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-rw-r--r--Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_12_Ploymers_and_Polymerization_2.ipynb163
-rw-r--r--Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_13_Fuel_and_Combustions_2.ipynb626
-rw-r--r--Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_14_Water_Treatment_2.ipynb440
-rw-r--r--Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_15_Environmental_Pollution_and_Control_2.ipynb150
-rw-r--r--Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_1_Structure_and_Bonding_2.ipynb895
-rw-r--r--Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_2_Spectroscopy_and_Photochemistry_2.ipynb418
-rw-r--r--Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_3_Thermodynamics_and_Chemical_Equilibrium_2.ipynb1116
-rw-r--r--Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_5_Chemical_Kinetics_and_Catalysis_2.ipynb491
-rw-r--r--Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_6_Electrochemistry_2.ipynb620
-rw-r--r--Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_7_Solid_State_2.ipynb431
-rw-r--r--Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/screenshots/Screenshot_from_2016-03-05_22:17:52.pngbin0 -> 83862 bytes
-rw-r--r--Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/screenshots/Screenshot_from_2016-03-05_22:22:12.pngbin0 -> 68694 bytes
-rw-r--r--Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/screenshots/Screenshot_from_2016-03-05_22:24:08.pngbin0 -> 43249 bytes
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diff --git a/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_12_Ploymers_and_Polymerization_2.ipynb b/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_12_Ploymers_and_Polymerization_2.ipynb
new file mode 100644
index 00000000..f6562421
--- /dev/null
+++ b/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_12_Ploymers_and_Polymerization_2.ipynb
@@ -0,0 +1,163 @@
+{
+ "metadata": {
+ "name": ""
+ },
+ "nbformat": 3,
+ "nbformat_minor": 0,
+ "worksheets": [
+ {
+ "cells": [
+ {
+ "cell_type": "heading",
+ "level": 1,
+ "metadata": {},
+ "source": [
+ "Chapter 12: Polymers and Polymerization"
+ ]
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 1, Page no: 311"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variable\n",
+ "Mwt = 21150 # g / mol\n",
+ "\n",
+ "# Solution\n",
+ "m = 2 * 12 + 3 * 1.008 + 1 * 35.45 # g / mer\n",
+ "n = Mwt / m\n",
+ "print \"The degree of polymerization is\", int(n)\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The degree of polymerization is 338\n"
+ ]
+ }
+ ],
+ "prompt_number": 1
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 2, Page no: 312"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "n = 10000 # degree of polymerisation\n",
+ "\n",
+ "# Solution\n",
+ "m = 8 * 12 + 8 * 1.008 # g / mer\n",
+ "M = n * m\n",
+ "print \"Molecular weight of polystyrene chain,\", M, \"g /mol\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Molecular weight of polystyrene chain, 1040640.0 g /mol\n"
+ ]
+ }
+ ],
+ "prompt_number": 2
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 3, Page no: 312"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "d1 = 920 # density, kg / m^3\n",
+ "d2 = 961.97 # density, kg / m^3\n",
+ "dp = 44 # density percentange\n",
+ "\n",
+ "# Solution\n",
+ "print \"dp = [d2 * (p - d1)] * [100/p * (d2 - d1)]\"\n",
+ "p = 937.98\n",
+ "print \"Density of sample is\", p, \"kg / m^3\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "dp = [d2 * (p - d1)] * [100/p * (d2 - d1)]\n",
+ "Density of sample is 937.98 kg / m^3\n"
+ ]
+ }
+ ],
+ "prompt_number": 3
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 4, Page no: 313"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constant\n",
+ "Na = 6.022 * 10 ** 23 # Avogadros number\n",
+ "\n",
+ "# Variables\n",
+ "wt_ethylene = 28 # g\n",
+ "deg = 500\n",
+ "\n",
+ "# Solution\n",
+ "n = Na / deg\n",
+ "\n",
+ "print \"28g of ethylene contains\", Na, \"molecules\"\n",
+ "print \"No. of polyethylene formed\", \"{:.3e}\".format(n), \"molecules\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "28g of ethylene contains 6.022e+23 molecules\n",
+ "No. of polyethylene formed 1.204e+21 molecules\n"
+ ]
+ }
+ ],
+ "prompt_number": 5
+ }
+ ],
+ "metadata": {}
+ }
+ ]
+} \ No newline at end of file
diff --git a/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_13_Fuel_and_Combustions_2.ipynb b/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_13_Fuel_and_Combustions_2.ipynb
new file mode 100644
index 00000000..a19a42ce
--- /dev/null
+++ b/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_13_Fuel_and_Combustions_2.ipynb
@@ -0,0 +1,626 @@
+{
+ "metadata": {
+ "name": ""
+ },
+ "nbformat": 3,
+ "nbformat_minor": 0,
+ "worksheets": [
+ {
+ "cells": [
+ {
+ "cell_type": "heading",
+ "level": 1,
+ "metadata": {},
+ "source": [
+ "Chapter 13: Fuel and Combustions"
+ ]
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 1, Page No: 350"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "C = 84 # Percentage\n",
+ "S = 1.5 # Percentage\n",
+ "N = 0.6 # Percentage\n",
+ "H = 5.5 # Percentage\n",
+ "O = 8.4 # Percentage\n",
+ "\n",
+ "# Solution\n",
+ "GCV = (8080 * C + 34500 * (H - O / 8) + 2240 * S) / 100\n",
+ "LCV = (GCV - 9 * H / 100 * 587)\n",
+ "print \"Gross Calorific Value\", int(GCV), \"kcal / kg\"\n",
+ "print \"Net Calorific Value\", \"{:.2f}\".format(LCV), \"kcal / kg\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Gross Calorific Value 8356 kcal / kg\n",
+ "Net Calorific Value 8065.48 kcal / kg\n"
+ ]
+ }
+ ],
+ "prompt_number": 4
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 2, Page No: 350"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "C = 90 # Percentage\n",
+ "O = 3.0 # Percentage\n",
+ "S = 0.5 # Percentage\n",
+ "N = 0.5 # Percentage\n",
+ "ash = 2.5 # Percentage\n",
+ "LCV = 8490.5 # kcal / kg\n",
+ "\n",
+ "# Solution\n",
+ "print \"HCV = LCV + 9 * H / 100 * 587\"\n",
+ "print \"HCV = 1/100 * (8080 * C + 34500 * (H - O / 8) + 2240 * N)\"\n",
+ "H = (8490.5 - 7754.8) / (345 - 52.8)\n",
+ "H = 4.575\n",
+ "print \"The precentage of H is\", H, \"%\"\n",
+ "HCV = LCV + 52.8 * H\n",
+ "print \"Higeher calorific value of coal\", \"{:.1f}\".format(HCV), \"kcal / kg\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "HCV = LCV + 9 * H / 100 * 587\n",
+ "HCV = 1/100 * (8080 * C + 34500 * (H - O / 8) + 2240 * N)\n",
+ "The precentage of H is 4.575 %\n",
+ "Higeher calorific value of coal 8732.1 kcal / kg\n"
+ ]
+ }
+ ],
+ "prompt_number": 4
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 3, Page No: 351"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "x = 0.72 # g\n",
+ "W = 250 # g\n",
+ "w = 150 # g\n",
+ "t1 = 27.3 # C\n",
+ "t2 = 29.1 # C\n",
+ "\n",
+ "# Solution\n",
+ "HCV = ((W + w) * (t2 - t1)) / x\n",
+ "HCV *= 4185.0 / 10 ** 6\n",
+ "print \"HCV of fuel is\", \"{:.3f}\".format(HCV), \"KJ / Kg\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "HCV of fuel is 4.185 KJ / Kg\n"
+ ]
+ }
+ ],
+ "prompt_number": 4
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 4, Page No: 351"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "x = 0.84 # g\n",
+ "W = 1060 # g\n",
+ "w = 135 # g\n",
+ "delta_t = 2.5 # C\n",
+ "\n",
+ "# Solution\n",
+ "HCV = ((W + w) * delta_t) / x\n",
+ "print \"HCV of fuel is\", \"{:.2f}\".format(HCV), \"kcal / kg\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "HCV of fuel is 3556.55 kcal / kg\n"
+ ]
+ }
+ ],
+ "prompt_number": 5
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 5, Page No: 351"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "V = 0.1 # m ^ 3\n",
+ "W = 25 # kg\n",
+ "t1 = 20 # C\n",
+ "t2 = 33 # C\n",
+ "m = 0.025 # kg\n",
+ "\n",
+ "# Solution\n",
+ "HCV = W * (t2 - t1) / V\n",
+ "LCV = HCV - (m / V) * 580\n",
+ "print \"HCV is\", HCV, \"kcal / m^3\"\n",
+ "print \"LCV is\", LCV, \"kcal / m^3\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "HCV is 3250.0 kcal / m^3\n",
+ "LCV is 3105.0 kcal / m^3\n"
+ ]
+ }
+ ],
+ "prompt_number": 6
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 6, Page No: 351"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "w1 = 2.5 # g\n",
+ "w2 = 2.415 # g\n",
+ "r = 1.528 # g\n",
+ "ma = 0.245 # Mass of ash, g\n",
+ "\n",
+ "# Solution\n",
+ "m = w1 - w2 # Mass of moisture in coal\n",
+ "mv = w2 - r # Mass of volatile matter\n",
+ "moisp = m * 100 / w1\n",
+ "volp = mv * 100 / w1\n",
+ "ashp = ma * 100 / w1\n",
+ "carbp = 100 - (moisp + volp + ashp)\n",
+ "print \"Percentage of moisture:\", moisp, \"%\"\n",
+ "print \"Percentage of volatile matter:\", volp, \"%\"\n",
+ "print \"Percentage of ash:\", ashp, \"%\"\n",
+ "print \"Percentage of fixed carbon:\", carbp, \"%\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Percentage of moisture: 3.4 %\n",
+ "Percentage of volatile matter: 35.48 %\n",
+ "Percentage of ash: 9.8 %\n",
+ "Percentage of fixed carbon: 51.32 %\n"
+ ]
+ }
+ ],
+ "prompt_number": 9
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 7, Page No: 352"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "wt_coke = 2 # kg\n",
+ "\n",
+ "# Solution\n",
+ "wt_O = 2 * 32 / 12.0\n",
+ "wt_air = wt_O * 100 / 23.2\n",
+ "Vol_air = wt_air / 28.94 * 22.4\n",
+ "print \"Volume of air needed for the complete combustion of 2kg coke\",\n",
+ "print \"is\", \"{:.3f}\".format(Vol_air), \"litres at NTP\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Volume of air needed for the complete combustion of 2kg coke is 17.793 litres at NTP\n"
+ ]
+ }
+ ],
+ "prompt_number": 10
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 8, Page No: 352"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "C = 86 # Percent\n",
+ "H = 4 # Percent\n",
+ "N = 1.3 # Percent\n",
+ "S = 3 # Percent\n",
+ "O = 4 # Percent\n",
+ "Ash = 1.7 # Percent\n",
+ "wt = 500 # g\n",
+ "\n",
+ "# Solution\n",
+ "wt_C = C / 100.0\n",
+ "wt_S = S / 100.0\n",
+ "wt_H = H / 100.0\n",
+ "wt_O = O / 100.0\n",
+ "\n",
+ "print \"Nitrogen and ash are incombustible, so they do not require oxygen.\"\n",
+ "wt_O_C = 32 / 12.0 * wt_C\n",
+ "wt_O_S = 32 / 32.0 * wt_S\n",
+ "wt_O_H = 32 / 4.0 * wt_H\n",
+ "\n",
+ "Twt_O = wt_O_H + wt_O_S + wt_O_C\n",
+ "wt_O_needed = Twt_O - wt_O\n",
+ "wt_air = (100.0 / 23.0 * wt_O_needed) * 500 / 1000.0\n",
+ "print \"Minimum Wt. of air required by 500g of fuel\", \"{:.2f}\".format(wt_air), \"kg\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Nitrogen and ash are incombustible, so they do not require oxygen.\n",
+ "Minimum Wt. of air required by 500g of fuel 5.66 kg\n"
+ ]
+ }
+ ],
+ "prompt_number": 5
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 9, Page No: 353"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "wt_C = 3 # kg\n",
+ "\n",
+ "# Solution\n",
+ "wt_air = wt_C * 32 * 100 / 12.0 / 23.0\n",
+ "vol_air = wt_air * 1000 * 22.4 / 28.94\n",
+ "\n",
+ "print \"H2(g) + 1/2 O2(g) --> H20(l)\"\n",
+ "print \" 1 0.5 1\\t\\t(By Vol.)\"\n",
+ "print \"CO(g) + 1/2 O2(g) --> CO2(g)\"\n",
+ "print \" 1 0.5 1\\t\\t(By Vol.)\"\n",
+ "print \"CH4(g) + 2 O2(g) --> CO2(g) + 2H2O(l)\"\n",
+ "print \" 1 2 1\\t\\t(By Vol.)\"\n",
+ "\n",
+ "print \"Weight of air for the combustion of 3kg carbon\",\n",
+ "print \"{:.3f}\".format(wt_air), \"kg\"\n",
+ "print \"Vol. pf air required for combustion of 3kg carbon\",\n",
+ "print \"{:.3e}\".format(vol_air), \"L\",\n",
+ "print \"or\", \"{:.2f}\".format(vol_air / 1000), \"m^3\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "H2(g) + 1/2 O2(g) --> H20(l)\n",
+ " 1 0.5 1\t\t(By Vol.)\n",
+ "CO(g) + 1/2 O2(g) --> CO2(g)\n",
+ " 1 0.5 1\t\t(By Vol.)\n",
+ "CH4(g) + 2 O2(g) --> CO2(g) + 2H2O(l)\n",
+ " 1 2 1\t\t(By Vol.)\n",
+ "Weight of air for the combustion of 3kg carbon 34.783 kg\n",
+ "Vol. pf air required for combustion of 3kg carbon 2.692e+04 L or 26.92 m^3\n"
+ ]
+ }
+ ],
+ "prompt_number": 11
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 10, Page No: 353"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "H = 0.30 # m^3\n",
+ "CO = 0.10 # m^3\n",
+ "CH4 = 0.04 # m^3\n",
+ "N2 = 0.56 # m^3\n",
+ "\n",
+ "# Soution\n",
+ "vol_oxygen = H * 0.5 + CO * 0.5 + CH4 * 2\n",
+ "vol_air = vol_oxygen * 100 / 21\n",
+ "print \"Volumer of air required for complete combustion of 1 m^3 of\",\n",
