diff options
Diffstat (limited to 'Basic_Principles_And_Calculations_In_Chemical_Engineering')
24 files changed, 133 insertions, 235 deletions
diff --git a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch1.ipynb b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch1.ipynb index 947cfb01..0948f57e 100644 --- a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch1.ipynb +++ b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch1.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:ad7d15642ee4e9d7fd8a276d1246f62e3d28aa177d39ecd9ac2c125ea04f5d33" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,9 +28,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "'''Finding the density'''\n", "\n", - "#let the total mass of mud be 100lbm\n", "#variables\n", "m_total=100.0; #lbm\n", "#70% by wt of mud is sand(SiO2)and remaining is water\n", @@ -70,9 +69,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "'''\n", - "Calculate the shear stress at the surface of the inner cylinder\n", - "'''\n", + "\n", "import math\n", "\n", "# variables\n", @@ -117,7 +114,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#problem on surface tension\n", + "\n", "# variablees\n", "l=0.10; #m (length of sliding part)\n", "f=0.00589; #N (pull due to 0.6 gm of mass)\n", @@ -155,7 +152,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#Convert 327 miles/hr into ft/s\n", + "\n", "\n", "# variables\n", "V=327. #miles/hr\n", @@ -193,7 +190,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#Convert 2.6 hours into seconds\n", + "\n", "\n", "# variables\n", "t=2.6 #hr\n", @@ -230,8 +227,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#Calculate the acceleration in ft/min^2\n", - "\n", + "#\n", "# variables\n", "m=10. #lbm\n", "F=3.5 #lbf\n", @@ -269,7 +265,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "#Calculate the wt of metallic aluminium deposited in an electrolytic cell\n", "\n", "# variables\n", "I=50000. #Ampere or Coulumbs/sec\n", diff --git a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch10.ipynb b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch10.ipynb index 621beb27..e4b7fe7d 100644 --- a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch10.ipynb +++ b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch10.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:9f0f51ee792551db4a5ae3ded00fa549611bdd66fece52d68af61c7a164f38e5" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,9 +28,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Reaction in which Fraction Conversion is specified\n", "\n", - "# Variables \n", "F = 100 # feed to the reactor-[g mol]\n", "CH4 = 0.4*F # [g mol]\n", "Cl2 = 0.5*F ; # [g mol]\n", @@ -112,7 +111,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# A reaction in which Fraction Conversion is to beCalculated\n", + "\n", "\n", "# Variables \n", "S = 5000. ; # Sulphur [lb]\n", @@ -182,7 +181,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Material Balances for Process in which two Simultaneous Reactions Occur\n", "\n", "# Variables \n", "F = 1 #CH3OH -[gmol]\n", @@ -280,7 +278,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Analysis of Bioreactor\n", + "\n", "from numpy import matrix\n", "\n", "# Variables \n", @@ -356,7 +354,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Solution using Elemental Balances\n", + "\n", "from numpy import matrix\n", "\n", "# Variables \n", @@ -507,7 +505,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Use of Elemental Balance to Solve a Hydrocracking Problem\n", + "\n", "from numpy import matrix\n", "\n", "# Variables \n", @@ -560,7 +558,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Excesss Air\n", "\n", "# Variables \n", "C3H8 = 20 #C3H8 burned in a test-[kg]\n", @@ -605,7 +602,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# A Fuel Cell to generate Electricity from Methane\n", + "\n", "\n", "# Variables\n", "F = 16. # feed of CH4 -[kg]\n", @@ -682,7 +679,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Combustion of Coal\n", "\n", "# Variables\n", "F = 100. # feed of coal -[lb]\n", diff --git a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch11.ipynb b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch11.ipynb index 9592fff3..70f855c2 100644 --- a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch11.ipynb +++ b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch11.