From d36fc3b8f88cc3108ffff6151e376b619b9abb01 Mon Sep 17 00:00:00 2001 From: kinitrupti Date: Fri, 12 May 2017 18:40:35 +0530 Subject: Revised list of TBCs --- .../Sample.S._Fogler.ipynb | 231 +++++++++++++++++++++ .../Sample.S._Fogler_UPDATED.ipynb | 231 +++++++++++++++++++++ .../Sample.S._Fogler_UPDATED_(1).ipynb | 191 +++++++++++++++++ .../AjaySatish/Sample_H.S._Fogler.ipynb | 231 --------------------- .../AjaySatish/Sample_H.S._Fogler_UPDATED.ipynb | 231 --------------------- .../Sample_H.S._Fogler_UPDATED_(1).ipynb | 191 ----------------- 6 files changed, 653 insertions(+), 653 deletions(-) create mode 100755 sample_notebooks/AjaySatish/AjaySatish_version_backup/Sample.S._Fogler.ipynb create mode 100755 sample_notebooks/AjaySatish/AjaySatish_version_backup/Sample.S._Fogler_UPDATED.ipynb create mode 100755 sample_notebooks/AjaySatish/AjaySatish_version_backup/Sample.S._Fogler_UPDATED_(1).ipynb delete mode 100755 sample_notebooks/AjaySatish/Sample_H.S._Fogler.ipynb delete mode 100755 sample_notebooks/AjaySatish/Sample_H.S._Fogler_UPDATED.ipynb delete mode 100755 sample_notebooks/AjaySatish/Sample_H.S._Fogler_UPDATED_(1).ipynb (limited to 'sample_notebooks/AjaySatish') diff --git a/sample_notebooks/AjaySatish/AjaySatish_version_backup/Sample.S._Fogler.ipynb b/sample_notebooks/AjaySatish/AjaySatish_version_backup/Sample.S._Fogler.ipynb new file mode 100755 index 00000000..51134ef9 --- /dev/null +++ b/sample_notebooks/AjaySatish/AjaySatish_version_backup/Sample.S._Fogler.ipynb @@ -0,0 +1,231 @@ +{ + "metadata": { + "celltoolbar": "Raw Cell Format", + "name": "", + "signature": "sha256:ef32575f9668e7c75384fec9d19e3d17f6260e600de2d26c9157520e2a39253b" + }, + "nbformat": 3, + "nbformat_minor": 0, + "worksheets": [ + { + "cells": [ + { + "cell_type": "heading", + "level": 1, + "metadata": {}, + "source": [ + "ELEMENTS OF CHEMICAL ENGINEERING BY H.S. FOGLER" + ] + }, + { + "cell_type": "heading", + "level": 1, + "metadata": {}, + "source": [ + "CHAPTER NUMBER 1 : MOLE BALANCES" + ] + }, + { + "cell_type": "heading", + "level": 2, + "metadata": {}, + "source": [ + "EXAMPLE NUMBER 1.3" + ] + }, + { + "cell_type": "code", + "collapsed": false, + "input": [ + "import math\n", + "k = 0.23; #min**-1\n", + "v0 = 10;#dm**3/min\n", + "#CA = 0.1*CA0;\n", + "V = (v0/k)*math.log(1/0.1);\n", + "print \"V =\",round(V,4),\"dm**3\"" + ], + "language": "python", + "metadata": {}, + "outputs": [ + { + "output_type": "stream", + "stream": "stdout", + "text": [ + "V = 100.1124 dm**3\n" + ] + } + ], + "prompt_number": 9 + }, + { + "cell_type": "heading", + "level": 2, + "metadata": {}, + "source": [ + "CHAPTER NUMBER 2 : CONVERSION AND REACTOR SIZING" + ] + }, + { + "cell_type": "heading", + "level": 2, + "metadata": {}, + "source": [ + "EXAMPLE NUMBER 2.1" + ] + }, + { + "cell_type": "code", + "collapsed": false, + "input": [ + " \n", + "import math\n", + " \n", + "P0 = 10; #atm\n", + "yA0 = 0.5;\n", + "T0 = 422.2;#K\n", + "R = 0.082;# dm**3.atm/mol.K\n", + "v0 = 6;#dm**3/s\n", + "CA0=(yA0*P0)/(R*T0);\n", + "FA0 = CA0*v0;\n", + "print \"CA0 =\",round(CA0,4),\"mol/dm**3\"\n", + "print \"FA0 =\",round(FA0,4),\"mol/s\"" + ], + "language": "python", + "metadata": {}, + "outputs": [ + { + "output_type": "stream", + "stream": "stdout", + "text": [ + "CA0 = 0.1444 mol/dm**3\n", + "FA0 = 0.8665 mol/s\n" + ] + } + ], + "prompt_number": 10 + }, + { + "cell_type": "heading", + "level": 2, + "metadata": {}, + "source": [ + "EXAMPLE NUMBER 2.2" + ] + }, + { + "cell_type": "code", + "collapsed": false, + "input": [ + "import math\n", + "P0 = 10; #atm\n", + "yA0 = 0.5;\n", + "T0 = 422.2;#K\n", + "R = 0.082;# dm**3.atm/mol.K\n", + "v0 = 6;#dm**3/s\n", + "X = 0.8;\n", + "rA = -1/800;#1/-rA = 800#dm**3.s/mol\n", + "CA0=(yA0*P0)/(R*T0);\n", + "FA0 = CA0*v0;\n", + "V = FA0*X*(1/-rA)\n", + "print \"FA0 =\",round(FA0,4),\"mol/s\"\n", + "print \"V =\",round(V,4),\"dm**3\"\n" + ], + "language": "python", + "metadata": {}, + "outputs": [ + { + "output_type": "stream", + "stream": "stdout", + "text": [ + "FA0 = 0.8665 mol/s\n", + "V = 0.6932 dm**3\n" + ] + } + ], + "prompt_number": 11 + }, + { + "cell_type": "heading", + "level": 2, + "metadata": {}, + "source": [ + "EXAMPLE NUMBER 2.3" + ] + }, + { + "cell_type": "code", + "collapsed": false, + "input": [ + "import math\n", + " \n", + "P0 = 10; #atm\n", + "yA0 = 0.5;\n", + "T0 = 422.2;#K\n", + "R = 0.082;# dm**3.atm/mol.K\n", + "v0 = 6;#dm**3/s\n", + "X = [0,0.1,0.2,0.3,0.4,0.5,0.6,0.7,0.8];\n", + "p = [189,192,200,222,250,303,400,556,800];#1/-rA = 800#dm**3.s/mols\n", + "CA0=(yA0*P0)/(R*T0);\n", + "FA0 = CA0*v0;\n", + "#V = FA0*X*(1/-rA)\n", + "\n", + "V = FA0*np.interp(0.42,X,p)\n", + "print \"FA0 =\",FA0,\"mol/s\"\n", + "print \"V =\",V,\"dm**3\"" + ], + "language": "python", + "metadata": {}, + "outputs": [ + { + "output_type": "stream", + "stream": "stdout", + "text": [ + "FA0 = 0.866541114487 mol/s\n", + "V = 225.820614435 dm**3\n" + ] + } + ], + "prompt_number": 21 + }, + { + "cell_type": "heading", + "level": 2, + "metadata": {}, + "source": [ + "EXAMPLE NUMBER 2.4" + ] + }, + { + "cell_type": "code", + "collapsed": false, + "input": [ + "import math\n", + "FA0 = 5; # mol/s\n", + "rAat=-0.0025;\n", + "X = [0,0.1,0.2,0.3,0.4,0.5,0.6];\n", + "p = [189,192,200,222,250,303,400];#1/-rA = 800#dm**3.s/mols\n", + "\n", + "VCSTR = FA0*X[6]*(1/-rAat);\n", + "VPFR = FA0*np.interp(0.00017,X,p)\n", + "print \"VCSTR =\",VCSTR,\"dm**3\"\n", + "print \"VPFR =\",VPFR,\"dm**3\"" + ], + "language": "python", + "metadata": {}, + "outputs": [ + { + "output_type": "stream", + "stream": "stdout", + "text": [ + "VCSTR = 1200.0 dm**3\n", + "VPFR = 945.0255 dm**3\n" + ] + } + ], + "prompt_number": 37 + } + ], + "metadata": {} + } + ] +} \ No newline at end of file diff --git a/sample_notebooks/AjaySatish/AjaySatish_version_backup/Sample.S._Fogler_UPDATED.ipynb b/sample_notebooks/AjaySatish/AjaySatish_version_backup/Sample.S._Fogler_UPDATED.ipynb new file mode 100755 index 00000000..a2bda001 --- /dev/null +++ b/sample_notebooks/AjaySatish/AjaySatish_version_backup/Sample.S._Fogler_UPDATED.ipynb @@ -0,0 +1,231 @@ +{ + "metadata": { + "celltoolbar": "Raw Cell Format", + "name": "", + "signature": "sha256:37859c50b0a22beb7e2005b729edef7d0375ee40d0e34f554e83e84af89eab44" + }, + "nbformat": 3, + "nbformat_minor": 0, + "worksheets": [ + { + "cells": [ + { + "cell_type": "heading", + "level": 1, + "metadata": {}, + "source": [ + "ELEMENTS OF CHEMICAL ENGINEERING