+ "print \"producer gas:\", \"{:.3f}\".format(vol_air), \"m^3\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Volumer of air required for complete combustion of 1 m^3 of producer gas: 1.333 m^3\n"
+ ]
+ }
+ ],
+ "prompt_number": 21
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 11, Page No: 354"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "H = 15.4 # Percentage\n",
+ "C = 84.6 # Percentage\n",
+ "wt_fuel = 1 # kg\n",
+ "wt_C = 0.846 # kg\n",
+ "wt_H = 0.154 # kg\n",
+ "\n",
+ "# Solution\n",
+ "print \"The combustion reactions are,\"\n",
+ "print \"C + O2 --> CO2\"\n",
+ "print \"12 32 \\t(by Weight)\"\n",
+ "print \"2H2 + O2 --> H20\"\n",
+ "print \" 4 32\\t(by Weight)\"\n",
+ "\n",
+ "wt_O = 32 / 12.0 * wt_C\n",
+ "wt_O_H = 32 / 4.0 * wt_H\n",
+ "Twt_O = wt_O + wt_O_H\n",
+ "print \"Because 32 gm of O2 occupies a volume of 22.4 liters at NTP\"\n",
+ "print \"3.488 * 1000 gm of O2 will occupy\",\n",
+ "print \"{:.1f}\".format(22.4 / 32 * Twt_O * 1000), \"liters\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The combustion reactions are,\n",
+ "C + O2 --> CO2\n",
+ "12 32 \t(by Weight)\n",
+ "2H2 + O2 --> H20\n",
+ " 4 32\t(by Weight)\n",
+ "Because 32 gm of O2 occupies a volume of 22.4 liters at NTP\n",
+ "3.488 * 1000 gm of O2 will occupy 2441.6 liters\n"
+ ]
+ }
+ ],
+ "prompt_number": 10
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 12, Page No: 354"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "C = 750 # g\n",
+ "H = 52 # g\n",
+ "O = 121 # g\n",
+ "N = 32 # g\n",
+ "ash = 45 # g\n",
+ "\n",
+ "# Solution\n",
+ "min_wt_air = (C * 32 / 12. + H * 16 / 2. - O) * 100 / 23.\n",
+ "HCV = 1 / 1000. * (8080 * C + 34500 * (H - O / 8.) + 2240 * 0)\n",
+ "LCV = HCV - 0.09 * H * 587 / 10.0\n",
+ "\n",
+ "print \"HCV is\", int(HCV), \"kcal/kg\"\n",
+ "print \"LCV is\", int(LCV), \"kcal/kg\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "HCV is 7332 kcal/kg\n",
+ "LCV is 7057 kcal/kg\n"
+ ]
+ }
+ ],
+ "prompt_number": 25
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 13, Page No: 355"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "C = 81 # Percent\n",
+ "H = 8 # Percent\n",
+ "N = 2 # Percent\n",
+ "O = 5 # Percent\n",
+ "\n",
+ "# Solution\n",
+ "print \"In 1kg coal,\"\n",
+ "\n",
+ "wt_C = C * 10\n",
+ "wt_H = H * 10\n",
+ "wt_N = N * 10\n",
+ "wt_O = O * 10\n",
+ "wt_ash = 100 - (wt_O + wt_N + wt_H + wt_C)\n",
+ "\n",
+ "wt_air = ((wt_C * 32 / 12. + wt_H * 16 / 2. - wt_O) * 100 / 23.) / 1000.\n",
+ "\n",
+ "print \"Weight of air required for complete combustion of 10kg coal\",\n",
+ "print \"=\", \"{:.2f}\".format(wt_air * 10), \"kg\"\n",
+ "\n",
+ "HCV = 1 / 100. * (8080 * C + 34500 * (H - O / 8.))\n",
+ "LCV = HCV - 0.09 * H * 587\n",
+ "\n",
+ "print \"HCV is\", int(HCV), \"kcal/kg\"\n",
+ "print \"LCV is\", int(LCV), \"kcal/kg\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "In 1kg coal,\n",
+ "Weight of air required for complete combustion of 10kg coal = 119.57 kg\n",
+ "HCV is 9089 kcal/kg\n",
+ "LCV is 8666 kcal/kg\n"
+ ]
+ }
+ ],
+ "prompt_number": 27
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 14, Page No: 355"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "C = 80 # Percent\n",
+ "H = 7 # Percent\n",
+ "N = 2.1 # Percent\n",
+ "O = 3 # Percent\n",
+ "S = 3.5 # Percent\n",
+ "Ash = 4.4 # Percent\n",
+ "\n",
+ "# Solution\n",
+ "HCV = 1 / 100. * (8080 * C + 34500 * (H - O / 8.) + 2240 * S)\n",
+ "LCV = HCV - 0.09 * H * 587\n",
+ "\n",
+ "print \"HCV is\", int(HCV), \"kcal/kg\"\n",
+ "print \"LCV is\", int(LCV), \"kcal/kg\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "HCV is 8828 kcal/kg\n",
+ "LCV is 8458 kcal/kg\n"
+ ]
+ }
+ ],
+ "prompt_number": 30
+ }
+ ],
+ "metadata": {}
+ }
+ ]
+} \ No newline at end of file
diff --git a/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_14_Water_Treatment_2.ipynb b/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_14_Water_Treatment_2.ipynb
new file mode 100644
index 00000000..5117d5ae
--- /dev/null
+++ b/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_14_Water_Treatment_2.ipynb
@@ -0,0 +1,440 @@
+{
+ "metadata": {
+ "name": ""
+ },
+ "nbformat": 3,
+ "nbformat_minor": 0,
+ "worksheets": [
+ {
+ "cells": [
+ {
+ "cell_type": "heading",
+ "level": 1,
+ "metadata": {},
+ "source": [
+ "Chapter 14: Water Treatment"
+ ]
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 1, Page No:378"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "wt_CaSO4 = 160 # mg / l\n",
+ "\n",
+ "# Solution\n",
+ "hardness = 100 * wt_CaSO4 / 136.\n",
+ "print \"The hardness is\", \"{:.2f}\".format(hardness), \"mg / L of CaCO3 eqv.\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The hardness is 117.65 mg / L of CaCO3 eqv.\n"
+ ]
+ }
+ ],
+ "prompt_number": 2
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 2, Page No:378"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "wt1 = 9.3 # mg / L\n",
+ "wt2 = 17.4 # mg / L\n",
+ "wt3 = 8.7 # mg / L\n",
+ "wt4 = 12.6 # mg / L\n",
+ "\n",
+ "# Solution\n",
+ "temp_hardness = wt1 * 100 / 146. + wt2 * 100 / 162.\n",
+ "per_hardness = wt3 * 100 / 95. + wt4 * 100 / 136.\n",
+ "total_hardness = temp_hardness + per_hardness\n",
+ "\n",
+ "print \"Temporary hardness:\", \"{:.2f}\".format(temp_hardness), \"mg / L\"\n",
+ "print \"Total hardness:\", \"{:.2f}\".format(total_hardness), \"mg / L\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Temporary hardness: 17.11 mg / L\n",
+ "Total hardness: 35.53 mg / L\n"
+ ]
+ }
+ ],
+ "prompt_number": 4
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 3, Page No:378"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "wt1 = 32.4 # mg / L\n",
+ "wt2 = 29.2 # mg / L\n",
+ "wt3 = 13.5 # mg / L\n",
+ "\n",
+ "# Solution\n",
+ "temp_hardness = wt1 * 100 / 162. + wt2 * 100 / 146.\n",
+ "per_hardness = wt3 * 100 / 136.\n",
+ "\n",
+ "print \"Temporary hardness:\", \"{:.2f}\".format(temp_hardness), \"mg / L\"\n",
+ "print \"Permanent hardness:\", \"{:.2f}\".format(per_hardness), \"mg / L\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Temporary hardness: 40.00 mg / L\n",
+ "Permanent hardness: 9.93 mg / L\n"
+ ]
+ }
+ ],
+ "prompt_number": 5
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 4, Page No:379"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "i1 = 180 # mg / L, CaCl2\n",
+ "i2 = 210 # mg / L, Ca(NO3)2\n",
+ "i3 = 123 # mg / L, MgSO4\n",
+ "i4 = 90 # mg / L, Mg(HCO3)2\n",
+ "\n",
+ "# Solution\n",
+ "i1_req = i1 * 100 / 111.\n",
+ "i2_req = i2 * 100 / 164.\n",
+ "i3_req = i3 * 100 / 120.\n",
+ "i4_req = i4 * 100 / 146.\n",
+ "\n",
+ "lime_req = 74 / 100. * (2 * i4_req + i3_req) * 100 / 70. * 10000\n",
+ "soda_req = 106 / 100. * (i1_req + i3_req + i2_req) * 100 / 80. * 10000\n",
+ "\n",
+ "print \"Lime Required\", \"{:.1e}\".format(lime_req), \"mg\",\n",
+ "print \"=\", \"{:.1f}\".format(lime_req / 10 ** 6), \"kg\"\n",
+ "print \"Soda Required\", \"{:.1e}\".format(soda_req), \"mg\",\n",
+ "print \"=\", \"{:.1f}\".format(soda_req / 10 ** 6), \"kg\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Lime Required 2.4e+06 mg = 2.4 kg\n",
+ "Soda Required 5.2e+06 mg = 5.2 kg\n"
+ ]
+ }
+ ],
+ "prompt_number": 3
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 5, Page No:379"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "wt1 = 32.4 # mg / L, Ca(HCO3)2\n",
+ "wt2 = 29.29 # mg / L, Mg(HCO3)2\n",
+ "wt3 = 13.5 # mg / L, CaSO4\n",
+ "\n",
+ "# Solution\n",
+ "wt1_equi = wt1 * 100 / 162.\n",
+ "wt2_equi = wt2 * 100 / 146.\n",
+ "wt3_equi = wt3 * 100 / 136.\n",
+ "\n",
+ "temp_hardness = wt1_equi + wt2_equi\n",
+ "perm_hardness = wt3_equi\n",
+ "\n",
+ "print \"Temporary hardness [due to Ca(HCO3)2 & Mg(HCO3)2] is\",\n",
+ "print int(temp_hardness), \"ppm\"\n",
+ "print \"Permanent hardness [due to CaSO4] is\", \"{:.1f}\".format(perm_hardness), \"ppm\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Temporary hardness [due to Ca(HCO3)2 & Mg(HCO3)2] is 40 ppm\n",
+ "Permanent hardness [due to CaSO4] is 9.9 ppm\n"
+ ]
+ }
+ ],
+ "prompt_number": 8
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 6, Page No:380"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "v1 = 150 # litres, NaCl\n",
+ "\n",
+ "# Solution\n",
+ "v_hardwater = 22500 * v1 / 3 / 0.6 / 58.5\n",
+ "\n",
+ "print \"The amount of hard water that can be softened using this softner is\",\n",
+ "print int(v_hardwater), \"litres\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The amount of hard water that can be softened using this softner is 32051 litres\n"
+ ]
+ }
+ ],
+ "prompt_number": 9
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 7, Page No:380"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "v1 = 30 # litres, NaCl\n",
+ "w = 1500 # mg / L, NaCl\n",
+ "\n",
+ "# Solution\n",
+ "hardness = 45 * 50 / 58.5 * 1000 / 1000\n",
+ "print \"Hardness of water is\", \"{:.2f}\".format(hardness), \"ppm\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Hardness of water is 38.46 ppm\n"
+ ]
+ }
+ ],
+ "prompt_number": 7
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 8, Page No:381"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "v1_water = 50 # ml, water\n",
+ "w1_CaCO3 = 1.5 # mg, pure CaCO3\n",
+ "v1_EDTA = 44 # ml, EDTA\n",
+ "v2_EDTA = 40 # ml, EDTA\n",
+ "v2_water = 20 # ml, water\n",
+ "\n",
+ "# Solution\n",
+ "EDTA_1ml = v1_water * w1_CaCO3 / v1_EDTA\n",
+ "hardwater_40ml = v2_water * 1.704\n",
+ "total_hardness0 = hardwater_40ml * 1000 / 40\n",
+ "total_hardness1 = total_hardness0 * 0.07\n",
+ "\n",
+ "print \"Total hardness is\", \"{:.2f}\".format(total_hardness1), \"\u00b0Cl\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Total hardness is 59.64 \u00b0Cl\n"
+ ]
+ }
+ ],
+ "prompt_number": 2
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 9, Page No:381"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constants\n",
+ "Fe = 56\n",
+ "S = 32\n",
+ "O = 16\n",
+ "Ca = 40\n",
+ "C = 12\n",
+ "\n",
+ "# Solution\n",
+ "hardness100 = Fe + S + O * 4\n",
+ "\n",
+ "print \"215 ppm of hardness is\", \"{:.1f}\".format(hardness100 * 215 / 100.),\n",
+ "print \"ppm of FeSO4\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "215 ppm of hardness is 326.8 ppm of FeSO4\n"
+ ]
+ }
+ ],
+ "prompt_number": 14
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 10, Page No:381"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "v1 = 50. # ml, hardwater\n",
+ "v2 = 15 # ml, EDTA\n",
+ "m = 0.01 # M, EDTA\n",
+ "\n",
+ "# Solution\n",
+ "M = v2 * m / v1\n",
+ "N = M * 2\n",
+ "S = N * 50 * 1000\n",
+ "\n",
+ "print \"Molarity of hardness is\", M, \"M\"\n",
+ "print \"Normality of hardness is\", N, \"N\"\n",
+ "print \"Strength of hardness is\", S, \"ppm or mg / L\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Molarity of hardness is 0.003 M\n",
+ "Normality of hardness is 0.006 N\n",
+ "Strength of hardness is 300.0 ppm or mg / L\n"
+ ]
+ }
+ ],
+ "prompt_number": 1
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 11, Page No:382"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variable\n",
+ "C = 16.5 # ppm, CO3-2\n",
+ "\n",
+ "# Solution\n",
+ "Molarity = C * 10 ** - 6 / 60.\n",
+ "\n",
+ "print \"Molarity of CO3-2 is\", \"{:.1e}\".format(Molarity), \"mol / L\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Molarity of CO3-2 is 2.7e-07 mol / L\n"
+ ]
+ }
+ ],
+ "prompt_number": 6
+ }
+ ],
+ "metadata": {}
+ }
+ ]
+} \ No newline at end of file
diff --git a/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_15_Environmental_Pollution_and_Control_2.ipynb b/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_15_Environmental_Pollution_and_Control_2.ipynb
new file mode 100644
index 00000000..ab29e076
--- /dev/null
+++ b/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_15_Environmental_Pollution_and_Control_2.ipynb
@@ -0,0 +1,150 @@
+{
+ "metadata": {
+ "name": ""
+ },
+ "nbformat": 3,
+ "nbformat_minor": 0,
+ "worksheets": [
+ {
+ "cells": [
+ {
+ "cell_type": "heading",
+ "level": 1,
+ "metadata": {},
+ "source": [
+ "Chapter 15: Environmental Pollution and Control"
+ ]
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 1, Page No: 401"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constant\n",
+ "MM = 294 # Molar mass, K2Cr2O7\n",
+ "\n",
+ "# Variables\n",
+ "v_eff = 25 # cm ^ 3, effluent\n",
+ "v = 8.3 # cm ^ 3, K2Cr2O7\n",
+ "M = 0.001 # M, K2Cr2O7\n",
+ "\n",
+ "# Solution\n",
+ "w_O = v * 8 * 6 * M / 1000.\n",
+ "\n",