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:03c09e4ffd933027d277b1c64cc2c94bd3c72b7cbc229c1b8170ffd14e813958" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,7 +28,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determination of the Number of Independent Material Balance in a process with Multiple Units\n", + "\n", "\n", "# Variables \n", "\n", @@ -122,7 +123,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Material Balances for Multiple Units in which no Reaction occurs\n", + "\n", "\n", "from numpy import matrix\n", "\n", @@ -201,7 +202,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Material Balance for problems Involving Multiple units and Reactions\n", "\n", "from numpy import matrix\n", "\n", @@ -299,8 +299,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Analysis of Sugar Recovery Process involving Multiple Serial Units\n", - "# Solution fig E11.4\n", + "\n", "from numpy import matrix\n", "\n", "# Variables \n", @@ -440,7 +439,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Production of a Hormone in connected Reactor\n", + "\n", "\n", "# Variables \n", "F = 15. #[L/hr]\n", diff --git a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch13.ipynb b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch13.ipynb index b72b411d..d6a85197 100644 --- a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch13.ipynb +++ b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch13.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:86277517338e3080962ec366bf78a36ead36dc032944d5f67a8c58022c6af85a" }, "nbformat": 3, "nbformat_minor": 0, @@ -279,8 +280,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "\t\t\t# Example 13.7 Page no. 416\n", - "\t\t\t# Solution fig E13.7\n", + "\n", "\n", "# Variables\n", "G = 100. ;\t\t\t# Basis: Pyrolysis Gas-[lb mol] \n", diff --git a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch15.ipynb b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch15.ipynb index c6c7dffb..e0ee646a 100644 --- a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch15.ipynb +++ b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch15.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:eeb1c8da856a86d3cb60a72e738f1fe4c7b2d7aaa546df7d68c6871754268745" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,7 +28,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Application of Van der Walls Equation to Calculate a Temperature\n", "\n", "# variables\n", "R = 82.06 # gas constant-[(cm**3 *atm)/(g mol *K)]\n", diff --git a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch19.ipynb b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch19.ipynb index dc3cb7a9..509330f3 100644 --- a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch19.ipynb +++ b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch19.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:c896c859a24a6b70446a5e83cded412ac42718005bc7d2e546816e8274c18e21" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,10 +28,8 @@ "cell_type": "code", "collapsed": false, "input": [ - "'''Calculating the number of degrees to freedom'''\n", "\n", - "# Use phase rule to get degree of freedom(F) = 2-P+C \n", - "# (a)\n", + "\n", "N1 = 1.;\n", "P1 = 1. ;\t\t\t# Number of phases present\n", "C1 = 1. ;\t\t\t#Number of components present\n", @@ -95,10 +94,8 @@ "cell_type": "code", "collapsed": false, "input": [ - "'''Calculating the number of degrees to freedom'''\n", "\n", - "# Use phase rule to get degree of freedom(F) = 2-P+C \n", - "# (a)\n", + "\n", "N1 = 5.;\n", "P1 = 1.; \t\t\t# Number of phases present,here 1 gas \n", "C1 = 3. ;\t\t\t#Number of independent components present,here 3 because 3 elements(C,O and H)\n", @@ -143,7 +140,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "'''Bubble point calculation'''\n", "\n", "from scipy.optimize import fsolve\n", "import math\n", @@ -211,7 +207,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "'''Calculating the fraction of liquid that will remain in equilibrium'''\n", "\n", "# Variables\n", "# Basis : 100 g solution\n", @@ -271,7 +266,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "'''Seperation of virus from a culture'''\n", "\n", "# Variables\n", "Vo = 3.0 ;\t\t\t# Initial volume of the solution containing the culture and virus-[L]\n", diff --git a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch2.ipynb b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch2.ipynb index d803af44..84439d15 100644 --- a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch2.ipynb +++ b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch2.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:ef26cf09debc2accb827957d575ac9576db35c1e13d184b4161dad1098add2f0" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,7 +28,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# calculate specific weight of water\n", + "\n", "\n", "# variables\n", "g=32.2; #ft/s^2\n", @@ -68,7 +69,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#calc pressure at depth of 304.9m\n", + "\n", "\n", "# variables\n", "d=304.9; #m\n", @@ -108,7 +109,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "#gauge pressure=(density)*(acc. due to gravity)*(depth)\n", "\n", "# variables\n", "rho_oil=55.; #lbm/ft^3\n", @@ -153,7 +153,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculate the pressures\n", + "\n", "import math\n", "\n", "# varirbles\n", @@ -213,7 +213,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#calc pressuer at different heights considering on density change in air\n", + "\n", "\n", "# variables\n", "p_atm=14.7; #psia\n", @@ -275,7 +275,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# calculate the atmosphere\n", + "\n", "import math\n", "\n", "# variables\n", @@ -319,7 +319,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# calculate net pressure.