluid-Fluid Reactions: Kinetics"
]
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"level": 2,
"metadata": {},
"source": [
"Example 23.1 pageno : 536"
]
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"input": [
"import math \n",
"\n",
"# Variables\n",
"k = 10.**6;\n",
"Kag_a = 0.01 #mol/hr. m**3. Pa\n",
"fl = 0.98;\n",
"Kal = 1.;\n",
"HA = 10.**5; # very low solubility\n",
"DAl = 10.**-6;\n",
"DBl = DAl;\n",
"PA = 5*10.**3 #Pa\n",
"CB = 100. #mol/m3\n",
"b = 2. \n",
"a = 20. #m2/m3\n",
"\n",
"# Calculations\n",
"Mh = math.sqrt(DAl*k*CB*CB)/Kal;\n",
"Ei = 1+(DBl*CB*HA/(b*DAl*PA));\n",
"E = 100.\n",
"print \" Part a\"\n",
"\n",
"res_total = (((1/(Kag_a))+(HA/(Kal*a*E))+(HA/(k*CB*CB*fl)))) #Total Resismath.tance\n",
"f_gas = (1/(Kag_a))/res_total; #fraction of resismath.tance in gas film\n",
"f_liq = (HA/(Kal*a*E))/res_total; #fraction of resismath.tance in liquid film\n",
"\n",
"\n",
"# Results\n",
"print \" Fraction of the resistance in the gas film is %f\"%(f_gas)\n",
"print \" Fraction of the resistance in the liquid film is %f\"%(f_liq)\n",
"print \" Part b\"\n",
"print \" The reaction zone is in the liquid film\"\n",
"print \" Part c\"\n",
"if Ei>5*Mh:\n",
" print \" We have pseudo 1st order reaction in the film\"\n",
"\n",
"rA = PA/(((1/(Kag_a))+(HA/(Kal*a*E))+(HA/(k*CB*CB*fl))));\n",
"print \" Part d\"\n",
"print \" The rate of reactionmol/m3.hr) is %f\"%(rA)\n"
],
"language": "python",
"metadata": {},
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"output_type": "stream",
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"text": [
" Part a\n",
" Fraction of the resistance in the gas film is 0.666667\n",
" Fraction of the resistance in the liquid film is 0.333333\n",
" Part b\n",
" The reaction zone is in the liquid film\n",
" Part c\n",
" We have pseudo 1st order reaction in the film\n",
" Part d\n",
" The rate of reactionmol/m3.hr) is 33.333331\n"
]
}
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"language": "python",
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