+ "print \"8.3 cm^3 of 0.006 N K2Cr2O7 =\", \"{:.3e}\".format(w_O), \"g of O2\"\n",
+ "print \"25 ml of the effluent requires\", \"{:.3e}\".format(w_O), \"g of O2\"\n",
+ "\n",
+ "cod = w_O * 10 ** 6 / 25.\n",
+ "print \"1 l of the effluent requires\", \"{:.2f}\".format(cod), \"g of O2\"\n",
+ "print \"COD of the effluent sample is\", \"{:.2f}\".format(cod), \"ppm or mg / L\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "8.3 cm^3 of 0.006 N K2Cr2O7 = 3.984e-04 g of O2\n",
+ "25 ml of the effluent requires 3.984e-04 g of O2\n",
+ "1 l of the effluent requires 15.94 g of O2\n",
+ "COD of the effluent sample is 15.94 ppm or mg / L\n"
+ ]
+ }
+ ],
+ "prompt_number": 2
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 2, Page No: 401"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "v0 = 30 # cm^3, effluent\n",
+ "v1 = 9.8 # cm^3, K2Cr2O7\n",
+ "M = 0.001 # M, K2Cr2O7\n",
+ "\n",
+ "# Solution\n",
+ "O_30eff = 6 * 8 * v1 * M\n",
+ "print \"So 30 cm^3 of effluent contains =\", \"{:.4f}\".format(O_30eff), \"mg of O2\"\n",
+ "\n",
+ "cod = O_30eff * 1000 / 30.\n",
+ "\n",
+ "print \"1 l of the effluent requires\", cod, \"mg of O2\"\n",
+ "print \"COD of the effluent sample =\", cod, \"ppm\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "So 30 cm^3 of effluent contains = 0.4704 mg of O2\n",
+ "1 l of the effluent requires 15.68 mg of O2\n",
+ "COD of the effluent sample = 15.68 ppm\n"
+ ]
+ }
+ ],
+ "prompt_number": 1
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 3, Page No: 401"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "v0 = 25 # ml, sewage\n",
+ "d0_O = 410 # ppm, dissolved oxygen\n",
+ "d1_O = 120 # ppm, dissolved oxygen\n",
+ "v1 = 50 # ml, sewage\n",
+ "\n",
+ "# Solution\n",
+ "print \"BOD = (DOb - DOi) * Dilution Factor\"\n",
+ "print \"BOD = (DOb - DOi) *\",\n",
+ "print \"(ml of sample after dilution) / (ml of sample before dilution)\"\n",
+ "\n",
+ "BOD = (d0_O - d1_O) * (v1 / v0)\n",
+ "print \"BOD =\", BOD, \"ppm\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "BOD = (DOb - DOi) * Dilution Factor\n",
+ "BOD = (DOb - DOi) * (ml of sample after dilution) / (ml of sample before dilution)\n",
+ "BOD = 580 ppm\n"
+ ]
+ }
+ ],
+ "prompt_number": 10
+ }
+ ],
+ "metadata": {}
+ }
+ ]
+} \ No newline at end of file
diff --git a/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_1_Structure_and_Bonding_2.ipynb b/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_1_Structure_and_Bonding_2.ipynb
new file mode 100644
index 00000000..c0748974
--- /dev/null
+++ b/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_1_Structure_and_Bonding_2.ipynb
@@ -0,0 +1,895 @@
+{
+ "metadata": {
+ "name": ""
+ },
+ "nbformat": 3,
+ "nbformat_minor": 0,
+ "worksheets": [
+ {
+ "cells": [
+ {
+ "cell_type": "heading",
+ "level": 1,
+ "metadata": {},
+ "source": [
+ "Chapter 1: Structure and Bonding"
+ ]
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 1, Page no: 35"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constant\n",
+ "c = 3 * 10 ** 10 # Velocity of light, cm/sec\n",
+ "\n",
+ "# Variable\n",
+ "wavelength = 3500 * 10 ** -8 # Wavelength of radiation, cm\n",
+ "\n",
+ "# Solution\n",
+ "print \"v = c / wavelength\"\n",
+ "print \"v: Velocity, c: Speed of light\"\n",
+ "\n",
+ "v = c / wavelength\n",
+ "\n",
+ "print \"The frequency of radiation is\", '{:.2e}'.format(v), \"Heartz.\""
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "v = c / wavelength\n",
+ "v: Velocity, c: Speed of light\n",
+ "The frequency of radiation is 8.57e+14 Heartz.\n"
+ ]
+ }
+ ],
+ "prompt_number": 6
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 2, Page no: 36"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constant\n",
+ "c = 3 * 10 ** 8 # speed of light, m/sec\n",
+ "\n",
+ "# Variable\n",
+ "f = 5 * 10 ** 16 # frequency, cycles/sec\n",
+ "\n",
+ "# Solution\n",
+ "v_bar = f / c\n",
+ "print \"The wave number is\", '{:.2e}'.format(v_bar), \"cycles/m.\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The wave number is 1.67e+08 cycles/m.\n"
+ ]
+ }
+ ],
+ "prompt_number": 7
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 3, Page no: 36"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constant\n",
+ "c = 3 * 10 ** 8 # Speed of light, m/sec\n",
+ "\n",
+ "# Variable\n",
+ "T = 2.4 * 10 ** -10 # Time period, sec\n",
+ "\n",
+ "# Solution\n",
+ "f = 1 / T # Frequency, /sec\n",
+ "lamda = c / f # wavelength, m\n",
+ "v_bar = 1 / lamda # wavenumber, /meter\n",
+ "\n",
+ "print \"Frequency:\", '{:.2e}'.format(f), \"/sec\"\n",
+ "print \"Wavelength:\", '{:.2e}'.format(lamda), \"m\"\n",
+ "print \"Wave number:\", '{:.2e}'.format(v_bar), \"/m\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Frequency: 4.17e+09 /sec\n",
+ "Wavelength: 7.20e-02 m\n",
+ "Wave number: 1.39e+01 /m\n"
+ ]
+ }
+ ],
+ "prompt_number": 8
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 4, Page no: 36"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "import math\n",
+ "\n",
+ "# Constants\n",
+ "c = 3 * 10 ** 8 # Speed of light, m/sec\n",
+ "m = 9.1 * 10 ** -31 # Mass of electron, kg\n",
+ "h = 6.626 * 10 ** -34 # Plank's constant, J.sec\n",
+ "\n",
+ "# Variable\n",
+ "ke = 4.55 * 10 ** -25 # Kinetic Energy, J\n",
+ "\n",
+ "# Solution\n",
+ "v = math.sqrt(ke * 2 / m)\n",
+ "\n",
+ "lamda = h / (m * v)\n",
+ "\n",
+ "print \"The de Broglie wavelength is\", '{:.2e}'.format(lamda), \"m\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The de Broglie wavelength is 7.28e-07 m\n"
+ ]
+ }
+ ],
+ "prompt_number": 9
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 5, Page no: 36"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constant\n",
+ "h = 6.626 * 10 ** -34 # Plank's constant, J.sec\n",
+ "\n",
+ "# Variables\n",
+ "m = 10 * 10 ** -3 # Mass of the ball, kg\n",
+ "v = 10 ** 5 # Velocity of ball, cm / sec\n",
+ "\n",
+ "# Solution\n",
+ "lamda = (h * 10 ** 7) / (m * v)\n",
+ "print \"The Wavelength of iron ball is\", \"{:.2}\".format(lamda), \"cm\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The Wavelength of iron ball is 6.6e-30 cm\n"
+ ]
+ }
+ ],
+ "prompt_number": 10
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 6, Page no: 37"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constant\n",
+ "h = 6.626 * 10 ** -34 # Plank's constant, J.sec\n",
+ "\n",
+ "# Variable\n",
+ "lamda = 2 * 10 ** -10 # wavelength, m\n",
+ "\n",
+ "# Solution\n",
+ "p = h / lamda\n",
+ "\n",
+ "print \"The momentum of the particle is\", \"{:.2}\".format(p), \"kg.m/s\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The momentum of the particle is 3.3e-24 kg.m/s\n"
+ ]
+ }
+ ],
+ "prompt_number": 12
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 7, Page no: 37"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constants\n",
+ "m = 9.1 * 10 ** -31 # Mass of electron, kg\n",
+ "h = 6.626 * 10 ** -34 # Plank's constant, J.sec\n",
+ "pi = 3.141 # Pi\n",
+ "\n",
+ "# Variable\n",
+ "delta_x = 1 * 10 ** -10 # uncertainty in velocity, m\n",
+ "\n",
+ "# Solution\n",
+ "delta_v = h / (4 * pi * m * delta_x)\n",
+ "\n",
+ "print \"Uncertainty in position of electron >=\",\n",
+ "print \"{:.2}\".format(delta_v), \"m/s\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Uncertainty in position of electron >= 5.8e+05 m/s\n"
+ ]
+ }
+ ],
+ "prompt_number": 20
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 8, Page no: 37"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constants\n",
+ "h = 6.626 * 10 ** -34 # Plank's constant, J.sec\n",
+ "pi = 3.141 # Pi\n",
+ "\n",
+ "# Variables\n",
+ "m = 10 ** -11 # Mass of particle, g\n",
+ "v = 10 ** -4 # Velocity of particle, cm/sec\n",
+ "delta_v = 0.1 / 100 # Uncertainty in velocity\n",
+ "\n",
+ "# Solution\n",
+ "delta_v = v / 1000\n",
+ "delta_x = (h * 10 ** 7) / (4 * pi * delta_v * m)\n",
+ "\n",
+ "print \"Uncertainty in position >=\",\n",
+ "print \"{:.3e}\".format(delta_x), \"cm\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Uncertainty in position 5.27e-10 cm\n"
+ ]
+ }
+ ],
+ "prompt_number": 19
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 9, Page no: 37"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constants\n",
+ "c = 3 * 10 ** 8 # Speed of light, m/sec\n",
+ "h = 6.626 * 10 ** -34 # Plank's constant, J.sec\n",
+ "\n",
+ "# Variable\n",
+ "lamda = 650 * 10 ** -12 # Wavelength of radiation, m\n",
+ "\n",
+ "# Solution\n",
+ "E = h * c / lamda\n",
+ "\n",
+ "print \"Energy per photon\", \"{:.3e}\".format(E), \"J\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Energy per photon 3.058e-16 J\n"
+ ]
+ }
+ ],
+ "prompt_number": 22
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 10, Page no: 37"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constant\n",
+ "h = 6.625 * 10 ** -34 # Plank's constant, J.sec\n",
+ "\n",
+ "# Variables\n",
+ "v = 6.5 * 10 ** 7 # Velocity of particle, m/s\n",
+ "lamda = 5 * 10 ** -11 # Wavelength, m\n",
+ "\n",
+ "# Solution\n",
+ "P = h / lamda\n",
+ "\n",
+ "print \"The momentum of the particle\", \"{:.2e}\".format(P), \"kg.m/s\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The momentum of the particle 1.33e-23 kg.m/s\n"
+ ]
+ }
+ ],
+ "prompt_number": 24
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 11, Page no: 38"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "import math\n",
+ "\n",
+ "# Constants\n",
+ "c = 3 * 10 ** 8 # Speed of light, m/sec\n",
+ "m = 9.1 * 10 ** -31 # Mass of electron, kg\n",
+ "h = 6.626 * 10 ** -34 # Plank's constant, J.sec\n",
+ "\n",
+ "# Variables\n",
+ "lamda = 200 * 10 ** -7 # Wavelength, cm\n",
+ "wf = 6.95 * 10 ** -12 # Work function, erg\n",
+ "\n",
+ "# Solution\n",
+ "E = (h * c) * 10 ** 9 / lamda\n",
+ "\n",
+ "print \"Energy of photon\", \"{:.3e}\".format(E), \"erg\"\n",
+ "\n",
+ "ke = E - wf\n",
+ "\n",
+ "v = math.sqrt((2 * ke) / (m * 10 ** 3)) * 10 ** -2\n",
+ "\n",
+ "print \"The maximum velocity of electron\", \"{:.3e}\".format(v), \"m/sec\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Energy of photon 9.939e-12 erg\n",
+ "The maximum velocity of electron 8.105e+05 m/sec\n"
+ ]
+ }
+ ],
+ "prompt_number": 26
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 12, Page no: 38"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constant\n",
+ "h = 6.626 * 10 ** -34 # Plank's constant, J.sec\n",
+ "\n",
+ "# Variables\n",
+ "m = 150 # Weight of ball, gm\n",
+ "v = 50 # Velocity, m/sec\n",
+ "\n",
+ "lamda = h / (m * v * 10 ** -8)\n",
+ "print \"Wavelength of ball\", \"{:.3e}\".format(lamda), \"m\"\n",
+ "print \"Its wavelength is so short that it does not fall\",\n",
+ "print \"in visible range, so we cannot observe it.\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Wavelength of ball 8.835e-30 m\n",
+ "Its wavelength is so short that it does not fall in visible range, so we cannot observe it.\n"
+ ]
+ }
+ ],
+ "prompt_number": 34
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 13, Page no: 39"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constant\n",
+ "h = 6.626 * 10 ** -34 # Plank's constant, J.sec\n",
+ "pi = 3.141 # Pi\n",
+ "\n",
+ "# Variables\n",
+ "m = 0.1 # Mass of base ball, kg\n",
+ "delta_x = 10 ** -10 # Uncertainty in position, m\n",
+ "\n",
+ "# Solution\n",
+ "delta_v = h / (4 * pi * m * delta_x)\n",
+ "\n",
+ "print \"Uncertainty in velocity >=\", \"{:.2e}\".format(delta_v), \"m/s\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Uncertainty in velocity >= 5.27e-24 m/s\n"
+ ]
+ }
+ ],
+ "prompt_number": 35
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 14, Page no: 39"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constant\n",
+ "t_v = 1.3 * 10 ** 15 # Threashold freq. Pt, /sec\n",
+ "h = 6.626 * 10 ** -34 # Plank's constant, J.sec\n",
+ "\n",
+ "\n",
+ "# Solution\n",
+ "print \"The threshold frequency is the lowest frequency\",\n",
+ "print \"that photons may possess to produce the photoelectric\",\n",
+ "print \"effect.\"\n",
+ "E = h * t_v\n",
+ "print \"The energy corresponding to this frequency is the minimum\",\n",
+ "print \"energy =\", \"{:.2e}\".format(E), \"erg\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The threshold frequency is the lowest frequency that photons may possess to produce the photoelectric effect.\n",
+ "The energy corresponding to this frequency is the minimum energy = 8.61e-19 erg\n"
+ ]
+ }
+ ],