\n", + "\n", "import math\n", "\n", "# variables\n", @@ -366,7 +366,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "#calc the total force on a lock gate\n", "\n", "# variables\n", "#lock gate has water on one side and air on the other at atm. pressure\n", @@ -414,7 +413,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#calc thickness of an oil storage\n", + "\n", "sigma_tensile=20000. #lbf/in^2 (tensile stress is normally 1/4 rupture stress)\n", "\n", "#max pressure is observed at the bottom of the storage\n", @@ -456,7 +455,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "#calc thickness of a storage tank\n", "\n", "# variables\n", "p_working=250.0; #lbf/in^2\n", @@ -498,7 +496,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#calc payload of a helium balloon\n", + "\n", "import math\n", "\n", "# variables\n", @@ -548,7 +546,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "#wooden block floating in two phase mix of water and gasoline\n", "\n", "# variables\n", "#calc fraction of block in water\n", @@ -588,7 +585,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#calc gauge pressure of cylinder in a manometer\n", + "\n", "\n", "# variables\n", "#height of water above pt.C = 2.5ft\n", @@ -631,7 +628,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#calc pressure diff between two tanks in a two liquid manometer\n", + "\n", "rho_water=62.3; #lbm/ft^3\n", "SG_oil=1.1;\n", "rho_oil=SG_oil*(rho_water);\n", @@ -674,7 +671,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "#calc pressure of gauge through a spring piston system\n", "\n", "# variables\n", "k=10000.; #N/m (spring constant)\n", @@ -714,7 +710,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#calc pressure diff at the mouth of the fire place\n", + "\n", "\n", "# variables\n", "g=32.2; #ft/s^2\n", @@ -756,7 +752,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# calculate the gauge pressure at the bottom of the tank.\n", "\n", "# variables\n", "rho_water=1000. #Kg/m^3\n", @@ -811,7 +806,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# calculate angle\n", + "\n", "import math\n", "\n", "# variables\n", @@ -853,7 +848,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "#calc the height to which liq in a cylinder rises when rotated\n", "\n", "import math\n", "# variables\n", @@ -895,7 +889,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#calc thickness of liquid strip at the bottom of the industrial centrifuge\n", + "\n", "import math\n", "\n", "# variables\n", diff --git a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch20.ipynb b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch20.ipynb index 9286e99b..2a777cf6 100644 --- a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch20.ipynb +++ b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch20.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:160cdac5d7f0b7135dad8dda86f1147a9289b5d9942c1ebb05ca32b461c42f4f" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,7 +28,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Fitting Adsorption Isotherms to Experimental Data\n", "\n", "%pylab inline\n", "\n", @@ -75,7 +75,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Seperation of Biochemicals by Solvent Extraction\n", + "\n", "\n", "# Variables\n", "G = 1000.0 ;\t\t\t# Volume of solution - [L]\n", @@ -116,7 +116,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Combination of an Adsorption Isotherm with a Meterial Balance\n", "\n", "# Variables\n", "G = 1000. ;\t\t\t# Volume of solution - [L]\n", diff --git a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch21.ipynb b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch21.ipynb index 741dcc7d..69c36534 100644 --- a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch21.ipynb +++ b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch21.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:63761cd2f20f542c8cf7d5599bfa09993cda87c6763136710915fa76185904f1" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,7 +28,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of Mechanical work by a gas on a piston showing how the path affects the value of the work\n", + "\n", "\n", "from scipy.integrate import quad\n", "\n", @@ -78,7 +79,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of Specific Kinetic energy for a Flowing fluid\n", + "\n", "\n", "# Variables\n", "id_ = 3. ;\t\t\t# Internal diameter of tube-[cm]\n", @@ -119,7 +120,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of potential Energy change of water\n", + "\n", "\n", "# Variables\n", "# Let water level in first reservoir be the reference plane\n", @@ -157,7 +158,7 @@ "cell_type": "code", "collapsed": true, "input": [ - "# Calculation of an internal energy change using the heat capacity\n", + "\n", "\n", "# Variables\n", "#Constant volume process \n", @@ -200,7 +201,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of Enthalpy change\n", "\n", "# Variables\n", "#Constant pressure process \n", diff --git a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch22.ipynb b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch22.ipynb index 01acfa93..52b1e9dd 100644 --- a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch22.ipynb +++ b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch22.