BY H.S. FOGLER" + ] + }, + { + "cell_type": "heading", + "level": 1, + "metadata": {}, + "source": [ + "CHAPTER NUMBER 1 : MOLE BALANCES" + ] + }, + { + "cell_type": "heading", + "level": 2, + "metadata": {}, + "source": [ + "EXAMPLE NUMBER 1.3 : PAGE NUMBER 15" + ] + }, + { + "cell_type": "code", + "collapsed": false, + "input": [ + "import math\n", + "k = 0.23; #min**-1\n", + "v0 = 10;#dm**3/min\n", + "#CA = 0.1*CA0;\n", + "V = (v0/k)*math.log(1/0.1);\n", + "print \"V =\",round(V,4),\"dm**3\"" + ], + "language": "python", + "metadata": {}, + "outputs": [ + { + "output_type": "stream", + "stream": "stdout", + "text": [ + "V = 100.1124 dm**3\n" + ] + } + ], + "prompt_number": 9 + }, + { + "cell_type": "heading", + "level": 1, + "metadata": {}, + "source": [ + "CHAPTER NUMBER 2 : CONVERSION AND REACTOR SIZING" + ] + }, + { + "cell_type": "heading", + "level": 2, + "metadata": {}, + "source": [ + "EXAMPLE NUMBER 2.1 : PAGE NUMBER 38" + ] + }, + { + "cell_type": "code", + "collapsed": false, + "input": [ + " \n", + "import math\n", + " \n", + "P0 = 10; #atm\n", + "yA0 = 0.5;\n", + "T0 = 422.2;#K\n", + "R = 0.082;# dm**3.atm/mol.K\n", + "v0 = 6;#dm**3/s\n", + "CA0=(yA0*P0)/(R*T0);\n", + "FA0 = CA0*v0;\n", + "print \"CA0 =\",round(CA0,4),\"mol/dm**3\"\n", + "print \"FA0 =\",round(FA0,4),\"mol/s\"" + ], + "language": "python", + "metadata": {}, + "outputs": [ + { + "output_type": "stream", + "stream": "stdout", + "text": [ + "CA0 = 0.1444 mol/dm**3\n", + "FA0 = 0.8665 mol/s\n" + ] + } + ], + "prompt_number": 10 + }, + { + "cell_type": "heading", + "level": 2, + "metadata": {}, + "source": [ + "EXAMPLE NUMBER 2.2 : PAGE NUMBER 42" + ] + }, + { + "cell_type": "code", + "collapsed": false, + "input": [ + "import math\n", + "P0 = 10; #atm\n", + "yA0 = 0.5;\n", + "T0 = 422.2;#K\n", + "R = 0.082;# dm**3.atm/mol.K\n", + "v0 = 6;#dm**3/s\n", + "X = 0.8;\n", + "rA = -1/800;#1/-rA = 800#dm**3.s/mol\n", + "CA0=(yA0*P0)/(R*T0);\n", + "FA0 = CA0*v0;\n", + "V = FA0*X*(1/-rA)\n", + "print \"FA0 =\",round(FA0,4),\"mol/s\"\n", + "print \"V =\",round(V,4),\"dm**3\"\n" + ], + "language": "python", + "metadata": {}, + "outputs": [ + { + "output_type": "stream", + "stream": "stdout", + "text": [ + "FA0 = 0.8665 mol/s\n", + "V = 0.6932 dm**3\n" + ] + } + ], + "prompt_number": 11 + }, + { + "cell_type": "heading", + "level": 2, + "metadata": {}, + "source": [ + "EXAMPLE NUMBER 2.3 : PAGE NUMBER 44" + ] + }, + { + "cell_type": "code", + "collapsed": false, + "input": [ + "import math\n", + " \n", + "P0 = 10; #atm\n", + "yA0 = 0.5;\n", + "T0 = 422.2;#K\n", + "R = 0.082;# dm**3.atm/mol.K\n", + "v0 = 6;#dm**3/s\n", + "X = [0,0.1,0.2,0.3,0.4,0.5,0.6,0.7,0.8];\n", + "p = [189,192,200,222,250,303,400,556,800];#1/-rA = 800#dm**3.s/mols\n", + "CA0=(yA0*P0)/(R*T0);\n", + "FA0 = CA0*v0;\n", + "#V = FA0*X*(1/-rA)\n", + "\n", + "V = FA0*np.interp(0.42,X,p)\n", + "print \"FA0 =\",FA0,\"mol/s\"\n", + "print \"V =\",V,\"dm**3\"" + ], + "language": "python", + "metadata": {}, + "outputs": [ + { + "output_type": "stream", + "stream": "stdout", + "text": [ + "FA0 = 0.866541114487 mol/s\n", + "V = 225.820614435 dm**3\n" + ] + } + ], + "prompt_number": 21 + }, + { + "cell_type": "heading", + "level": 2, + "metadata": {}, + "source": [ + "EXAMPLE NUMBER 2.4 : PAGE NUMBER 46" + ] + }, + { + "cell_type": "code", + "collapsed": false, + "input": [ + "import math\n", + "FA0 = 5; # mol/s\n", + "rAat=-0.0025;\n", + "X = [0,0.1,0.2,0.3,0.4,0.5,0.6];\n", + "p = [189,192,200,222,250,303,400];#1/-rA = 800#dm**3.s/mols\n", + "\n", + "VCSTR = FA0*X[6]*(1/-rAat);\n", + "VPFR = FA0*np.interp(0.00017,X,p)\n", + "print \"VCSTR =\",VCSTR,\"dm**3\"\n", + "print \"VPFR =\",VPFR,\"dm**3\"" + ], + "language": "python", + "metadata": {}, + "outputs": [ + { + "output_type": "stream", + "stream": "stdout", + "text": [ + "VCSTR = 1200.0 dm**3\n", + "VPFR = 945.0255 dm**3\n" + ] + } + ], + "prompt_number": 37 + } + ], + "metadata": {} + } + ] +} \ No newline at end of file diff --git a/sample_notebooks/AjaySatish/AjaySatish_version_backup/Sample.S._Fogler_UPDATED_(1).ipynb b/sample_notebooks/AjaySatish/AjaySatish_version_backup/Sample.S._Fogler_UPDATED_(1).ipynb new file mode 100755 index 00000000..2b950ef8 --- /dev/null +++ b/sample_notebooks/AjaySatish/AjaySatish_version_backup/Sample.S._Fogler_UPDATED_(1).ipynb @@ -0,0 +1,191 @@ +{ + "metadata": { + "celltoolbar": "Raw Cell Format", + "name": "", + "signature": "sha256:6aa7321c51ecc68ee01a5bb4aa554a936a01c87ebd6725c56b8e0edb6adbcf78" + }, + "nbformat": 3, + "nbformat_minor": 0, + "worksheets": [ + { + "cells": [ + { + "cell_type": "heading", + "level": 1, + "metadata": {}, + "source": [ + "ELEMENTS OF CHEMICAL ENGINEERING BY H.S. FOGLER" + ] + }, + { + "cell_type": "heading", + "level": 1, + "metadata": {}, + "source": [ + "CHAPTER NUMBER 2 : CONVERSION AND REACTOR SIZING" + ] + }, + { + "cell_type": "heading", + "level": 2, + "metadata": {}, + "source": [ + "EXAMPLE NUMBER 2.1 : PAGE NUMBER 38" + ] + }, + { + "cell_type": "code", + "collapsed": false, + "input": [ + " \n", + "import math\n", + " \n", + "P0 = 10; #atm\n", + "yA0 = 0.5;\n", + "T0 = 422.2;#K\n", + "R = 0.082;# dm**3.atm/mol.K\n", + "v0 = 6;#dm**3/s\n", + "CA0=(yA0*P0)/(R*T0);\n", + "FA0 = CA0*v0;\n", + "print \"CA0 =\",round(CA0,4),\"mol/dm**3\"\n", + "print \"FA0 =\",round(FA0,4),\"mol/s\"" + ], + "language": "python", + "metadata": {}, + "outputs": [ + { + "output_type": "stream", + "stream": "stdout", + "text": [ + "CA0 = 0.1444 mol/dm**3\n", + "FA0 = 0.8665 mol/s\n" + ] + } + ], + "prompt_number": 10 + }, + { + "cell_type": "heading", + "level": 2, + "metadata": {}, + "source": [ + "EXAMPLE NUMBER 2.2 : PAGE NUMBER 42" + ] + }, + { + "cell_type": "code", + "collapsed": false, + "input": [ + "import math\n", + "P0 = 10; #atm\n", + "yA0 = 0.5;\n", + "T0 = 422.2;#K\n", + "R = 0.082;# dm**3.atm/mol.K\n", + "v0 = 6;#dm**3/s\n", + "X = 0.8;\n", + "rA = -1/800;#1/-rA = 800#dm**3.s/mol\n", + "CA0=(yA0*P0)/(R*T0);\n", + "FA0 = CA0*v0;\n", + "V = FA0*X*(1/-rA)\n", + "print \"FA0 =\",round(FA0,4),\"mol/s\"\n", + "print \"V =\",round(V,4),\"dm**3\"\n" + ], + "language": "python", + "metadata": {}, + "outputs": [ + { + "output_type": "stream", + "stream": "stdout", + "text": [ + "FA0 = 0.8665 mol/s\n", + "V = 0.6932 dm**3\n" + ] + } + ], + "prompt_number": 11 + }, + { + "cell_type": "heading", + "level": 2, + "metadata": {}, + "source": [ + "EXAMPLE NUMBER 2.3 : PAGE NUMBER 