+ "prompt_number": 38
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 15, Page no: 39"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constants\n",
+ "m = 9.1 * 10 ** -31 # Mass of electron, kg\n",
+ "h = 6.626 * 10 ** -34 # Plank's constant, J.sec\n",
+ "e = 1.602 * 10 ** -19 # Charge of electron, C\n",
+ "\n",
+ "# Variable\n",
+ "v = 1.87 * 10 ** 9 # Velocity of electron, m/sec\n",
+ "\n",
+ "# Solution\n",
+ "V = m * v ** 2 / (2 * e)\n",
+ "lamda = h / (m * v)\n",
+ "\n",
+ "print \"The voltage is\", \"{:.2e}\".format(V), \"volt\"\n",
+ "print \"The de Broglie wavelength is\", \"{:.2e}\".format(lamda), \"m\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The voltage is 9.93e+06 volt\n",
+ "The de Broglie wavelength is 3.89e-13 m\n"
+ ]
+ }
+ ],
+ "prompt_number": 39
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem 16, Page no: 39"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constants\n",
+ "m = 9.1 * 10 ** -31 # Mass of electron, kg\n",
+ "h = 6.626 * 10 ** -34 # Plank's constant, J.sec\n",
+ "\n",
+ "# Variable\n",
+ "lamda = 4.8 * 10 ** -9 # Wavelength of electron, m\n",
+ "\n",
+ "# Solution\n",
+ "ke = ((h / lamda) ** 2) / (2 * m)\n",
+ "\n",
+ "print \"The Kinetic Energy of moving electron is\", \"{:.2e}\".format(ke),\n",
+ "print \"J\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The Kinetic Energy of moving electron is 1.05e-20 J\n"
+ ]
+ }
+ ],
+ "prompt_number": 40
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 17, Page no: 39"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constants\n",
+ "m = 9.1 * 10 ** -31 # Mass of electron, kg\n",
+ "h = 6.626 * 10 ** -34 # Plank's constant, J.sec\n",
+ "c = 3 * 10 ** 8 # Speed of light, m/sec\n",
+ "\n",
+ "# Variables\n",
+ "v = 6.46 * 10 ** 5 # Velocity of electron, m/sec\n",
+ "lamda = 200 * 10 ** -9 # Wavelength of light, m\n",
+ "\n",
+ "# Solution\n",
+ "E = (h * c) / lamda\n",
+ "ke = m * v ** 2\n",
+ "w = E - ke\n",
+ "\n",
+ "print \"The workfunction of the metal surface is\", \"{:.3e}\".format(w),\n",
+ "print \"J\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The workfunction of the metal surface is 6.141e-19 J\n"
+ ]
+ }
+ ],
+ "prompt_number": 44
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 18, Page no: 40"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "import math\n",
+ "\n",
+ "# Constants\n",
+ "e = 1.602 * 10 ** -19 # Charge of proton, C\n",
+ "m_p = 1.66 * 10 ** -27 # Mass of proton, kg\n",
+ "m_e = 9.1 * 10 ** -31 # Mass of electron, kg\n",
+ "h = 6.626 * 10 ** -34 # Plank's constant, J.sec\n",
+ "\n",
+ "# Variable\n",
+ "V = 35 # Acceleration potential, volt\n",
+ "\n",
+ "# Solution\n",
+ "lamda_p = h / math.sqrt(2 * e * V * m_p)\n",
+ "lamda_e = h / math.sqrt(2 * e * V * m_e)\n",
+ "\n",
+ "print \"The wavelength of electron when accelerated with same\",\n",
+ "print \"potential is\", \"{:.3e}\".format(lamda_e), \"m\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The wavelength of electron when accelerated with same potential is 2.074e-10 m\n"
+ ]
+ }
+ ],
+ "prompt_number": 45
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 19, Page no: 41"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "B_O1 = (10 - 6) / 2 # Bond Order for O2\n",
+ "B_O2 = (10 - 7) / 2 # Bond Order for O2-\n",
+ "\n",
+ "print \"Bond length of O2- > O2 as Bond order of O2\",\n",
+ "print \"> Bond order of O2- :\", B_O1 > B_O2\n",
+ "print \"Both are paramagnetic, because they contain unpaired electrons.\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Bond length of O2- > O2 as Bond order of O2 > Bond order of O2- : True\n",
+ "Both are paramagnetic, because they contain unpaired electrons.\n"
+ ]
+ }
+ ],
+ "prompt_number": 51
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 20, Page no: 41"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "B_O = (9 - 4) / 2.0 # Bond order of N2+\n",
+ "\n",
+ "print \"MO configuration of N2+ is\"\n",
+ "print \"\u03c3(1s2)\u03c3*(1s2)\u03c3(2s2)\u03c3*(2s2) [\u03c0(2px2) = \u03c0(2py2)] \u03c3(2pz1)\\n\"\n",
+ "print \"The Bond order of N2+, 1/2[Nb - Na] =\", B_O\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "MO configuration of N2+ is\n",
+ "\u03c3(1s2)\u03c3*(1s2)\u03c3(2s2)\u03c3*(2s2) [\u03c0(2px2) = \u03c0(2py2)] \u03c3(2pz1)\n",
+ "\n",
+ "The Bond order of N2+, 1/2[Nb - Na] = 2.5\n"
+ ]
+ }
+ ],
+ "prompt_number": 8
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 21, Page no: 41"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Solution\n",
+ "v_n = 2 * 5 # number of valence e- in nitrogen\n",
+ "v_co = 4 + 6 # number of valence e- in CO\n",
+ "\n",
+ "print \"The number of valence electrons in N2\", v_n\n",
+ "print \"The number of valence electrons in CO\", v_co\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The number of valence electrons in N2 10\n",
+ "The number of valence electrons in CO 10\n"
+ ]
+ }
+ ],
+ "prompt_number": 55
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 22, Page no: 41"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "print \"O2(+2) [B.O. = 1.0] < O2(-1) [B.O. = 1.5] <\",\n",
+ "print \"O2 [B.O. = 2.0] < O2(+1) [B.O. =2.5]\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "O2(+2) [B.O. = 1.0] < O2(-1) [B.O. = 1.5] < O2 [B.O. = 2.0] < O2(+1) [B.O. =2.5]\n"
+ ]
+ }
+ ],
+ "prompt_number": 2
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 23, Page no: 41"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "print \"The number of electrons in N2-\", (7 + 8)\n",
+ "print \"The molecular configuration of N2- is\"\n",
+ "print \"\u03c3(1s2)\u03c3*(1s2)\u03c3(2s2)\u03c3*(2s2) [\u03c0(2px2) = \u03c0(2py2)]\",\n",
+ "print \"\u03c3(2pz2) [\u03c0*(2px1) = \u03c0*(2py0)] OR [\u03c0*(2px0) = \u03c0*(2py1)]\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The number of electrons in N2- 15\n",
+ "The molecular configuration of N2- is\n",
+ "\u03c3(1s2)\u03c3*(1s2)\u03c3(2s2)\u03c3*(2s2) [\u03c0(2px2) = \u03c0(2py2)] \u03c3(2pz2) [\u03c0*(2px1) = \u03c0*(2py0)] OR [\u03c0*(2px0) = \u03c0*(2py1)]\n"
+ ]
+ }
+ ],
+ "prompt_number": 6
+ }
+ ],
+ "metadata": {}
+ }
+ ]
+} \ No newline at end of file
diff --git a/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_2_Spectroscopy_and_Photochemistry_2.ipynb b/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_2_Spectroscopy_and_Photochemistry_2.ipynb
new file mode 100644
index 00000000..58e602ab
--- /dev/null
+++ b/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_2_Spectroscopy_and_Photochemistry_2.ipynb
@@ -0,0 +1,418 @@
+{
+ "metadata": {
+ "name": ""
+ },
+ "nbformat": 3,
+ "nbformat_minor": 0,
+ "worksheets": [
+ {
+ "cells": [
+ {
+ "cell_type": "heading",
+ "level": 1,
+ "metadata": {},
+ "source": [
+ "Chapter 2: Spectroscopy and Photochemistry"
+ ]
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 1, Page no: 65"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constants\n",
+ "m_br79 = 78.9183 # Mass of 79Br, amu\n",
+ "m_br81 = 80.9163 # Mass of 91Br, amu\n",
+ "Na = 6.022 * 10 ** 23 # Mole constant, /mol\n",
+ "pi = 3.141 # Pi\n",
+ "c = 3 * 10 ** 10 # Speed of light, cm /s\n",
+ "\n",
+ "# Variable\n",
+ "wave_no = 323.2 # Wave no. of fund. vibration of 79Br - 81Br, /cm\n",
+ "\n",
+ "# Solution\n",
+ "mu = (m_br79 * m_br81) / ((m_br79 + m_br81) * Na)\n",
+ "\n",
+ "k = 4 * (pi * c * wave_no) ** 2 * mu * 10 ** -3\n",
+ "\n",
+ "print \"The force constant of the bond is\", \"{:.3e}\".format(k), \"N/m\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The force constant of the bond is 2.461e+02 N/m\n"
+ ]
+ }
+ ],
+ "prompt_number": 2
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 2, Page no: 65"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constants\n",
+ "Na = 6.022 * 10 ** 23 # Mole constant, /mol\n",
+ "pi = 3.141 # Pi\n",
+ "c = 3 * 10 ** 10 # Speed of light, cm /s\n",
+ "h = 6.626 * 10 ** -34 # Plank's constant, J.sec\n",
+ "\n",
+ "# Variables\n",
+ "b_l = 112.81 * 10 ** -12 # Equillibrium bond length, m\n",
+ "m1 = 12 # Mass of Carbon, g /mol\n",
+ "m2 = 16 # Mass of Oxygen, g /mol\n",
+ "\n",
+ "# Solution\n",
+ "mu = m1 * m2 / ((m1 + m2) * Na) # g\n",
+ "mu *= 10 ** -3 # kg\n",
+ "\n",
+ "B = h / (8 * pi ** 2 * mu * b_l ** 2 * c)\n",
+ "v2_3 = B * 6\n",
+ "\n",
+ "print \"The reduced mass of CO is\", \"{:.3e}\".format(mu), \"kg\"\n",
+ "print \"The frequency of 3->2 transition is\", \"{:.2f}\".format(v2_3), \"/cm\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The reduced mass of CO is 1.139e-26 kg\n",
+ "The frequency of 3->2 transition is 11.59 /cm\n"
+ ]
+ }
+ ],
+ "prompt_number": 3
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 3, Page no: 66"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constants\n",
+ "Na = 6.022 * 10 ** 23 # Mole constant, /mol\n",
+ "\n",
+ "# Variables\n",
+ "d_NaCl = 2.36 * 10 ** -10 # Intermolecular dist. NaCl, m\n",
+ "m_Cl = 35 * 10 ** -3 # Atomic mass, kg /mol\n",
+ "m_Na = 23 * 10 ** -3 # Atomic mass, kg /mol\n",
+ "\n",
+ "# Solution\n",
+ "mu = m_Na * m_Cl / ((m_Na + m_Cl) * 10 ** -3 * Na) * 10 ** -3\n",
+ "\n",
+ "I = mu * d_NaCl ** 2\n",
+ "\n",
+ "print \"The reduced mass of NaCl is\", \"{:.3e}\".format(mu), \"kg\"\n",
+ "print \"The moment of inertia of NaCl is\", \"{:.3e}\".format(I), \"kg.m^2\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The reduced mass of NaCl is 2.305e-26 kg\n",
+ "The moment of inertia of NaCl is 1.284e-45 kg.m^2\n"
+ ]
+ }
+ ],
+ "prompt_number": 4
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 4, Page no: 66"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "import math\n",
+ "\n",
+ "# Constant\n",
+ "e = 4000 # Extinction coeff., dm^3/mol/cm\n",
+ "\n",
+ "# Variable\n",
+ "x = 3 # Solution thickness, cm\n",
+ "\n",
+ "# Solution\n",
+ "A = math.log10(1 / 0.3) # Absorbance\n",
+ "C = A / (e * x)\n",
+ "\n",
+ "print \"The concentration of the solution is\", \"{:.2e}\".format(C), \"mol/dm^3\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The concentration of the solution is 4.36e-05 mol/dm^3\n"
+ ]
+ }
+ ],
+ "prompt_number": 5
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 5, Page no: 67"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constants\n",
+ "pi = 3.141 # Pi\n",
+ "c = 3 * 10 ** 10 # Speed of light, cm /s\n",
+ "\n",
+ "# Variables\n",
+ "v_bar = 2140 # Fundamental vibrating freq, /cm\n",
+ "m_C = 19.9 * 10 ** -27 # Atomic mass of C, kg\n",
+ "m_O = 26.6 * 10 ** -27 # Atomic mass of O, kg\n",
+ "\n",
+ "# Solution\n",
+ "mu = m_O * m_C / (m_C + m_O)\n",
+ "k = 4 * (pi * c * v_bar) ** 2 * mu\n",
+ "\n",
+ "print \"The force constant of the molecule is\", \"{:.3e}\".format(k), \"N/m\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The force constant of the molecule is 1.852e+03 N/m\n"
+ ]
+ }
+ ],
+ "prompt_number": 6
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 6, Page no: 67"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "print \"a) Microwave < IR < UV-Visible < X-Ray.\"\n",
+ "print \"b) HCl and NO because they possess permanent dipole moments, so they are rotationally active.\""
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "a) Microwave < IR < UV-Visible < X-Ray.\n",
+ "b) HCl and NO because they possess permanent dipole moments, so they are rotationally active.\n"
+ ]
+ }
+ ],
+ "prompt_number": 8
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 7, Page no: 67"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "import math\n",
+ "\n",
+ "# Constants\n",
+ "pi = 3.141 # pi\n",
+ "c = 3 * 10 ** 10 # speed of light, cm /s\n",
+ "h = 6.626 * 10 ** -34 # Plank's constant, J.sec\n",
+ "Na = 6.022 * 10 ** 23 # Mole constant, /mol\n",
+ "\n",
+ "# Variables\n",
+ "d = 20.7 # Interspacing, /cm\n",
+ "m1 = 1 # Mass of H, g / mol\n",
+ "m2 = 35.5 # Masso f Cl, g / mol\n",
+ "\n",
+ "# Solution\n",
+ "B = 0.1035 * 10 ** 2 # /m\n",
+ "I = h / (8 * pi ** 2 * B * c)\n",
+ "mu = m1 * m2 / ((m1 + m2) * Na)\n",
+ "mu *= 10 ** -3\n",
+ "r = math.sqrt(I / mu)\n",
+ "\n",
+ "print \"The intermolecular distance of HCl is\", \"{:.3e}\".format(r), \"m\"\n",
+ "# Discrepency in value is due to error in calculation in the textbook\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The intermolecular distance of HCl is 1.294e-10 m\n"
+ ]
+ }
+ ],
+ "prompt_number": 9
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 8, Page no: 68"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "import math\n",