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:378027dede13493be733241ad48420c91ebbcd1218fa032fc3c46fa099a45a58" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,7 +28,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Application of the energy balance to a closed system\n", + "\n", "\n", "# Variables\n", "#Assume that properties of water can be used to substitute properties of solution\n", @@ -75,7 +76,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of U using American engineering units\n", + "\n", "\n", "# Variables\n", "# Given\n", @@ -134,7 +135,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# use of the general energy balance to analyze an open , unsteady-state system\n", + "\n", "\n", "# Variables\n", "#Lets take tank to be system\n", @@ -180,7 +181,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# application of the energy balance to a open, steady-state system, a heat exchanger\n", + "\n", "\n", "# Variables\n", "# Take milk plus water in tank to be system\n", @@ -241,7 +242,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of power needed to pump water in an open, steady state system\n", + "\n", "\n", "# Variables\n", "# Take pipe between initial and final level of water\n", diff --git a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch23.ipynb b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch23.ipynb index 6773ceb9..78279b16 100644 --- a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch23.ipynb +++ b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch23.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:85497d817768e6e1d81546cc4adcb855eed2a97589497e4f8a3f22d0bc4a6c3d" }, "nbformat": 3, "nbformat_minor": 0, @@ -28,7 +29,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Graph that showing the heat of vaporization of water\n", "\n", "%pylab inline\n", "from matplotlib.pyplot import *\n", @@ -77,7 +77,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# comparison of various sources to estimate the heat of vaporization\n", "\n", "import math\n", "\n", @@ -139,7 +138,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Conversion of units in a heat capacity equation\n", + "\n", "\n", "# Variables\n", "c = 2.675*10**4 #*.4536)/(1055*1.8) ;\n", @@ -182,7 +181,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Fitting Heat Capacity Equation to Heat Capacity Data\n", "\n", "\n", "# Variables\n", @@ -235,7 +233,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of H for a gas mixture using heat capacity equation for each component\n", + "\n", "\n", "from scipy.integrate import quad\n", "# Variables\n", @@ -318,7 +316,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of the Change in Enthalpy for a Gas using Tabulated Enthalpy Values\n", + "\n", "\n", "\n", "# Solution \n", @@ -362,9 +360,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "#Use of Steam Tables to Calculate Change in Enthalpy\n", - "\n", - "# Solution Fig.E23.7\n", "\n", "# Variables\n", "#Given\n", @@ -423,7 +418,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Use of Steam Table when a Phase Change is involved to Calculate the final State of Water\n", + "\n", "\n", "\n", "# Solution \n", @@ -473,7 +468,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculate Enthalpy Difference betwee two States by Pressure Enthalpy Chart for Butane\n", "\n", "\n", "# Solution \n", diff --git a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch24.ipynb b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch24.ipynb index 00a323af..b4b06951 100644 --- a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch24.ipynb +++ b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch24.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:81bdcd8b52f99578fa3372035df0b4461d5784b0d3f676ae0e588533ba351cbf" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,11 +28,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# simplification of the general energy balance\n", "\n", - "# Solution Fig. E24.1\n", - "\n", - "# Assumptions to be made in eqn. 24.1 in following segment \n", "print 'Assumptions to be made in eqn. 24.1 in following segments are:'\n", "#(a)- 1 to 5\n", "print '(a)- 1 to 5.'\n", @@ -120,7 +117,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Application of the energy balance.\n", + "\n", "\n", "# Variables\n", "# Given\n", @@ -167,7 +164,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Application of the energy balance to plasma etching.