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author | Hardik Ghaghada | 2014-06-20 15:52:25 +0530 |
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committer | Hardik Ghaghada | 2014-06-20 15:52:25 +0530 |
commit | e1e59ca3a50d9f93e8b7bc0693b8081d5db77771 (patch) | |
tree | f54eab21dd3d725d64a495fcd47c00d37abed004 /Basic_Principles_And_Calculations_In_Chemical_Engineering/ch25.ipynb | |
parent | a78126bbe4443e9526a64df9d8245c4af8843044 (diff) | |
parent | 83c1bfceb1b681b4bb7253b47491be2d8b2014a1 (diff) | |
download | Python-Textbook-Companions-e1e59ca3a50d9f93e8b7bc0693b8081d5db77771.tar.gz Python-Textbook-Companions-e1e59ca3a50d9f93e8b7bc0693b8081d5db77771.tar.bz2 Python-Textbook-Companions-e1e59ca3a50d9f93e8b7bc0693b8081d5db77771.zip |
Merge pull request #1 from debashisdeb/master
removing problem statements from all the chapters to avoid copyright violations
Diffstat (limited to 'Basic_Principles_And_Calculations_In_Chemical_Engineering/ch25.ipynb')
-rw-r--r-- | Basic_Principles_And_Calculations_In_Chemical_Engineering/ch25.ipynb | 20 |
1 files changed, 5 insertions, 15 deletions
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", |