+ "\n",
+ "# Constant\n",
+ "e = 8000 # Molar absorbtion coeff, dm^3 / mol / cm\n",
+ "\n",
+ "# Variable\n",
+ "l = 2.5 # Thickness of solution, cm\n",
+ "\n",
+ "# Solution\n",
+ "C = math.log10(1 / 0.3) / (e * l)\n",
+ "\n",
+ "print \"The concentration of Solution from Lambert-Beer's Law is\",\n",
+ "print \"{:.2e}\".format(C), \"mol/dm^3\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The concentration of Solution from Lambert-Beer's Law is 2.61e-05 mol/dm^3\n"
+ ]
+ }
+ ],
+ "prompt_number": 10
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 9, Page no: 68"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "print \"a) In the visible-UV spectra, CH2 = CHOCHOCH3 exhibits\"\n",
+ "print \"a higher value of lambda(max) because it has two conjugated\"\n",
+ "print \"chromophores, that is, one double bond (C=C) and a carbonyl\"\n",
+ "print \"group.\"\n",
+ "\n",
+ "print\n",
+ "print \"b) Because of the symmetrical vibrations of C=C double bond and\"\n",
+ "print \"triple bond, ethylene and acetylene do not absorb IR energy.\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "a) In the visible-UV spectra, CH2 = CHOCHOCH3 exhibits\n",
+ "a higher value of lambda(max) because it has two conjugated\n",
+ "chromophores, that is, one double bond (C=C) and a carbonyl\n",
+ "group.\n",
+ "\n",
+ "b) Because of the symmetrical vibrations of C=C double bond and\n",
+ "triple bond, ethylene and acetylene do not absorb IR energy.\n"
+ ]
+ }
+ ],
+ "prompt_number": 13
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 10, Page no: 68"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "print \"Because CO2 is a linear molecule.\"\n",
+ "v_deg = 3 * 3 - 5\n",
+ "print \"The vibrational degree of freedom is\", v_deg"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Because CO2 is a linear molecule.\n",
+ "The vibrational degree of freedom is 4\n"
+ ]
+ }
+ ],
+ "prompt_number": 14
+ }
+ ],
+ "metadata": {}
+ }
+ ]
+} \ No newline at end of file
diff --git a/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_3_Thermodynamics_and_Chemical_Equilibrium_2.ipynb b/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_3_Thermodynamics_and_Chemical_Equilibrium_2.ipynb
new file mode 100644
index 00000000..16fb19f8
--- /dev/null
+++ b/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_3_Thermodynamics_and_Chemical_Equilibrium_2.ipynb
@@ -0,0 +1,1116 @@
+{
+ "metadata": {
+ "name": ""
+ },
+ "nbformat": 3,
+ "nbformat_minor": 0,
+ "worksheets": [
+ {
+ "cells": [
+ {
+ "cell_type": "heading",
+ "level": 1,
+ "metadata": {},
+ "source": [
+ "Chapter 3: Thermodynamic and Chemical Equilibrium"
+ ]
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 1, Page no: 105"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "q = 120 # Heat from surrounding, cal\n",
+ "W = 70 # Work done, cal\n",
+ "\n",
+ "# Solution\n",
+ "delta_E = q - W\n",
+ "\n",
+ "print \"Change in internal Energy\", delta_E, \"cals.\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Change in internal Energy 50 cals.\n"
+ ]
+ }
+ ],
+ "prompt_number": 2
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 2, Page no: 105"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "print \"CH4 (g) + 2O2 (g) -> CO2 (g) + 2H20 (l)\"\n",
+ "delta_n = 1 - (1 + 2)\n",
+ "solution = - 2 * 2 * 298 # cals\n",
+ "print \"Delta H - Delta E is:\", solution, \"cals\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "CH4 (g) + 2O2 (g) -> CO2 (g) + 2H20 (l)\n",
+ "Delta H - Delta E is: -1192 cals\n"
+ ]
+ }
+ ],
+ "prompt_number": 2
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 3, Page no: 105"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "delta_G = -16.0 # Kelvin cal\n",
+ "delta_H = -10.0 # Kelvin cal\n",
+ "T = 300 # Kelvin\n",
+ "\n",
+ "# Solution\n",
+ "delta_S = (delta_H - delta_G) * 10 ** 3 / T # cal/deg\n",
+ "new_T = 330 # Kelvin\n",
+ "new_delta_G = (delta_H * 10 ** 3) - new_T * delta_S\n",
+ "\n",
+ "print \"The free energy at 330K is:\", \"{:.2e}\".format(new_delta_G), \"K cal\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The free energy at 330K is: -1.66e+04 K cal\n"
+ ]
+ }
+ ],
+ "prompt_number": 5
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 4, Page no: 106"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "delta_S = -20.7 # cal /deg /mol\n",
+ "delta_H = -67.37 # K cal\n",
+ "T = 25 # deg C\n",
+ "\n",
+ "# Solution\n",
+ "T += 273 # K\n",
+ "delta_G = delta_H - (T * delta_S * 10 ** -3)\n",
+ "print \"The change in free energy at 25deg C is:\", delta_G, \"K cal / mol\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The change in free energy at 25deg C is: -61.2014 K cal / mol\n"
+ ]
+ }
+ ],
+ "prompt_number": 8
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 5, Page no: 106"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "wt = 1 # g\n",
+ "delta_H = 149 # joules\n",
+ "\n",
+ "# Solution\n",
+ "delta_H_fusion = delta_H * (10 * 12 + 8 * 1)\n",
+ "print \"Enthalpy of fusion of naphthalene:\", delta_H_fusion * 10 ** -3, \"kJ/mol\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Enthalpy of fusion of naphthalene: 19.072 kJ/mol\n"
+ ]
+ }
+ ],
+ "prompt_number": 9
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 6, Page no: 106"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "delta_H_acetylene = 230 # kJ/mol\n",
+ "delta_H_benzene = 85 # kJ/mol\n",
+ "T = 298 # K\n",
+ "\n",
+ "# Solution\n",
+ "delta_H = delta_H_benzene - 3 * delta_H_acetylene\n",
+ "print \"The enthalpy change for the reaction is:\", delta_H, \"kJ/mole\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The enthalpy change for the reaction is: -605 kJ/mole\n"
+ ]
+ }
+ ],
+ "prompt_number": 10
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 7, Page no: 106"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constant\n",
+ "delta_H_vap = 2.0723 # kJ/g\n",
+ "Tb = 373 # K\n",
+ "\n",
+ "# Solution\n",
+ "delta_H_vap *= 18 # kJ/mol\n",
+ "delta_S = delta_H_vap / Tb\n",
+ "delta_G = delta_H_vap - Tb * delta_S\n",
+ "delta_S *= 1000\n",
+ "\n",
+ "print \"The Entropy change is:\", \"{:.1f}\".format(delta_S), \"J/mol/K\"\n",
+ "print \"The Free Energy change is:\", delta_G, \"kJ/mol\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The Entropy change is: 100.0 J/mol/K\n",
+ "The Free Energy change is: 0.0 kJ/mol\n"
+ ]
+ }
+ ],
+ "prompt_number": 11
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 8, Page no: 106"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "import math\n",
+ "\n",
+ "# Constant\n",
+ "R = 1.987 # cal /K /mol\n",
+ "\n",
+ "# Variables\n",
+ "moles = 5\n",
+ "Vo = 4 # litres, Initial Volume\n",
+ "Vf = 40 # litres, Final Volume\n",
+ "T = 27 # deg C\n",
+ "\n",
+ "# Solution\n",
+ "print \"dS = nRln(V2 / V1)\"\n",
+ "dS = moles * R * 2.303 * math.log10(Vf / Vo)\n",
+ "print \"The change in entropy is:\", \"{:.2f}\".format(dS), \"cal / degree\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "dS = nRln(V2 / V1)\n",
+ "The change in entropy is: 22.88 cal / degree\n"
+ ]
+ }
+ ],
+ "prompt_number": 12
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 9, Page no: 107"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "wt = 10 # g\n",
+ "heat_abs = 4.5 # K\n",
+ "\n",
+ "# Solution\n",
+ "mole = 10 / 100.0 # mol\n",
+ "delta_H = heat_abs / mole\n",
+ "print \"The heat of the reaction is:\", delta_H, \"K cal / mol\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The heat of the reaction is: 45.0 K cal / mol\n"
+ ]
+ }
+ ],
+ "prompt_number": 1
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 10, Page no: 107"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "import math\n",
+ "\n",
+ "# Constant\n",
+ "R = 8.314 # J / K\n",
+ "\n",
+ "# Variables\n",
+ "V_O2 = 2.8 # litres\n",
+ "V_H2 = 19.6 # litres\n",
+ "\n",
+ "# Solution\n",
+ "na = V_O2 / 22.4 # mol\n",
+ "nb = V_H2 / 22.4 # mol\n",
+ "Xa = na / (na + nb)\n",
+ "Xb = nb / (na + nb)\n",
+ "delta_S = (- R) * (na * math.log(Xa) + nb * math.log(Xb))\n",
+ "\n",
+ "print \"The increase in entropy on mixing is:\", \"{:.3f}\".format(delta_S), \"J / K\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The increase in entropy on mixing is: 3.132 J / K\n"
+ ]
+ }
+ ],
+ "prompt_number": 2
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 11, Page no: 107"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Solution\n",
+ "print \"For 1 mole of ideal gas,\"\n",
+ "print \"\\tPV = RT or T = (PV) / R\\n\"\n",
+ "print \"Differentiating with respect to V at constant P,\"\n",
+ "print \"\\t[dT/dV]p = P/R\\n\"\n",
+ "print \"Differentiating again with respect oto P at constant V\"\n",
+ "print \"\\t[d2T/(dV*dP)] = 1/R\\n\"\n",
+ "print \"Now differectiating with respect to P at constant V,\"\n",
+ "print \"\\t[dT/dP]v = V/R\\n\"\n",
+ "print \"Differentiating again with respect to V at constant P,\"\n",
+ "print \"\\t[d2T/(dV*dP)] = 1/R\\n\"\n",
+ "print \"From equations we get:\"\n",
+ "print \"\\t[d2T/(dV*dP)] = [d2T/(dV*dP)]\\n\"\n",
+ "print \"Hence, dT is a perfect differential.\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "For 1 mole of ideal gas,\n",
+ "\tPV = RT or T = (PV) / R\n",
+ "\n",
+ "Differentiating with respect to V at constant P,\n",
+ "\t[dT/dV]p = P/R\n",
+ "\n",
+ "Differentiating again with respect oto P at constant V\n",
+ "\t[d2T/(dV*dP)] = 1/R\n",
+ "\n",
+ "Now differectiating with respect to P at constant V,\n",
+ "\t[dT/dP]v = V/R\n",
+ "\n",
+ "Differentiating again with respect to V at constant P,\n",
+ "\t[d2T/(dV*dP)] = 1/R\n",
+ "\n",
+ "From equations we get:\n",
+ "\t[d2T/(dV*dP)] = [d2T/(dV*dP)]\n",
+ "\n",
+ "Hence, dT is a perfect differential.\n"
+ ]
+ }
+ ],
+ "prompt_number": 14
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 12, Page no: 108"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "delta_G_25 = - 85.77 # k J, Free Energy at 25 C\n",
+ "delta_G_35 = - 83.68 # k J, Free Energy at 35 C\n",
+ "Ti = 273 + 25 # K\n",
+ "Tf = 273 + 35 # K\n",
+ "\n",
+ "# Solution\n",
+ "print \"Equating the entropy change at both the temperatures.\"\n",
+ "print \"(delta_H + delta_G_25) / Ti = (delta_H + delta_G_35) / Tf\"\n",
+ "delta_H = - 148\n",
+ "print \"The change in enthalpy for the process at 30C is\", delta_H, \"kJ\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Equating the entropy change at both the temperatures.\n",
+ "(delta_H + delta_G_25) / Ti = (delta_H + delta_G_35) / Tf\n",
+ "The change in enthalpy for the process at 30C is -148 kJ\n"
+ ]
+ }
+ ],
+ "prompt_number": 1
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 13, Page no: 108"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constants\n",
+ "Lv = 101 # cal /g, Latent headt of vap.\n",
+ "mwt = 78 # molecular weight of benzene\n",
+ "\n",
+ "# Variable\n",
+ "moles = 2\n",
+ "Tb = 80.2 # C, boiling point of benzene\n",
+ "\n",
+ "# Solution\n",
+ "Tb += 273 # K\n",
+ "delta_H = Lv * mwt\n",
+ "delta_S = delta_H / Tb\n",
+ "delta_G = delta_H - Tb * delta_S\n",
+ "print \"delta_S =\", \"{:.2f}\".format(delta_S), \"cal / K\"\n",
+ "print \"delta_G = delta_A =\", delta_G\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "delta_S = 22.30 cal / K\n",
+ "delta_G = delta_A = 0.0\n"
+ ]
+ }
+ ],
+ "prompt_number": 3
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 14, Page no: 109"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "V1 = 6 # dm^3\n",
+ "V2 = 2 # dm^3\n",
+ "T1 = 27 # C\n",
+ "moles = 5\n",
+ "\n",
+ "# Solution\n",
+ "print \"T1*V1 ^ (gamma - 1) = T2 * V2 ^ (gamma - 1)\"\n",
+ "T1 += 273 # K\n",
+ "T2 = T1 * (V1 / V2) ** (8.314 / 20.91)\n",
+ "print \"The final temperature is\", \"{:.1f}\".format(T2), \"K\"\n",
+ "q = 0 # Adiabatic process\n",
+ "delta_E = - moles * 20.91 * (T2 - T1)\n",
+ "delta_E /= 1000\n",
+ "print \"q = \", q\n",
+ "print \"Change is Energy is\", \"{:.2f}\".format(delta_E), \"kJ / mol\"\n",
+ "W = - delta_E\n",
+ "print \"W = \", \"{:.2f}\".format(delta_E), \"kJ / mol\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "T1*V1 ^ (gamma - 1) = T2 * V2 ^ (gamma - 1)\n",
+ "The final temperature is 464.3 K\n",
+ "q = 0\n",
+ "Change is Energy is -17.18 kJ / mol\n",
+ "W = -17.18 kJ / mol\n"
+ ]
+ }
+ ],
+ "prompt_number": 11
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 15, Page no: 109"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "import math\n",