\n", + "\n", "\n", "from scipy.optimize import fsolve\n", "\n", @@ -229,7 +226,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Energy balance applied to a batch process\n", "\n", "# Variables\n", "# Pick the system as shown in above figure of book\n", @@ -322,7 +318,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# application of the energy balance to pumping water\n", "\n", "from scipy.optimize import fsolve\n", "\n", @@ -389,8 +384,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# application of the energy balance, to heat a biomass.\n", - "\n", + "#\n", "# Variables\n", "# Pick the system as shown in above figure of book\n", "# Given\n", @@ -438,9 +432,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Sterilization of a Fermentation Medium\n", "\n", - "# Pick the system of whole process as shown in above figure of book\n", "# Given\n", "Q = 1.63 ;\t\t\t# Heat loss from the process - [ kW ]\n", "m_bm = 150 ;\t\t\t# Mass flow rate of biological media into the sterlizer -[kg/min]\n", @@ -486,7 +478,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Use of combined meterial and energy balances to solve a distillation problem.\n", + "\n", "\n", "# Variables\n", "F = 20000 ;\t\t\t# Feed rate of saturated liquid - [kg/h]\n", diff --git a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch25.ipynb b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch25.ipynb index 66cbaa91..8e33f5fb 100644 --- a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch25.ipynb +++ b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch25.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:da2384fa5db2cbd49ec84301569b45dd22f0d12dd2e12e0fa83528eb61b2d43b" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,7 +28,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determination of a heat of formation from heat transfer measurements\n", "\n", "# Variables\n", "Qa = -393.51 ;\t\t\t# Heat of reaction of reaction (a) - [kJ/g mol C] \n", @@ -66,7 +66,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Retrival of heats of formation from reference data.\n", "\n", "# Variables\n", "H_H2 = 0 ;\t\t\t# Standard heat of formation of H2 -[kJ/ g mol H2]\n", @@ -104,7 +103,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of the standard heat of reaction from the standard heats of formation.\n", + "\n", "\n", "# Variables\n", "H_fNH3 = -46.191 ;\t\t\t# Standard heat of formation of NH3 -[kJ/ g mol]\n", @@ -143,7 +142,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# calculation of the heat of reaction at a temparature different from the standard conditions.\n", "\n", "# Variables\n", "P1 = 1. ;\t\t\t# Initial pressure - [atm]\n", @@ -201,7 +199,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of the Heat Transfer using Heat of Reaction in a Process in\n", "\n", "# Variables\n", "m_CO2 = 1. ;\t\t\t# Moles of CO2 - [ g mol]\n", @@ -272,7 +269,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of the enthalpy change in anerobic culture.\n", "\n", "# Variables\n", "H_EtOH =-1330.51 ;\t\t\t# Change in enthalpy of ethanol -[kJ/g mol]\n", @@ -321,7 +317,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Green Chemistry Examining Alternate Processes\n", "\n", "\n", "# Solution \n", @@ -384,10 +379,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of the Heat of Reaction at a Tempera-\n", "\n", - "#ture different from the Standard Conditions with Heat of Formation Merged\n", - "#with Sensible Heat\n", "# Variables\n", "P1 = 1. ;\t\t\t# Initial pressure - [atm]\n", "P2 = 1. ;\t\t\t# Final pressure - [atm]\n", @@ -442,7 +434,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of the Heat Transfer when Reactants enter and Products leave at Different Temperatures\n", + "\n", "\n", "# Solution \n", "\n", @@ -498,7 +490,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Heating Value of Coal\n", + "\n", "\n", "# Solution \n", "\n", @@ -548,9 +540,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Selecting a Fuel to reduce SO2 emissions\n", "\n", - "# Solution \n", "\n", "# Variables\n", "H_req = 10**6 ;\t\t\t# Heat requirement - [Btu]\n", diff --git a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch26.ipynb b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch26.ipynb index 5268900c..5000414f 100644 --- a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch26.ipynb +++ b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch26.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:98deaafae63448982b8112f9e6ce85846fb35bc262bd2facf3329e5947fa2984" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,7 +28,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of an adiabetic reaction temperature.