diff options
Diffstat (limited to 'Chemical_Engineering_Thermodynamics/ch5_2.ipynb')
| -rw-r--r-- | Chemical_Engineering_Thermodynamics/ch5_2.ipynb | 36 |
1 files changed, 11 insertions, 25 deletions
diff --git a/Chemical_Engineering_Thermodynamics/ch5_2.ipynb b/Chemical_Engineering_Thermodynamics/ch5_2.ipynb index db8558ce..82489a66 100644 --- a/Chemical_Engineering_Thermodynamics/ch5_2.ipynb +++ b/Chemical_Engineering_Thermodynamics/ch5_2.ipynb @@ -1,6 +1,7 @@ { "metadata": { - "name": "" + "name": "", + "signature": "sha256:beb354ab1f11a4413c580f54f984be6db9b7dd2c39bed82bc1f4874533d75759" }, "nbformat": 3, "nbformat_minor": 0, @@ -27,8 +28,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determination of fraction of the availability loss\n", - "\n", + " \n", "import math\n", "\n", "# Variables\n", @@ -76,8 +76,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determination of availability change and irreversibility\n", - "\n", + " \n", "# Variables\n", "T_1 = 300.;\t\t\t#[K] - Initial temperature.\n", "P_1 = 100.;\t\t\t#[kPa] - Initial pressure.\n", @@ -143,8 +142,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determination of availability change and irreversibility\n", - "\n", + " \n", "import math\n", "# Variables\n", "P_1 = 15.;\t\t\t#[bar] - Initial pressure\n", @@ -296,9 +294,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determination of useful work and irreversibility\n", - "\n", - "# Variables\n", + " \n", "T_1 = 150+273.15;\t\t\t#[K] - Initial temperature.\n", "m = 4.6;\t\t\t#[kg] - mass of water\n", "P_1 = 1;\t\t\t#[MPa] - Initial pressure\n", @@ -380,9 +376,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determination of reversible work and irreversibility\n", - "\n", - "# Variables\n", + " \n", "T_1 = 700+273.15;\t\t\t#[K] - Initial temperature.\n", "P_1 = 12;\t\t\t#[MPa] - Initial pressure\n", "P_2 = 0.6;\t\t\t#[MPa] - Final pressure\n", @@ -480,9 +474,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determination of maximum obtainable work and efficiency\n", - "\n", - "# Variables\n", + " \n", "P_1 = 8.;\t\t\t#[bar] - Initial pressure\n", "T_1 = 93. + 273.15;\t\t\t#[C] - Initial temperature\n", "V_1 = 100.;\t\t\t#[m/s] - Initial velocity\n", @@ -545,9 +537,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determination of entropy generation rate and irreversibility\n", - "\n", - "# Variables\n", + " \n", "m_cold_water = 60;\t\t\t#[kg/s] - mass flow rate of cold water\n", "P_1 = 50;\t\t\t#[kPa]\n", "T_2 = 250;\t\t\t#[C]\n", @@ -617,9 +607,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Calculation of exit temperature entropy and irreversibility rate\n", - "\n", - "# Variables\n", + " \n", "m_water = 10000.;\t\t\t#[kg/h] - Mass flow rate of cold water\n", "m_water = m_water/3600;\t\t\t#[kg/s]\n", "T_1_water = 30. + 273.15;\t\t\t#[K] - Cold water entering temperature\n", @@ -686,9 +674,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "# Determinatio of exit temperature availability change and irreversibility\n", - "\n", - "# Variables\n", + " \n", "T_1_hotgas = 800.;\t\t\t#[K]\n", "P_1_hotgas = 1.;\t\t\t#[bar]\n", "T_2_hotgas = 700.;\t\t\t#[K]\n", |