+ "\n",
+ "# Constant\n",
+ "R = 8.314 # J / K mol\n",
+ "\n",
+ "# Variables\n",
+ "mole = 1\n",
+ "V1 = 5 # dm^3\n",
+ "V2 = 10 # dm^3\n",
+ "T = 300 # K\n",
+ "\n",
+ "# Solution\n",
+ "print \"For isothermal and reversible process,\"\n",
+ "delta_E = delta_H = 0\n",
+ "delta_A = delta_G = - 2.303 * mole * R * T * math.log10(V2 / V1)\n",
+ "q = W = - delta_G\n",
+ "print \"delta_E = delta_H =\", delta_H\n",
+ "print \"delta_G = delta_A =\", \"{:.3f}\".format(delta_G), \"J / mol\\n\"\n",
+ "print \"For isothermal and reversible expansion\"\n",
+ "print \"q = W = -delta_G =\", \"{:.3f}\".format(W), \"J / mol\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "For isothermal and reversible process,\n",
+ "delta_E = delta_H = 0\n",
+ "delta_G = delta_A = -1729.159 J / mol\n",
+ "\n",
+ "For isothermal and reversible expansion\n",
+ "q = W = -delta_G = 1729.159 J / mol\n"
+ ]
+ }
+ ],
+ "prompt_number": 4
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 16, Page no: 109"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "import math\n",
+ "\n",
+ "# Constant\n",
+ "R = 8.314 # J / K mol\n",
+ "\n",
+ "# Variables\n",
+ "n = 5 # moles\n",
+ "T = 27 # C\n",
+ "V1 = 50.0 # L, Initial Volume\n",
+ "V2 = 1000 # L, Final Volume\n",
+ "\n",
+ "# Solution\n",
+ "T += 273\n",
+ "delta_G = 2.303 * n * R * T * math.log10(V1 / V2)\n",
+ "delta_G /= 1000\n",
+ "print \"The free energy change is\", \"{:.3f}\".format(delta_G), \"k J\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The free energy change is -37.367 k J\n"
+ ]
+ }
+ ],
+ "prompt_number": 13
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 17, Page no: 110"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "delta_H_neu = - 51.46 # k J/mol, neutralization\n",
+ "delta_H_ion = - 57.1 # k J/mol, ionization\n",
+ "\n",
+ "# Solution\n",
+ "delta_H = - delta_H_ion + delta_H_neu\n",
+ "print \"The head of ionization for NH4OH is\", delta_H, \"kJ / mol\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The head of ionization for NH4OH is 5.64 kJ / mol\n"
+ ]
+ }
+ ],
+ "prompt_number": 16
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 18, Page no: 110"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "print \"For 1 mole of an ideal gas,\"\n",
+ "print \"PV = RT or V = (RT)/P\"\n",
+ "print \"(dV/ dP) = -(RT/P^2)\\t (at constant temperature)\"\n",
+ "print \"(d^2V/ (dP*dT)) = -(R/ P^2)\"\n",
+ "print \"(dV/ dT) = (R/ P)\\t (at constant pressure)\"\n",
+ "print \"(d^2V/ (dT*dP)) = -(R/ P^2)\\n\"\n",
+ "print \"(d^2V/ (dT*dP)) = (d^2V/ (dP*dT))\\t[From above equations]\"\n",
+ "print \"Hence, dV is an exact differential.\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "For 1 mole of an ideal gas,\n",
+ "PV = RT or V = (RT)/P\n",
+ "(dV/ dP) = -(RT/P^2)\t (at constant temperature)\n",
+ "(d^2V/ (dP*dT)) = -(R/ P^2)\n",
+ "(dV/ dT) = (R/ P)\t (at constant pressure)\n",
+ "(d^2V/ (dT*dP)) = -(R/ P^2)\n",
+ "\n",
+ "(d^2V/ (dT*dP)) = (d^2V/ (dP*dT))\t[From above equations]\n",
+ "Hence, dV is an exact differential.\n"
+ ]
+ }
+ ],
+ "prompt_number": 5
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 19, Page no: 110"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "print \"Let P1, V1, T1 and P2, V2, T2 b the initial and final\",\n",
+ "print \"state, respectively of the system\"\n",
+ "print \"W rev = nRT[P1/ P2 - 1]\"\n",
+ "print \"W irr = nRT[1 - P2/ P1]\"\n",
+ "print \"W rev - W irr = [nRT/(P1P2)]*(P1 - P2)^2\"\n",
+ "print \"Because RHS of the above equation is always positive,\"\n",
+ "print \"W rev > W irr\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Let P1, V1, T1 and P2, V2, T2 b the initial and final state, respectively of the system\n",
+ "W rev = nRT[P1/ P2 - 1]\n",
+ "W irr = nRT[1 - P2/ P1]\n",
+ "W rev - W irr = [nRT/(P1P2)]*(P1 - P2)^2\n",
+ "Because RHS of the above equation is always positive,\n",
+ "W rev > W irr\n"
+ ]
+ }
+ ],
+ "prompt_number": 18
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 20, Page no: 111"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Solution\n",
+ "Eq_HI = 1.56 / 2\n",
+ "Eq_H2 = 0.22 / 2\n",
+ "Eq_I2 = 0.22 / 2\n",
+ "Kc = Eq_H2 * Eq_I2 / (Eq_HI ** 2)\n",
+ "print \"The equilibrium constant for the dissociation reaction\",\n",
+ "print \"{:.4f}\".format(Kc)\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The equilibrium constant for the dissociation reaction 0.0199\n"
+ ]
+ }
+ ],
+ "prompt_number": 20
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 21, Page no: 111"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "Kc = 0.5 # / mole^2 litre^2\n",
+ "T = 400 # K\n",
+ "R = 0.082 # litre atm degree^-1 mole^-1\n",
+ "\n",
+ "# Solution\n",
+ "Kp = Kc * (R * T) ** (-2)\n",
+ "\n",
+ "print \"The given equilibrium is\"\n",
+ "print \"\\t\\tN2(g) + 3H2(g) <--> 2NH3(g)\"\n",
+ "print \"Kp is\", \"{:.3e}\".format(Kp)\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The given equilibrium is\n",
+ "\t\tN2(g) + 3H2(g) <--> 2NH3(g)\n",
+ "Kp is 4.648e-04\n"
+ ]
+ }
+ ],
+ "prompt_number": 7
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 22, Page no: 111"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "solubility = 7.5 * 10 ** - 5 # mol L^-1\n",
+ "\n",
+ "# Solution\n",
+ "Ksp = 4 * (solubility ** 3)\n",
+ "print \"Solubility product of the salt is\", \"{:.4e}\".format(Ksp), \"mol^3 / L^-3\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Solubility product of the salt is 1.6875e-12 mol^3 / L^-3\n"
+ ]
+ }
+ ],
+ "prompt_number": 23
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 23, Page no: 111"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "Ti = 25 # C\n",
+ "S = 0.00179 # g / L\n",
+ "\n",
+ "# Solution\n",
+ "S /= 170 # mol / L\n",
+ "Ksp = S ** 2\n",
+ "print \"Solubility product at 25 C is\", \"{:.4e}\".format(Ksp), \"mol^2 / L^-2\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Solubility product at 25 C is 1.1087e-10 mol^2 / L^-2\n"
+ ]
+ }
+ ],
+ "prompt_number": 25
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 24, Page no: 111"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "Ksp = 8 * 10 ** - 5 # Solubility product PbBr2\n",
+ "disso = 80 / 100 # % dissociation\n",
+ "\n",
+ "# Solution\n",
+ "S = (Ksp / 4) ** (1 / 3.0) # Solubility is 100%\n",
+ "S_80 = S * (80 / 100.0)\n",
+ "S_per_g = S_80 * 367 - 1.621\n",
+ "print \"Solubility in gm per litre is\", \"{:.3f}\".format(S_per_g), \"gm / litre\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Solubility in gm per litre is 6.349 gm / litre\n"
+ ]
+ }
+ ],
+ "prompt_number": 27
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 25, Page no: 112"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "n_acid = 1 # mole\n",
+ "n_alcohol = 1 # mole\n",
+ "T = 25 # C\n",
+ "x = 0.667 # mole\n",
+ "\n",
+ "# Solution\n",
+ "print \"Kc = [CH3COOC2H][H2O] / ([CH3COOH][C2H2OH])\"\n",
+ "Kc = 4\n",
+ "print \"[CH3COOH] = (2 - x) / V\"\n",
+ "print \"[C2H5OH] = (1 - x) / V\"\n",
+ "print \"[CH3COOC2H5] = [H20] = x / V\"\n",
+ "print \"3x^2 - 12x + 8 = 0\"\n",
+ "print \"x =\", 2.366, \"or\", 0.634\n",
+ "print \"0.634 mole of ester would be formed, because the other value,\",\n",
+ "print \"x = 2.366, is not permissible.\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Kc = [CH3COOC2H][H2O] / ([CH3COOH][C2H2OH])\n",
+ "[CH3COOH] = (2 - x) / V\n",
+ "[C2H5OH] = (1 - x) / V\n",
+ "[CH3COOC2H5] = [H20] = x / V\n",
+ "3x^2 - 12x + 8 = 0\n",
+ "x = 2.366 or 0.634\n",
+ "0.634 mole of ester would be formed, because the other value, x = 2.366, is not permissible.\n"
+ ]
+ }
+ ],
+ "prompt_number": 3
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 26, Page no: 113"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "import math\n",
+ "\n",
+ "# Variables\n",
+ "n_acid = 0.2 # mole\n",
+ "n_salt = 0.10 # mole\n",
+ "Ka = 1.8 * 10 ** -5\n",
+ "\n",
+ "# Solution\n",
+ "pH = - math.log10(Ka) + math.log10(n_salt / n_acid)\n",
+ "print \"The pH of acidic buffer is\", \"{:.3f}\".format(pH)\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The pH of acidic buffer is 4.444\n"
+ ]
+ }
+ ],
+ "prompt_number": 5
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 27, Page no: 113"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "import math\n",
+ "\n",
+ "# Variables\n",
+ "n_salt = 0.02 # mole\n",
+ "n_base = 0.2 # mole\n",
+ "pKb = 4.7\n",
+ "\n",
+ "# Solution\n",
+ "pOH = pKb + math.log10(n_salt / n_base)\n",
+ "pH = 14 - pOH\n",
+ "print \"pH of a buffer solution is\", pH\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "pH of a buffer solution is 10.3\n"
+ ]
+ }
+ ],
+ "prompt_number": 7
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 28, Page no: 113"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "n_H2 = 8.07 # moles\n",
+ "n_I2 = 9.08 # moles\n",
+ "T = 448 # C\n",
+ "n_eqHI2 = 13.38 # moles\n",
+ "\n",
+ "# Solution\n",
+ "x = n_eqHI2 / 2 + 6.69\n",
+ "Kc = n_eqHI2 ** 2 / (n_H2 * n_I2)\n",
+ "\n",
+ "print \"H2 + I2 <--> 2HI\"\n",
+ "print \"1 0 0\"\n",
+ "print \"1 - 2xx x x\"\n",
+ "print \"x/(1 - 2x) = (1/Kc)^0.5\"\n",
+ "print \"Dissociation constant of HI is 106.75 x 10^-3\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "H2 + I2 <--> 2HI\n",
+ "1 0 0\n",
+ "1 - 2xx x x\n",
+ "x/(1 - 2x) = (1/Kc)^0.5\n",
+ "Dissociation constant of HI is 106.75 x 10^-3\n"
+ ]
+ }
+ ],
+ "prompt_number": 9
+ }
+ ],
+ "metadata": {}
+ }
+ ]
+} \ No newline at end of file
diff --git a/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_5_Chemical_Kinetics_and_Catalysis_2.ipynb b/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_5_Chemical_Kinetics_and_Catalysis_2.ipynb
new file mode 100644
index 00000000..b0e0ac54
--- /dev/null
+++ b/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_5_Chemical_Kinetics_and_Catalysis_2.ipynb
@@ -0,0 +1,491 @@
+{
+ "metadata": {
+ "name": ""
+ },
+ "nbformat": 3,
+ "nbformat_minor": 0,
+ "worksheets": [
+ {
+ "cells": [
+ {
+ "cell_type": "heading",
+ "level": 1,
+ "metadata": {},
+ "source": [
+ "Chapter 5: Chemical Kinetics and Catalysis"
+ ]
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 1, Page no: 149"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "K = 3.5 * 10 ** - 2 # Rate constant\n",
+ "\n",
+ "# Solution\n",
+ "print \"First order reaction = 0.693 / K\"\n",
+ "t_05 = 0.693 / K\n",
+ "print \"Time taken for half the initial concentration to react\", t_05, \"minutes\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "First order reaction = 0.693 / K\n",
+ "Time taken for half the initial concentration to react 19.8 minutes\n"
+ ]
+ }
+ ],
+ "prompt_number": 2
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 2, Page no: 150"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "t05 = 40 # minutes\n",
+ "\n",
+ "# Solution\n",
+ "print \"Rate constant = 0.693 / t05\"\n",
+ "K = 0.693 / t05\n",
+ "print \"Rate constant\", \"{:.4f}\".format(K), \"/ min\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Rate constant = 0.693 / t05\n",
+ "Rate constant 0.0173 / min\n"
+ ]
+ }
+ ],
+ "prompt_number": 5
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 3, Page no: 150"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "from math import log10\n",
+ "\n",
+ "# Variables\n",
+ "t0 = 37.0 # cm^3 of KMnO4\n",
+ "t5 = 29.8 # cm^3 of KMnO4\n",
+ "t15 = 19.6 # cm^3 of KMnO4\n",
+ "t25 = 12.3 # cm^3 of KMnO4\n",
+ "t45 = 5.00 # cm^3 of KMnO4\n",
+ "\n",
+ "# Solution\n",
+ "K5 = 2.303 / 5 * log10(t0 / t5)\n",
+ "K15 = 2.303 / 15 * log10(t0 / t15)\n",
+ "K25 = 2.303 / 25 * log10(t0 / t25)\n",
+ "K45 = 2.303 / 45 * log10(t0 / t45)\n",
+ "\n",
+ "print \"At t = 5 min, K =\", \"{:.3e}\".format(K5), \"/min\"\n",
+ "print \"At t = 15 min, K =\", \"{:.3e}\".format(K15), \"/min\"\n",
+ "print \"At t = 25 min, K =\", \"{:.3e}\".format(K25), \"/min\"\n",
+ "print \"At t = 45 min, K =\", \"{:.3e}\".format(K45), \"/min\"\n",
+ "print \"As the different values of K are nearly same, so the reaction\",\n",
+ "print \"is of first-order\"\n",
+ "K = (K45 + K25 + K5 + K15) / 4\n",
+ "print \"The average value of K = \", \"{:.3e}\".format(K), \"/min\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "At t = 5 min, K = 4.329e-02 /min\n",
+ "At t = 15 min, K = 4.237e-02 /min\n",
+ "At t = 25 min, K = 4.406e-02 /min\n",
+ "At t = 45 min, K = 4.449e-02 /min\n",