\n", + "\n", "\n", "# Variables\n", "m1_CO = 1.; \t\t\t# Moles of CO input- [g mol]\n", @@ -106,9 +107,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Application of general Energy Balance in a Process in which More than one Reaction Occurs\n", - "\n", - "# Solution Fig E26.3b\n", "\n", "# Variables\n", "v_CH4 = 1000. ;\t\t\t# Volume of CH4 taken - [ cubic feet]\n", @@ -175,9 +173,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Application of general Energy Balance in a Process Composed of Multiple Units\n", - "\n", - "# Solution Fig E26.4b\n", "\n", "# Variables\n", "SO2_in = 2200. ;\t\t\t# Amount of SO2 entering reactor 2-[lb mol/hr]\n", @@ -254,9 +249,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Production of Citric Acid by Fungus\n", - "\n", - "# Solution \n", + " \n", "\n", "# Variables\n", "CA = 10000. ;\t\t\t# Produced citric acid - [kg]\n", diff --git a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch27.ipynb b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch27.ipynb index 0515e5c2..4bcff200 100644 --- a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch27.ipynb +++ b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch27.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:21747075c112c6cd9e1a0a4f001fec6264fd627d603e23ce68da0341f7d86ac0" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,8 +28,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of the Work done during Evaporation of a Liquid\n", - "# Solution E27.1\n", + "\n", "\n", "# Variables\n", "V_w = 1. ;\t\t\t# Volume of given water -[L]\n", @@ -71,8 +71,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of Work in a Batch Process\n", - "# Solution E27.2\n", + "\n", "\n", "# Variables\n", "m_N2 = 1. ;\t\t\t# Moles of N2 taken -[kg mol]\n", @@ -122,8 +121,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Efficiency of Power Generation by a Hydroelectric Plant\n", - "# Solution \n", + "\n", "\n", "# Variables\n", "p_plant = 20. ;\t\t\t# Power generated by plant-[MW]\n", @@ -165,8 +163,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of Plant Efficiency\n", - "# Solution Fig.E27.4\n", + "\n", "\n", "# Variables\n", "LHV = 36654. ;\t\t\t# LHV value of fuel - [kJ/ cubic metre]\n", @@ -220,7 +217,6 @@ "cell_type": "code", "collapsed": true, "input": [ - "# Comparison of the reversible work for a batch process with that of a flow process operating under the same conditions.\n", "\n", "from scipy.integrate import quad\n", "\n", @@ -279,7 +275,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Application of the mechanical energy balance to the pumping water\n", "\n", "from scipy.integrate import quad\n", "# Variables\n", diff --git a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch28.ipynb b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch28.ipynb index 6a34dc72..f3a9553e 100644 --- a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch28.ipynb +++ b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch28.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:ac2f423a0dd7909a3558159c9b6408459426072d293b0494654db2eec3dde604" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,9 +28,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Application of Heats of Solution data\n", "\n", - "# Solution \n", "# Variables\n", "Ref_T = 77. ;\t\t\t#Reference temperature-[degree F]\n", "\n", @@ -94,7 +93,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Application of the heat of solution data\n", + "\n", "\n", "from scipy.integrate import quad\n", "# Variables\n", @@ -164,9 +163,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Application of an Enthalpy Concentration Chart\n", - "\n", - "# Solution fig. 28.3\n", "\n", "# Variables\n", "soln1 = 600. ; \t\t\t# Mass flow rate of entering solution 1 -[lb/hr]\n", diff --git a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch29.ipynb b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch29.ipynb index db601ca5..7c95dcbe 100644 --- a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch29.ipynb +++ b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch29.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:b5b2fcf9bb3d537cea245cafaa4a19d4d1dc42af6ab432d7e1ef22a8e48ae245" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,9 +28,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# determining properties of moist air from the humidity chart\n", "\n", - "# Variables\n", "DBT = 90. ;\t\t\t# Dry bulb temperature - [degree F]\n", "WBT = 70. ;\t\t\t# Wet bulb temperature - [degree F]\n", "\n", @@ -70,9 +69,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Heating at constant Humidity\n", "\n", - "# Solution fig. E29.2\n", "\n", "# Variables\n", "DBT1 = 38 ;\t\t\t# Initial dry bulb temperature - [degree C]\n", @@ -125,9 +122,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Cooling and Humidification using a Water Spray\n", "\n", - "# Solution fig. E29.3b\n", "\n", "# Variables\n", "DBT1 = 40 ;\t\t\t# Initial dry bulb temperature - [degree C]\n", @@ -171,9 +166,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Combined Material and Energy Balance for a Cooling Tower\n", - "\n", - "# Solution fig. E29.4\n", "\n", "# Variables\n", "c_bl = 8.30 * 10**6 ;\t\t\t# Capacity of blower - [cubic feet/hr]\n", @@ -235,9 +227,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Drying of Chlorella\n", "\n", - "# Solution fig. E29.5\n", "\n", "# Variables\n", "W = 100 ;\t\t\t# Amount of entering water -[lb/hr]\n", diff --git a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch3.ipynb b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch3.ipynb index af8703d1..4e398ea9 100644 --- a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch3.ipynb +++ b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch3.