44" + ] + }, + { + "cell_type": "code", + "collapsed": false, + "input": [ + "import math\n", + " \n", + "P0 = 10; #atm\n", + "yA0 = 0.5;\n", + "T0 = 422.2;#K\n", + "R = 0.082;# dm**3.atm/mol.K\n", + "v0 = 6;#dm**3/s\n", + "X = [0,0.1,0.2,0.3,0.4,0.5,0.6,0.7,0.8];\n", + "p = [189,192,200,222,250,303,400,556,800];#1/-rA = 800#dm**3.s/mols\n", + "CA0=(yA0*P0)/(R*T0);\n", + "FA0 = CA0*v0;\n", + "#V = FA0*X*(1/-rA)\n", + "\n", + "V = FA0*np.interp(0.42,X,p)\n", + "print \"FA0 =\",FA0,\"mol/s\"\n", + "print \"V =\",V,\"dm**3\"" + ], + "language": "python", + "metadata": {}, + "outputs": [ + { + "output_type": "stream", + "stream": "stdout", + "text": [ + "FA0 = 0.866541114487 mol/s\n", + "V = 225.820614435 dm**3\n" + ] + } + ], + "prompt_number": 21 + }, + { + "cell_type": "heading", + "level": 2, + "metadata": {}, + "source": [ + "EXAMPLE NUMBER 2.4 : PAGE NUMBER 46" + ] + }, + { + "cell_type": "code", + "collapsed": false, + "input": [ + "import math\n", + "FA0 = 5; # mol/s\n", + "rAat=-0.0025;\n", + "X = [0,0.1,0.2,0.3,0.4,0.5,0.6];\n", + "p = [189,192,200,222,250,303,400];#1/-rA = 800#dm**3.s/mols\n", + "\n", + "VCSTR = FA0*X[6]*(1/-rAat);\n", + "VPFR = FA0*np.interp(0.00017,X,p)\n", + "print \"VCSTR =\",VCSTR,\"dm**3\"\n", + "print \"VPFR =\",VPFR,\"dm**3\"" + ], + "language": "python", + "metadata": {}, + "outputs": [ + { + "output_type": "stream", + "stream": "stdout", + "text": [ + "VCSTR = 1200.0 dm**3\n", + "VPFR = 945.0255 dm**3\n" + ] + } + ], + "prompt_number": 37 + } + ], + "metadata": {} + } + ] +} \ No newline at end of file diff --git a/sample_notebooks/AjaySatish/Sample_H.S._Fogler.ipynb b/sample_notebooks/AjaySatish/Sample_H.S._Fogler.ipynb deleted file mode 100755 index 51134ef9..00000000 --- a/sample_notebooks/AjaySatish/Sample_H.S._Fogler.ipynb +++ /dev/null @@ -1,231 +0,0 @@ -{ - "metadata": { - "celltoolbar": "Raw Cell Format", - "name": "", - "signature": "sha256:ef32575f9668e7c75384fec9d19e3d17f6260e600de2d26c9157520e2a39253b" - }, - "nbformat": 3, - "nbformat_minor": 0, - "worksheets": [ - { - "cells": [ - { - "cell_type": "heading", - "level": 1, - "metadata": {}, - "source": [ - "ELEMENTS OF CHEMICAL ENGINEERING BY H.S. FOGLER" - ] - }, - { - "cell_type": "heading", - "level": 1, - "metadata": {}, - "source": [ - "CHAPTER NUMBER 1 : MOLE BALANCES" - ] - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "EXAMPLE NUMBER 1.3" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "import math\n", - "k = 0.23; #min**-1\n", - "v0 = 10;#dm**3/min\n", - "#CA = 0.1*CA0;\n", - "V = (v0/k)*math.log(1/0.1);\n", - "print \"V =\",round(V,4),\"dm**3\"" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "V = 100.1124 dm**3\n" - ] - } - ], - "prompt_number": 9 - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "CHAPTER NUMBER 2 : CONVERSION AND REACTOR SIZING" - ] - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "EXAMPLE NUMBER 2.1" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - " \n", - "import math\n", - " \n", - "P0 = 10; #atm\n", - "yA0 = 0.5;\n", - "T0 = 422.2;#K\n", - "R = 0.082;# dm**3.atm/mol.K\n", - "v0 = 6;#dm**3/s\n", - "CA0=(yA0*P0)/(R*T0);\n", - "FA0 = CA0*v0;\n", - "print \"CA0 =\",round(CA0,4),\"mol/dm**3\"\n", - "print \"FA0 =\",round(FA0,4),\"mol/s\"" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "CA0 = 0.1444 mol/dm**3\n", - "FA0 = 0.8665 mol/s\n" - ] - } - ], - "prompt_number": 10 - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "EXAMPLE NUMBER 2.2" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "import math\n", - "P0 = 10; #atm\n", - "yA0 = 0.5;\n", - "T0 = 422.2;#K\n", - "R = 0.082;# dm**3.atm/mol.K\n", - "v0 = 6;#dm**3/s\n", - "X = 0.8;\n", - "rA = -1/800;#1/-rA = 800#dm**3.s/mol\n", - "CA0=(yA0*P0)/(R*T0);\n", - "FA0 = CA0*v0;\n", - "V = FA0*X*(1/-rA)\n", - "print \"FA0 =\",round(FA0,4),\"mol/s\"\n", - "print \"V =\",round(V,4),\"dm**3\"\n" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "FA0 = 0.8665 mol/s\n", - "V = 0.6932 dm**3\n" - ] - } - ], - "prompt_number": 11 - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "EXAMPLE NUMBER 2.3" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "import math\n", - " \n", - "P0 = 10; #atm\n", - "yA0 = 0.5;\n", - "T0 = 422.2;#K\n", - "R = 0.082;# dm**3.atm/mol.K\n", - "v0 = 6;#dm**3/s\n", - "X = [0,0.1,0.2,0.3,0.4,0.5,0.6,0.7,0.8];\n", - "p = [189,192,200,222,250,303,400,556,800];#1/-rA = 800#dm**3.s/mols\n", - "CA0=(yA0*P0)/(R*T0);\n", - "FA0 = CA0*v0;\n", - "#V = FA0*X*(1/-rA)\n", - "\n", - "V = FA0*np.interp(0.42,X,p)\n", - "print \"FA0 =\",FA0,\"mol/s\"\n", - "print \"V =\",V,\"dm**3\"" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "FA0 = 0.866541114487 mol/s\n", - "V = 225.820614435 dm**3\n" - ] - } - ], - "prompt_number": 21 - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "EXAMPLE NUMBER 2.4" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "import math\n", - "FA0 = 5; # mol/s\n", - "rAat=-0.0025;\n", - "X = [0,0.1,0.2,0.3,0.4,0.5,0.6];\n", - "p = [189,192,200,222,250,303,400];#1/-rA = 800#dm**3.s/mols\n", - "\n", - "VCSTR = FA0*X[6]*(1/-rAat);\n", - "VPFR = FA0*np.interp(0.00017,X,p)\n", - "print \"VCSTR =\",VCSTR,\"dm**3\"\n", - "print \"VPFR =\",VPFR,\"dm**3\"" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "VCSTR = 1200.0 dm**3\n", - "VPFR = 945.0255 dm**3\n" - ] - } - ], - "prompt_number": 37 - } - ], - "metadata": {} - } - ] -} \ No newline at end of file diff --git a/sample_notebooks/AjaySatish/Sample_H.S._Fogler_UPDATED.ipynb b/sample_notebooks/AjaySatish/Sample_H.S._Fogler_UPDATED.ipynb deleted file mode 100755 index a2bda001..00000000 --- a/sample_notebooks/AjaySatish/Sample_H.S._Fogler_UPDATED.ipynb +++ /dev/null @@ -1,231 +0,0 @@ -{ - "metadata": { - "celltoolbar": "Raw Cell Format", - "name": "", - "signature": "sha256:37859c50b0a22beb7e2005b729edef7d0375ee40d0e34f554e83e84af89eab44" - }, - "nbformat": 3, - "nbformat_minor": 0, - "worksheets": [ - { - "cells": [ - { - "cell_type": "heading", - "level": 1, - "metadata": {}, - "source": [ - "ELEMENTS OF CHEMICAL ENGINEERING BY H.S. FOGLER" - ] - }, - { - "cell_type": "heading", - "level": 1, - "metadata": {}, - "source": [ - "CHAPTER NUMBER 1 : MOLE BALANCES" - ] - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "EXAMPLE NUMBER 1.3 : PAGE NUMBER 15" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "import math\n", - "k = 0.23; #min**-1\n", - "v0 = 10;#dm**3/min\n", - "#CA = 0.1*CA0;\n", - "V = (v0/k)*math.log(1/0.1);\n", - "print \"V =\",round(V,4),\"dm**3\"" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "V = 100.1124 dm**3\n" - ] - } - ], - "prompt_number": 9 - }, - { - "cell_type": "heading", - "level": 1, - "metadata": {}, - "source": [ - "CHAPTER NUMBER 2 : CONVERSION AND REACTOR SIZING" - ] - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "EXAMPLE NUMBER 2.1 : PAGE NUMBER 38" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - " \n", - "import math\n", - " \n", - "P0 = 10; #atm\n", - "yA0 = 0.5;\n", - "T0 = 422.2;#K\n", - "R = 0.082;# dm**3.atm/mol.K\n", - "v0 = 6;#dm**3/s\n", - "CA0=(yA0*P0)/(R*T0);\n", - "FA0 = CA0*v0;\n", - "print \"CA0 =\",round(CA0,4),\"mol/dm**3\"\n", - "print \"FA0 =\",round(FA0,4),\"mol/s\"" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "CA0 = 0.1444 mol/dm**3\n", - "FA0 = 0.8665 mol/s\n" - ] - } - ], - "prompt_number": 10 - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "EXAMPLE NUMBER 2.2 : PAGE NUMBER 42" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "import math\n", - "P0 = 10; #atm\n", - "yA0 = 0.5;\n", - "T0 = 422.2;#K\n", - "R = 0.082;# dm**3.atm/mol.K\n", - "v0 = 6;#dm**3/s\n", - "X = 0.8;\n", - "rA = -1/800;#1/-rA = 800#dm**3.s/mol\n", - "CA0=(yA0*P0)/(R*T0);\n", - "FA0 = CA0*v0;\n", - "V = FA0*X*(1/-rA)\n", - "print \"FA0 =\",round(FA0,4),\"mol/s\"\n", - "print \"V =\",round(V,4),\"dm**3\"\n" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "FA0 = 0.8665 mol/s\n", - "V = 0.6932 dm**3\n" - ] - } - ], - "prompt_number": 11 - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "EXAMPLE NUMBER 2.3 : PAGE NUMBER 44" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "import math\n", - " \n", - "P0 = 10; #atm\n", - "yA0 = 0.5;\n", - "T0 = 422.2;#K\n", - "R = 0.082;# dm**3.atm/mol.K\n", - "v0 = 6;#dm**3/s\n", - "X = [0,0.1,0.2,0.3,0.4,0.5,0.6,0.7,0.8];\n", - "p = [189,192,200,222,250,303,400,556,800];#1/-rA = 800#dm**3.s/mols\n", - "CA0=(yA0*P0)/(R*T0);\n", - "FA0 = CA0*v0;\n", - "#V = FA0*X*(1/-rA)\n", - "\n", - "V = FA0*np.interp(0.42,X,p)\n", - "print \"FA0 =\",FA0,\"mol/s\"\n", - "print \"V =\",V,\"dm**3\"" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "FA0 = 0.866541114487 mol/s\n", - "V = 225.820614435 dm**3\n" - ] - } - ], - "prompt_number": 21 - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "EXAMPLE NUMBER 2.4 : PAGE NUMBER 46" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "import math\n", - "FA0 = 5; # mol/s\n", - "rAat=-0.0025;\n", - "X = [0,0.1,0.2,0.3,0.4,0.5,0.6];\n", - "p = [189,192,200,222,250,303,400];#1/-rA = 800#dm**3.s/mols\n", - "\n", - "VCSTR = FA0*X[6]*(1/-rAat);\n", - "VPFR = FA0*np.interp(0.00017,X,p)\n", - "print \"VCSTR =\",VCSTR,\"dm**3\"\n", - "print \"VPFR =\",VPFR,\"dm**3\"" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "VCSTR = 1200.0 dm**3\n", - "VPFR = 945.0255 dm**3\n" - ] - } - ], - "prompt_number": 37 - } - ], - "metadata": {} - } - ] -} \ No newline at end of file diff --git a/sample_notebooks/AjaySatish/Sample_H.S._Fogler_UPDATED_(1).ipynb b/sample_notebooks/AjaySatish/Sample_H.S._Fogler_UPDATED_(1).ipynb deleted file mode 100755 index 2b950ef8..00000000 --- a/sample_notebooks/AjaySatish/Sample_H.S._Fogler_UPDATED_(1).ipynb +++ /dev/null @@ -1,191 +0,0 @@ -{ - "metadata": { - "celltoolbar": "Raw Cell