+ "As the different values of K are nearly same, so the reaction is of first-order\n",
+ "The average value of K = 4.355e-02 /min\n"
+ ]
+ }
+ ],
+ "prompt_number": 1
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem : 4, Page no: 150"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "t = 60 # min\n",
+ "x = \"0.5a\"\n",
+ "K = 5.2 * 10 ** - 3 # / mol L / min\n",
+ "\n",
+ "# Solution\n",
+ "a = 1 / (t * K)\n",
+ "print \"Initial concentration\", \"{:.3f}\".format(a), \"mol / L\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Initial concentration 3.205 mol / L\n"
+ ]
+ }
+ ],
+ "prompt_number": 13
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 5, Page no: 151"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "from math import log10\n",
+ "\n",
+ "# Solution\n",
+ "print \"99.9 % / 50 % =\",\n",
+ "times = round((2.303 * log10(100 / (100 - 99.9))) / (2.303 * log10(100 / (100 - 50))))\n",
+ "print times\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "99.9 % / 50 % = 10.0\n"
+ ]
+ }
+ ],
+ "prompt_number": 18
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 6, Page no: 151"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "from math import log10\n",
+ "\n",
+ "# Constants\n",
+ "R = 1.987 # cal / K / mol\n",
+ "\n",
+ "# Variables\n",
+ "T1 = 273.0 # K\n",
+ "T2 = 303.0 # K\n",
+ "K1 = 2.45 * 10 ** -5\n",
+ "K2 = 162 * 10 ** -5\n",
+ "\n",
+ "# Solution\n",
+ "Ea = log10(K2 / K1) * R * 2.303 / ((T2 - T1) / (T1 * T2))\n",
+ "print \"The activation energy of the reaction is\", int(Ea), \"cal / mol\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The activation energy of the reaction is 22968 cal / mol\n"
+ ]
+ }
+ ],
+ "prompt_number": 22
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 7, Page no: 151"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "t05 = 30 # minutes\n",
+ "a = 0.1 # M\n",
+ "\n",
+ "# Solution\n",
+ "print \"For second order reaction,\"\n",
+ "print \"t0.5 = 1 / Ka\"\n",
+ "K = 1 / (a * t05)\n",
+ "print \"The rate constant is\", \"{:.3f}\".format(K), \"mol / lit / min\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "For second order reaction,\n",
+ "t0.5 = 1 / Ka\n",
+ "The rate constant is 0.333 mol / lit / min\n"
+ ]
+ }
+ ],
+ "prompt_number": 23
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 8, Page no: 151"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "from math import log\n",
+ "\n",
+ "# Variables\n",
+ "T = 500 # C\n",
+ "Pi = 350 # torr\n",
+ "r1 = 1.07 # torr / s\n",
+ "r2 = 0.76 # torr / s\n",
+ "\n",
+ "# Solution\n",
+ "print \"1.07 = k(0.95a)^n\"\n",
+ "print \"0.76 = k(0.80a)^n\"\n",
+ "n = log(r1 / r2) / log(0.95 / 0.80)\n",
+ "print \"Hence, order of reaction is\", round(n)\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "1.07 = k(0.95a)^n\n",
+ "0.76 = k(0.80a)^n\n",
+ "Hence, order of reaction is 2.0\n"
+ ]
+ }
+ ],
+ "prompt_number": 4
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 9, Page no: 152"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Solution\n",
+ "print \"Applying steady state approximation to the concentration of NOCl2,\",\n",
+ "print \"we get\"\n",
+ "print \"d[NOCl2] / dt = 0 = k1 [NO] [Cl2] - k-1 [NOCl2] - k2 [NO] [NOCl2]\"\n",
+ "print \"[NOCl2] = k1 [NO] [Cl2] / (k-1 + k2 [NO])\"\n",
+ "print \"Now, the overall rate of reaction,\"\n",
+ "print \"d[NOCl2] / dt = k2 [NO] [NOCl2]\"\n",
+ "print \"From the above equations we get,\"\n",
+ "print \"(k1 k2 / k-1) * [NO]^2 * [Cl2], if k2[NO] << k-1\"\n",
+ "print \"k [NO]^2[Cl2], where k = k1 * k2 / k-1\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Applying steady state approximation to the concentration of NOCl2, we get\n",
+ "d[NOCl2] / dt = 0 = k1 [NO] [Cl2] - k-1 [NOCl2] - k2 [NO] [NOCl2]\n",
+ "[NOCl2] = k1 [NO] [Cl2] / (k-1 + k2 [NO])\n",
+ "Now, the overall rate of reaction,\n",
+ "d[NOCl2] / dt = k2 [NO] [NOCl2]\n",
+ "From the above equations we get,\n",
+ "(k1 k2 / k-1) * [NO]^2 * [Cl2], if k2[NO] << k-1\n",
+ "k [NO]^2[Cl2], where k = k1 * k2 / k-1\n"
+ ]
+ }
+ ],
+ "prompt_number": 5
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 10, Page no: 153"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "from math import log10\n",
+ "\n",
+ "# Constant\n",
+ "R = 1.987 # cal / K / mol\n",
+ "\n",
+ "# Variables\n",
+ "K2_K1 = 4 # factor increase\n",
+ "T1 = 27 # C\n",
+ "T2 = 47 # C\n",
+ "\n",
+ "# Solution\n",
+ "T1 += 273.0\n",
+ "T2 += 273.0\n",
+ "Ea = log10(4) * 2.303 * R * (T1 * T2 / (T2 - T1))\n",
+ "print \"The activation energy for the reaction is\", \"{:.2e}\".format(Ea),\n",
+ "print \"cal /mol\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The activation energy for the reaction is 1.32e+04 cal /mol\n"
+ ]
+ }
+ ],
+ "prompt_number": 2
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 11, Page no: 153"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "from math import log10\n",
+ "\n",
+ "# Variables\n",
+ "a = 1 # mole\n",
+ "x = 3 / 4.0 # reaction completed\n",
+ "\n",
+ "# Solution\n",
+ "K = (2.303 / 6) * log10(1 / (1 - x))\n",
+ "print \"The rate constant is\", \"{:.3f}\".format(K), \"/min\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The rate constant is 0.231 /min\n"
+ ]
+ }
+ ],
+ "prompt_number": 11
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 12, Page no: 153"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "from math import log10\n",
+ "\n",
+ "# Solution\n",
+ "print \"Let the initial concentration be 100, when x = 25\",\n",
+ "print \" t = 30 minutes\"\n",
+ "a = 100\n",
+ "x = 25.0\n",
+ "t = 30 # minutes\n",
+ "K = 2.303 / t * log10(a / (a - x))\n",
+ "t05 = 0.683 / K\n",
+ "t = 2.303 / K * log10(a / x)\n",
+ "print \"K =\", \"{:.2e}\".format(K), \"/ min\"\n",
+ "print \"T0.5 =\", \"{:.2f}\".format(t05), \"min\"\n",
+ "print \"t =\", \"{:.1f}\".format(t), \"min\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Let the initial concentration be 100, when x = 25 t = 30 minutes\n",
+ "K = 9.59e-03 / min\n",
+ "T0.5 = 71.21 min\n",
+ "t = 144.6 min\n"
+ ]
+ }
+ ],
+ "prompt_number": 15
+ }
+ ],
+ "metadata": {}
+ }
+ ]
+} \ No newline at end of file
diff --git a/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_6_Electrochemistry_2.ipynb b/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_6_Electrochemistry_2.ipynb
new file mode 100644
index 00000000..b15856da
--- /dev/null
+++ b/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_6_Electrochemistry_2.ipynb
@@ -0,0 +1,620 @@
+{
+ "metadata": {
+ "name": ""
+ },
+ "nbformat": 3,
+ "nbformat_minor": 0,
+ "worksheets": [
+ {
+ "cells": [
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Chapter 6: Electrochemistry"
+ ]
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 1, Page no: 180"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "from math import log10\n",
+ "\n",
+ "# Variables\n",
+ "T = 25 # C\n",
+ "E = 0.296 # V\n",
+ "Cu = 0.015 # M\n",
+ "\n",
+ "# Solution\n",
+ "Eo = E - 0.0296 * log10(Cu)\n",
+ "print \"The standard electrode potential is\", \"{:.3f}\".format(Eo), \"V\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The standard electrode potential is 0.350 V\n"
+ ]
+ }
+ ],
+ "prompt_number": 2
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 2, Page no: 180"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "from math import log10\n",
+ "\n",
+ "# Variables\n",
+ "T = 25 # C\n",
+ "Cu = 0.1 # M\n",
+ "Zn = 0.001 # M\n",
+ "Eo = 1.1\n",
+ "\n",
+ "# Solution\n",
+ "E = Eo + 0.0296 * log10(Cu / Zn)\n",
+ "print \"The emf of Daniell cell is\", \"{:.4f}\".format(E), \"V\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The emf of Daniell cell is 1.1592 V\n"
+ ]
+ }
+ ],
+ "prompt_number": 4
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 3, Page no: 180"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "from math import log10\n",
+ "\n",
+ "# Constant\n",
+ "R = 8.314 # J / K\n",
+ "F = 96500 # C / mol\n",
+ "\n",
+ "# Variables\n",
+ "Cu = 0.15 # M\n",
+ "Eo = 0.34 # V\n",
+ "T = 298 # K\n",
+ "n = 2 # moles\n",
+ "\n",
+ "# Solution\n",
+ "E = Eo + (2.303 * R * T) / (n * F) * log10(Cu)\n",
+ "print \"The single electrode potential for copper metal is\", \"{:.4f}\".format(E),\n",
+ "print \"V\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The single electrode potential for copper metal is 0.3156 V\n"
+ ]
+ }
+ ],
+ "prompt_number": 1
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 4, Page no: 181"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variable\n",
+ "Eo_Cu = 0.3370 # Cu+2 -> Cu\n",
+ "Eo_Zn = - 0.7630 # Zn -> Zn +2\n",
+ "\n",
+ "# Solution\n",
+ "Eo_cell = Eo_Cu - Eo_Zn\n",
+ "print \"Daniel cell is, Zn | Zn +2 || Cu+2 | Cu\"\n",
+ "print \"Eo (cell) is\", Eo_cell, \"V\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Daniel cell is, Zn | Zn +2 || Cu+2 | Cu\n",
+ "Eo (cell) is 1.1 V\n"
+ ]
+ }
+ ],
+ "prompt_number": 2
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 5, Page no: 181"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variable\n",
+ "Eo_Cu = 0.3370 # Cu+2 -> Cu\n",
+ "Eo_Cd = - 0.4003 # Cd -> Cd +2\n",
+ "\n",
+ "# Solution\n",
+ "Eo_cell = Eo_Cu - Eo_Cd\n",
+ "print \"Cell is, Cd | Cd +2 || Cu+2 | Cu\"\n",
+ "print \"Eo (cell) is\", Eo_cell, \"V\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Cell is, Cd | Cd +2 || Cu+2 | Cu\n",
+ "Eo (cell) is 0.7373 V\n"
+ ]
+ }
+ ],
+ "prompt_number": 4
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 6, Page no: 181"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constant\n",
+ "F = 96500 # C / mol\n",
+ "\n",
+ "# Variables\n",
+ "n = 2\n",
+ "T = 25 # C\n",
+ "Eo_Ag = 0.80 # Ag+ / Ag\n",
+ "Eo_Ni = - 0.24 # Ni+2 / Ni\n",
+ "\n",
+ "# Solution\n",
+ "Eo_Cell = Eo_Ag - Eo_Ni\n",
+ "print \"Standard free energy change,\"\n",
+ "delta_Go = - n * F * Eo_Cell\n",
+ "print delta_Go, \"J / mol\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Standard free energy change,\n",
+ "-200720.0 J / mol\n"
+ ]
+ }
+ ],
+ "prompt_number": 5
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 7, Page no: 181"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Solution\n",
+ "print \"-------------------------\"\n",
+ "print \"Reduction half reaction:\",\n",
+ "print \"2Fe+3 + 2e- --> 2Fe+2\"\n",
+ "print \"Oxidation half reaction:\",\n",
+ "print \"Fe - 2e- --> Fe+2\"\n",
+ "print \"Overall cell reaction :\",\n",
+ "print \"2Fe+3 + Fe --> 3Fe+2\"\n",
+ "\n",
+ "print \"-------------------------\"\n",
+ "print \"Reduction half reaction:\",\n",
+ "print \"Hg+2 + 2e- --> Hg\"\n",
+ "print \"Oxidation half reaction:\",\n",
+ "print \"Zn - 2e- --> Zn+2\"\n",
+ "print \"Overall cell reaction :\",\n",
+ "print \"Hg+2 + Zn --> Hg + Zn+2\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "-------------------------\n",
+ "Reduction half reaction: 2Fe+3 + 2e- --> 2Fe+2\n",
+ "Oxidation half reaction: Fe - 2e- --> Fe+2\n",
+ "Overall cell reaction : 2Fe+3 + Fe --> 3Fe+2\n",
+ "-------------------------\n",
+ "Reduction half reaction: Hg+2 + 2e- --> Hg\n",
+ "Oxidation half reaction: Zn - 2e- --> Zn+2\n",
+ "Overall cell reaction : Hg+2 + Zn --> Hg + Zn+2\n"
+ ]
+ }
+ ],
+ "prompt_number": 6
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 8, Page no: 181"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constant\n",
+ "F = 96500 # C / mol\n",
+ "\n",
+ "# Variables\n",
+ "E1o = - 2.48 # V\n",
+ "E2o = 1.61 # V\n",
+ "\n",
+ "# Solution\n",
+ "delta_G1 = - 3 * F * (- 2.48)\n",
+ "delta_G2 = - 1 * F * 1.61\n",
+ "print \"delta_G3 = delta_G1 + delta_G2\"\n",
+ "print \"delta_G3 = - 4 * F * E3o\"\n",
+ "E3o = (delta_G1 + delta_G2) / (- 4 * F)\n",
+ "print \"The reduction potential for the half-cell Pt/Ce, Ce+4\",\n",
+ "print \"is\", \"{:.4f}\".format(E3o), \"V\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "delta_G3 = delta_G1 + delta_G2\n",
+ "delta_G3 = - 4 * F * E3o\n",
+ "The reduction potential for the half-cell Pt/Ce, Ce+4 is -1.4575 V\n"
+ ]
+ }
+ ],
+ "prompt_number": 7
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 9, Page no: 182"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Solution\n",
+ "print \"Anodic half reaction :\",\n",
+ "print \" Cd --> Cd+2 + 2e-\"\n",
+ "print \"Cathodic half reaction :\",\n",
+ "print \"2H+ + 2e- --> H2\"\n",
+ "print \"-\" * 50\n",
+ "print \"Overall cell reaction :\",\n",