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:445dec12235c400efa979dcf04faa2911a77ac6433ec8e786b9205e0e8fdeeb4" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,7 +28,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#Calculate vol. flow rate, mass flow rate and average vel of gasoline through pipe\n", + "\n", "import math\n", "\n", "# variables\n", @@ -73,7 +74,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#calculate velocity and mass flow rate of natural in a pipe\n", + "\n", "import math\n", "\n", "# variables\n", @@ -119,7 +120,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#calculate the mass flow rate, volumetric flow rate and velocity of waterin a pipe\n", + "\n", "import math\n", "\n", "# variables\n", @@ -167,7 +168,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#calulate the time required\n", + "\n", "import math\n", "\n", "# variables\n", @@ -207,7 +208,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "#calculate the final or steady state pressure in tank\n", "\n", "# variables\n", "m_in=0.0001; #lbm/min\n", @@ -247,7 +247,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#calculate how fast the level of water is rising or falling in a cylindrical tank\n", + "\n", "import math\n", "\n", "# variables\n", @@ -302,7 +302,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "#calculate flow rate of ventilation air supply\n", "\n", "# variables\n", "q=5/8.0; #kg/hr mass evaporation rate of benzene\n", diff --git a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch4.ipynb b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch4.ipynb index 392607c8..7ed88091 100644 --- a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch4.ipynb +++ b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch4.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:16617b0214df1f3fa0b6950901fd2bc173679187633649259f00cd5dd8aa8d5e" }, "nbformat": 3, "nbformat_minor": 0, @@ -28,8 +29,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Temperature Conversion\n", - "# Solution\n", + "\n", "\n", "# Variable\n", "#(a)\n", @@ -74,8 +74,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Temperature Conversion\n", - "# Solution\n", + "\n", "\n", "# Variables\n", "c = 139.1 + (1.56*10**-1)*(-460-32)/1.8 ;\n", diff --git a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch5.ipynb b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch5.ipynb index 5023ef53..7c4d25d6 100644 --- a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch5.ipynb +++ b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch5.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:17452ca2e9b7dcffa8d444e8e6e3bb3b7f47f9f947558729a784ae56a1f45de2" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,8 +28,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Pressure Conversion\n", - "# Solution\n", "\n", "# Variables\n", "P = 60 ; #[Gpa]\n", @@ -78,8 +77,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Pressure Conversion\n", - "# Solution\n", + "\n", "\n", "# Variable\n", "b_rd = 28.0 ; #[in. Hg]\n", @@ -117,8 +115,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Vacuum Pressure Reading\n", - "# Solution\n", "\n", "# Variables\n", "b_rd = 100.0 ; #[kPa]\n", @@ -158,8 +154,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of Pressure Difference\n", - "# Solution\n", + "\n", "\n", "# Variables\n", "df = 1.10*10**3 ; #[kg/m**3]\n", @@ -198,8 +193,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Pressure Conversion\n", - "# Solution\n", + "\n", "\n", "# Variables\n", "p_atm=730.0*29.92/760.0 ; #[in. Hg]\n", diff --git a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch6.ipynb b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch6.ipynb index 5ffa4f19..572f406f 100644 --- a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch6.ipynb +++ b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch6.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:829300ed441b0056de124b3c59bbb1f7034cd4f5704a4d95b4ff6c77357fd0c5" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,8 +28,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# A Material Balance for the blending of Gasoline\n", - "# Solution\n", + "\n", "from numpy import matrix\n", "\n", "# Variables\n", @@ -83,8 +83,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Concentration of cells using a Centrifuge\n", - "# Solution\n", + "\n", "\n", "# Variables\n", "fd= 1000.0 ; #feed rate-[L/hr]\n", @@ -124,10 +123,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Discharge of Tank Residuals to the Environment\n", - "# Solution\n", "\n", - "# Variables\n", "dn = 0.80 ; #Density of motor oil-[g/cm**3]\n", "\n", "# Calculation and Result\n", diff --git a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch7.ipynb b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch7.ipynb index 759dde83..f1754ae4 100644 --- a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch7.ipynb +++ b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch7.