Format", - "name": "", - "signature": "sha256:6aa7321c51ecc68ee01a5bb4aa554a936a01c87ebd6725c56b8e0edb6adbcf78" - }, - "nbformat": 3, - "nbformat_minor": 0, - "worksheets": [ - { - "cells": [ - { - "cell_type": "heading", - "level": 1, - "metadata": {}, - "source": [ - "ELEMENTS OF CHEMICAL ENGINEERING BY H.S. FOGLER" - ] - }, - { - "cell_type": "heading", - "level": 1, - "metadata": {}, - "source": [ - "CHAPTER NUMBER 2 : CONVERSION AND REACTOR SIZING" - ] - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "EXAMPLE NUMBER 2.1 : PAGE NUMBER 38" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - " \n", - "import math\n", - " \n", - "P0 = 10; #atm\n", - "yA0 = 0.5;\n", - "T0 = 422.2;#K\n", - "R = 0.082;# dm**3.atm/mol.K\n", - "v0 = 6;#dm**3/s\n", - "CA0=(yA0*P0)/(R*T0);\n", - "FA0 = CA0*v0;\n", - "print \"CA0 =\",round(CA0,4),\"mol/dm**3\"\n", - "print \"FA0 =\",round(FA0,4),\"mol/s\"" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "CA0 = 0.1444 mol/dm**3\n", - "FA0 = 0.8665 mol/s\n" - ] - } - ], - "prompt_number": 10 - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "EXAMPLE NUMBER 2.2 : PAGE NUMBER 42" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "import math\n", - "P0 = 10; #atm\n", - "yA0 = 0.5;\n", - "T0 = 422.2;#K\n", - "R = 0.082;# dm**3.atm/mol.K\n", - "v0 = 6;#dm**3/s\n", - "X = 0.8;\n", - "rA = -1/800;#1/-rA = 800#dm**3.s/mol\n", - "CA0=(yA0*P0)/(R*T0);\n", - "FA0 = CA0*v0;\n", - "V = FA0*X*(1/-rA)\n", - "print \"FA0 =\",round(FA0,4),\"mol/s\"\n", - "print \"V =\",round(V,4),\"dm**3\"\n" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "FA0 = 0.8665 mol/s\n", - "V = 0.6932 dm**3\n" - ] - } - ], - "prompt_number": 11 - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "EXAMPLE NUMBER 2.3 : PAGE NUMBER 44" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "import math\n", - " \n", - "P0 = 10; #atm\n", - "yA0 = 0.5;\n", - "T0 = 422.2;#K\n", - "R = 0.082;# dm**3.atm/mol.K\n", - "v0 = 6;#dm**3/s\n", - "X = [0,0.1,0.2,0.3,0.4,0.5,0.6,0.7,0.8];\n", - "p = [189,192,200,222,250,303,400,556,800];#1/-rA = 800#dm**3.s/mols\n", - "CA0=(yA0*P0)/(R*T0);\n", - "FA0 = CA0*v0;\n", - "#V = FA0*X*(1/-rA)\n", - "\n", - "V = FA0*np.interp(0.42,X,p)\n", - "print \"FA0 =\",FA0,\"mol/s\"\n", - "print \"V =\",V,\"dm**3\"" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "FA0 = 0.866541114487 mol/s\n", - "V = 225.820614435 dm**3\n" - ] - } - ], - "prompt_number": 21 - }, - { - "cell_type": "heading", - "level": 2, - "metadata": {}, - "source": [ - "EXAMPLE NUMBER 2.4 : PAGE NUMBER 46" - ] - }, - { - "cell_type": "code", - "collapsed": false, - "input": [ - "import math\n", - "FA0 = 5; # mol/s\n", - "rAat=-0.0025;\n", - "X = [0,0.1,0.2,0.3,0.4,0.5,0.6];\n", - "p = [189,192,200,222,250,303,400];#1/-rA = 800#dm**3.s/mols\n", - "\n", - "VCSTR = FA0*X[6]*(1/-rAat);\n", - "VPFR = FA0*np.interp(0.00017,X,p)\n", - "print \"VCSTR =\",VCSTR,\"dm**3\"\n", - "print \"VPFR =\",VPFR,\"dm**3\"" - ], - "language": "python", - "metadata": {}, - "outputs": [ - { - "output_type": "stream", - "stream": "stdout", - "text": [ - "VCSTR = 1200.0 dm**3\n", - "VPFR = 945.0255 dm**3\n" - ] - } - ], - "prompt_number": 37 - } - ], - "metadata": {} - } - ] -} \ No newline at end of file -- cgit