+ "print \"Cd + 2H+ <--> Cd+2 + H2\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Anodic half reaction : Cd --> Cd+2 + 2e-\n",
+ "Cathodic half reaction : 2H+ + 2e- --> H2\n",
+ "--------------------------------------------------\n",
+ "Overall cell reaction : Cd + 2H+ <--> Cd+2 + H2\n"
+ ]
+ }
+ ],
+ "prompt_number": 4
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 10, Page no: 182"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "from math import log10\n",
+ "\n",
+ "# Variables\n",
+ "T = 25 # C\n",
+ "Cu = 0.1 # M\n",
+ "Zn = 0.001 # M\n",
+ "Eo = 1.1 # V\n",
+ "\n",
+ "# Solution\n",
+ "print \"Zn(s) | Zn+2 (0.001M) || Cu+2(0.1M) | Cu(s)\"\n",
+ "Ecell = Eo + 0.0592 / 2 * log10(Cu / Zn)\n",
+ "print \"The emf of a Daniell cell is\", \"{:.4f}\".format(Ecell), \"V\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Zn(s) | Zn+2 (0.001M) || Cu+2(0.1M) | Cu(s)\n",
+ "The emf of a Daniell cell is 1.1592 V\n"
+ ]
+ }
+ ],
+ "prompt_number": 5
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 11, Page no: 182"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "from math import log10\n",
+ "\n",
+ "# Variables\n",
+ "pH = 7 # O2\n",
+ "Eo = 1.229 # V\n",
+ "pO2 = 0.20 # bar\n",
+ "\n",
+ "# Solution\n",
+ "print \"Nearnst's equation at 25C is,\"\n",
+ "print \"E = Eo - (0.0592 / 2) * log(1 / ([H+]^2 * [pO2]^ (1/2)))\"\n",
+ "E = Eo - (0.0592 / 2) * log10(1.0 / (((10 ** (- 7)) ** 2) * (pO2 ** (1 / 2.0))))\n",
+ "print \"The reduction potential for the reduction is\",\n",
+ "print \"{:.3f}\".format(E), \"V\"\n",
+ "# descrepency due to calculation error in the book"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Nearnst's equation at 25C is,\n",
+ "E = Eo - (0.0592 / 2) * log(1 / ([H+]^2 * [pO2]^ (1/2)))\n",
+ "The reduction potential for the reduction is 0.804 V\n"
+ ]
+ }
+ ],
+ "prompt_number": 6
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 12, Page no: 183"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "E_KCl = 0.2415 # V\n",
+ "E_cell = 0.445 # V\n",
+ "\n",
+ "\n",
+ "# Solution\n",
+ "print \"Emf of the cell is\"\n",
+ "print \"At 25C,\"\n",
+ "print \"E = Er - El = Eref - ((RT)/ F) * ln H+\"\n",
+ "pH = (E_cell - E_KCl) / 0.059\n",
+ "\n",
+ "Eo_cell = - 0.8277 # V\n",
+ "print \"Thus, equilibrium constant for the reaction\"\n",
+ "print \"\\t 2H2O --> H3O+ + OH- may be calculated as\"\n",
+ "K = 10 ** (Eo_cell / 0.0591)\n",
+ "print \"K =\", \"{:.0e}\".format(K)\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Emf of the cell is\n",
+ "At 25C,\n",
+ "E = Er - El = Eref - ((RT)/ F) * ln H+\n",
+ "Thus, equilibrium constant for the reaction\n",
+ "\t 2H2O --> H3O+ + OH- may be calculated as\n",
+ "K = 1e-14\n"
+ ]
+ }
+ ],
+ "prompt_number": 3
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 13, Page no: 183"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "EoSn = 0.15 # V\n",
+ "EoCr = - 0.74 # V\n",
+ "\n",
+ "# Solution\n",
+ "print \"3Sn+4 + 2Cr --> 3Sn+2 + 2Cr+3\"\n",
+ "Eo_cell = EoSn - EoCr\n",
+ "n = 6\n",
+ "K = 10 ** (n * Eo_cell / 0.0591)\n",
+ "print \"The equillibrium constant for th reaction is\", \"{:.2e}\".format(K)\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "3Sn+4 + 2Cr --> 3Sn+2 + 2Cr+3\n",
+ "The equillibrium constant for th reaction is 2.27e+90\n"
+ ]
+ }
+ ],
+ "prompt_number": 1
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 14, Page no: 184"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "T = 25 # C\n",
+ "Eo = - 0.8277 # V\n",
+ "\n",
+ "# Solution\n",
+ "print \"The reversible reaction,\"\n",
+ "print \"2H2O <--> H3O+ + OH-\"\n",
+ "print \"May be divided into two parts.\"\n",
+ "print \"2H2O + e- --> 1/2 H2 + OH- (cathode) Eo = -0.8277 V\"\n",
+ "print \"H2O + 1/2 H2 --> H3O+ + e- (anode) Eo = 0\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The reversible reaction,\n",
+ "2H2O <--> H3O+ + OH-\n",
+ "May be divided into two parts.\n",
+ "2H2O + e- --> 1/2 H2 + OH- (cathode) Eo = -0.8277 V\n",
+ "H2O + 1/2 H2 --> H3O+ + e- (anode) Eo = 0\n"
+ ]
+ }
+ ],
+ "prompt_number": 2
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem: 15, Page no: 184"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "E = 0.4 # V\n",
+ "\n",
+ "# Solution\n",
+ "print \"The cell is Pt(H2) | H+, pH2 = 1 atm\"\n",
+ "print \"The cell reaction is\"\n",
+ "print \"1/2 H2 --> H+ + e-\"\n",
+ "pH = E / 0.0591\n",
+ "print \"pH =\", \"{:.3f}\".format(pH)\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The cell is Pt(H2) | H+, pH2 = 1 atm\n",
+ "The cell reaction is\n",
+ "1/2 H2 --> H+ + e-\n",
+ "pH = 6.768\n"
+ ]
+ }
+ ],
+ "prompt_number": 4
+ }
+ ],
+ "metadata": {}
+ }
+ ]
+} \ No newline at end of file
diff --git a/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_7_Solid_State_2.ipynb b/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_7_Solid_State_2.ipynb
new file mode 100644
index 00000000..229b5da3
--- /dev/null
+++ b/Advanced_Engineering_Chemistry__by_Dr._M.R._Senapati/Chapter_7_Solid_State_2.ipynb
@@ -0,0 +1,431 @@
+{
+ "metadata": {
+ "name": ""
+ },
+ "nbformat": 3,
+ "nbformat_minor": 0,
+ "worksheets": [
+ {
+ "cells": [
+ {
+ "cell_type": "heading",
+ "level": 1,
+ "metadata": {},
+ "source": [
+ "Chapter 7: Solid State"
+ ]
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem 1, Page no: 209"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Solution\n",
+ "print \"Weiss indices \\t\\t\\t1/2, 2/3, infinity \\t2/3, 2, 1/3\"\n",
+ "print \"Reciprocal of Weiss indices 2, 3/2, 1/infinity \\t3/2, 1/2, 3\"\n",
+ "print \"Clear fractions\\t\\t\\t4, 3, 0 \\t3, 1, 6\"\n",
+ "print \"Miller indices \\t\\t\\t (430) \\t (316)\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Weiss indices \t\t\t1/2, 2/3, infinity \t2/3, 2, 1/3\n",
+ "Reciprocal of Weiss indices 2, 3/2, 1/infinity \t3/2, 1/2, 3\n",
+ "Clear fractions\t\t\t4, 3, 0 \t3, 1, 6\n",
+ "Miller indices \t\t\t (430) \t (316)\n"
+ ]
+ }
+ ],
+ "prompt_number": 3
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem 2, Page no: 209"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "from math import sqrt\n",
+ "\n",
+ "\n",
+ "# Variable\n",
+ "a = 450 # pm\n",
+ "\n",
+ "# Solution\n",
+ "d220 = a / sqrt(2 ** 2 + 2 ** 2 + 0)\n",
+ "print \"Interplanar spacing\", int(d220)\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Interplanar spacing 159\n"
+ ]
+ }
+ ],
+ "prompt_number": 5
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem 3, Page no: 209"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Solution\n",
+ "print \"Intercept \\t(a, b ,c)\\t\\t(a, 2b, c) \\t\\t(a, 2b, 2c) \\t\\t(infi, b, -c)\"\n",
+ "print \"Weiss indices\\t 1, 1, 1 \\t\\t 1, 2, 1 \\t\\t 1, 2, 2 \\t\\t infi, 1, -1\"\n",
+ "print \"Reciprocals \\t 1, 1, 1 \\t\\t 1, 1/2, 1 \\t\\t 1, 1/2, 1/2\\t\\t 0, 1, -1\"\n",
+ "print \"Miller indicec\\t (111) \\t\\t (212) \\t\\t (211) \\t\\t (011)\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Intercept \t(a, b ,c)\t\t(a, 2b, c) \t\t(a, 2b, 2c) \t\t(infi, b, -c)\n",
+ "Weiss indices\t 1, 1, 1 \t\t 1, 2, 1 \t\t 1, 2, 2 \t\t infi, 1, -1\n",
+ "Reciprocals \t 1, 1, 1 \t\t 1, 1/2, 1 \t\t 1, 1/2, 1/2\t\t 0, 1, -1\n",
+ "Miller indicec\t (111) \t\t (212) \t\t (211) \t\t (011)\n"
+ ]
+ }
+ ],
+ "prompt_number": 7
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem 4, Page no: 209"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "rNa = 0.98 * 10 ** - 10 # m\n",
+ "rCl = 1.81 * 10 ** - 10 # m\n",
+ "\n",
+ "# Solution\n",
+ "rr = rNa / rCl\n",
+ "print \"When the radius ration is\", \"{:.2f}\".format(rr),\n",
+ "print \", the coordination number is 6.\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "When the radius ration is 0.54 , the coordination number is 6.\n"
+ ]
+ }
+ ],
+ "prompt_number": 9
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem 5, Page no: 210"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Variables\n",
+ "rLi = 68 # pm\n",
+ "rF = 136. # pm\n",
+ "\n",
+ "# Solution\n",
+ "rr = rLi / rF\n",
+ "print \"Radius ratio =\", rr\n",
+ "print \"The structure of LiF is scc and C.N of Li+ = 6\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Radius ratio = 0.5\n",
+ "The structure of LiF is scc and C.N of Li+ = 6\n"
+ ]
+ }
+ ],
+ "prompt_number": 2
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem 6, Page no: 210"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "from math import sin\n",
+ "\n",
+ "\n",
+ "# Variables\n",
+ "lamda = 2 * 10 ** - 10 # m\n",
+ "theta = 30 # degrees\n",
+ "\n",
+ "# Solution\n",
+ "print \"For first-order reflection\"\n",
+ "d = lamda / (2 * sin(theta))\n",
+ "dist = 2 * d\n",
+ "print \"Hence, distance between planes is\", \"{:.0e}\".format(abs(dist)), \"m\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "For first-order reflection\n",
+ "Hence, distance between planes is 2e-10 m\n"
+ ]
+ }
+ ],
+ "prompt_number": 3
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem 7, Page no: 210"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "from math import sqrt\n",
+ "\n",
+ "\n",
+ "# Variables\n",
+ "r = 174.6 # pm\n",
+ "\n",
+ "# Solution\n",
+ "a = r * sqrt(8)\n",
+ "print \"For 200 plane: h = 2, k = 0, l = 0\"\n",
+ "d200 = a / sqrt(2 ** 2)\n",
+ "print \"d200 =\", \"{:.1f}\".format(d200), \"pm\"\n",
+ "print \"For 200 plane: h = 2, k = 2, l = 0\"\n",
+ "d220 = a / sqrt(2 ** 2 + 2 ** 2)\n",
+ "print \"d220 =\", d220, \"pm\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "For 200 plane: h = 2, k = 0, l = 0\n",
+ "d200 = 246.9 pm\n",
+ "For 200 plane: h = 2, k = 2, l = 0\n",
+ "d220 = 174.6 pm\n"
+ ]
+ }
+ ],
+ "prompt_number": 17
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem 8, Page no: 210"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constant\n",
+ "N = 6.023 * 10 ** 23\n",
+ "\n",
+ "# Variables\n",
+ "wt = 55.6\n",
+ "p = 0.29 # nm\n",
+ "n = 2\n",
+ "\n",
+ "# Solution\n",
+ "print \"For BCC pattern,\"\n",
+ "print \"number of atoms per unit cell = 2\"\n",
+ "d = n * (wt * 10 ** -3) / (N * (p * 10 ** - 9) ** 3)\n",
+ "print \"Density of the metal is\", \"{:.2e}\".format(d), \"kg / m^3\"\n",
+ "print \"Number of nearest enighbour for BCC = 8\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "For BCC pattern,\n",
+ "number of atoms per unit cell = 2\n",
+ "Density of the metal is 7.57e+03 kg / m^3\n",
+ "Number of nearest enighbour for BCC = 8\n"
+ ]
+ }
+ ],
+ "prompt_number": 4
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem 9, Page no: 210"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Solution\n",
+ "print \"Intercept \\t2a/2, 2b, c/3\"\n",
+ "print \"Weiss indices\\t1, 2, 1/3\"\n",
+ "print \"Reciprocals \\t1, 1/2, 3\"\n",
+ "print \"Miller indices\\t (216)\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Intercept \t2a/2, 2b, c/3\n",
+ "Weiss indices\t1, 2, 1/3\n",
+ "Reciprocals \t1, 1/2, 3\n",
+ "Miller indices\t (216)\n"
+ ]
+ }
+ ],
+ "prompt_number": 19
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem 10, Page no: 211"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "# Constant\n",
+ "N = 6.023 * 10 ** 23\n",
+ "\n",
+ "# Variables\n",
+ "D = 0.53 # g / cm ^ 3\n",
+ "MM = 6.94 # g / mol\n",
+ "n = 2\n",
+ "\n",
+ "# Solution\n",
+ "print \"For BCC pattern,\"\n",
+ "print \"number of atoms per unit cell = 2\"\n",
+ "V = D * N / (n * MM)\n",
+ "V = 1 / V\n",
+ "print \"Volume of a unit cell of lithium metal is\", \"{:.2e}\".format(V), \"cc\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "For BCC pattern,\n",
+ "number of atoms per unit cell = 2\n",
+ "Volume of a unit cell of lithium metal is 4.35e-23 cc\n"
+ ]
+ }
+ ],
+ "prompt_number": 23
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Problem 11, Page no: 211"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "from math import sqrt\n",
+ "\n",
+ "\n",
+ "print \"AB remain in BCC structure if the edge length is a then body diagonal\",\n",
+ "print \"is root(3)a\"\n",
+ "print \"root(3)a = 2(r+ + r-)\"\n",
+ "A = (sqrt(3) * 0.4123 - 2 * 0.81) / 2\n",
+ "print \"A+ =\", \"{:.2f}\".format(A), \"nm\"\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "AB remain in BCC structure if the edge length is a then body diagonal is root(3)a\n",
+ "root(3)a = 2(r+ + r-)\n",
+ "A+ = -0.45 nm\n"
+ ]
+ }
+ ],
+ "prompt_number": 25
+ }
+ ],
+ "metadata": {}
+ }
+ ]
+} \ No newline at end of file
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