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:702f6d54433444391f54642fccdef71d5ded6c19433d61198181ed7204437113" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,8 +28,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Understanding the Problem\n", - "# Solution\n", + "\n", "\n", "# Variables\n", "v_ts = 105.0 ; # velocity of train wrt station-[cm/s]\n", @@ -69,8 +69,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Drawing a Sketch of a Mixing Process\n", - "# Solution\n", + "\n", "\n", "# Variables\n", "n_un= 7 ; # Number of unknowns in the given problem- 3 values of xi and 4 values Fi\n", @@ -107,8 +106,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Placing the unknown Information on the Diagram\n", - "# Solution\n", "\n", "# variables\n", "n_un=8 ; # Number of unknowns in the given problem- 8 values of mole fractions\n", diff --git a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch8.ipynb b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch8.ipynb index 4d600c4f..350e9391 100644 --- a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch8.ipynb +++ b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch8.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:db3a394cd915f3675da3a1ec91e93913eb152d495576bd0a47778fe0952f79fb" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,8 +28,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Extraction of Streptomycin from a Fermentation Broth\n", - "# Solution\n", + "\n", "\n", "# Variables\n", "# Basis : 1 min\n", @@ -79,8 +79,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Separation of gases Using a Membrane\n", - "# Solution Fig. E8.2b\n", + "\n", "\n", "# Variables\n", "F_O2 = 0.21 ; # fraction of O2 in feed(F) \n", @@ -131,8 +130,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Overall analysis for a continuous Distillation Column\n", - "# Solution\n", + "\n", "\n", "# Variables\n", "# Basis : 1 hr so F = 1000 kg\n", @@ -192,8 +190,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Mixing of Battery Acid\n", - "# Solution Fig E8.4\n", + "\n", "from numpy import matrix\n", "\n", "# Variables\n", @@ -243,8 +240,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Drying\n", - "# Solution Fig E8.5\n", + "\n", "from numpy import matrix\n", "\n", "# Variables\n", @@ -289,8 +285,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Crystallizaton\n", - "# Solution\n", "\n", "# Variables\n", "# Composition of initial solution at 30 degree C\n", @@ -359,8 +353,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Hemodialysis\n", - "# Solution\n", + "\n", "\n", "# Variables\n", "# Write given data\n", diff --git a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch9.ipynb b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch9.ipynb index 4b127966..53f8e501 100644 --- a/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch9.ipynb +++ b/Basic_Principles_And_Calculations_In_Chemical_Engineering/ch9.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:fa0721f1d96e3929565a094cfe21c7d86b4e801aa71b0940b32ef9174b4285dc" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,8 +28,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Balancing a reaction for a Biological Reaction\n", - "# Solution\n", + "\n", "\n", "# variables\n", "# Given \n", @@ -75,8 +75,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Use of Chemical Reaction to Calculate the Mass of Reactants given the Mass of Products\n", - "# Solution\n", + "\n", "\n", "# Variables\n", "m_CO2 = 44.0 ; #molecular wt-[g]\n", @@ -116,8 +115,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Application of Stoichiometry when more than one Reaction occurs\n", - "# Solution\n", + "\n", "\n", "# Variables\n", "m_CaCO3 = 100.1 ; #molecular wt-[g]\n", @@ -177,8 +175,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of extent of Reaction\n", - "# Solution\n", + "\n", "\n", "# Variables\n", "f_NH3 = 5. ; # NH3 in feed-[g]\n", @@ -250,8 +247,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of Limiting and Excess Reactants\n", - "# Solution\n", + "\n", "\n", "# Variables\n", "f_N2 = 10. ; # N2 in feed-[g]\n", @@ -316,8 +312,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Yeilds in the Reaction of Glucose to produce Ethanol\n", - "# Solution\n", + "\n", "\n", "# variables\n", "#(a)\n", @@ -361,8 +356,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Selectivity in the Production of Nanotubes\n", - "# Solution\n", "\n", "# Variables\n", "# By using reaction (a)\n", @@ -400,8 +393,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of various terms Pertaning to Reaction\n", - "# Solution\n", + "\n", "\n", "# Variables\n", "m_C3H6 = 42.08 # molecular wt. of propene-[g]\n", |