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-rw-r--r--Chemical_Engineering_Thermodynamics/ch11_1.ipynb18
1 files changed, 7 insertions, 11 deletions
diff --git a/Chemical_Engineering_Thermodynamics/ch11_1.ipynb b/Chemical_Engineering_Thermodynamics/ch11_1.ipynb
index fdf3f695..79f48f9c 100644
--- a/Chemical_Engineering_Thermodynamics/ch11_1.ipynb
+++ b/Chemical_Engineering_Thermodynamics/ch11_1.ipynb
@@ -1,6 +1,7 @@
{
"metadata": {
- "name": ""
+ "name": "",
+ "signature": "sha256:ea5fa2ce45062851dc4892fcc5b621c33d72fa0443d476b1ef4133dade9e39b0"
},
"nbformat": 3,
"nbformat_minor": 0,
@@ -27,8 +28,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# Determination of volumes of ethanol and water\n",
- "\n",
+ " \n",
"import math\n",
"\n",
"# Variables\n",
@@ -89,8 +89,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# Developing an expression\n",
- "\n",
+ " \n",
"# Variables\n",
"T = 25+273.15;\t\t\t#[K] - Temperature\n",
"P = 1;\t\t\t#[atm]\n",
@@ -144,8 +143,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# Calculation of enthalpies\n",
- "\n",
+ " \n",
"# Variables\n",
"#H = a*x_1 + b*x_2 +c*x_1*x_2\n",
"\n",
@@ -233,8 +231,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# Calculation of minimum work required\n",
- "\n",
+ " \n",
"# Variables\n",
"n = 1*10**(3);\t\t\t#[mol] - No of moles\n",
"P = 0.1;\t\t\t#[MPa] - Pressure of the surrounding\n",
@@ -289,8 +286,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# Calculation of fugacity 0f the mixture\n",
- "\n",
+ " \n",
"# Variables\n",
"x_A = 0.20;\t\t\t# Mole fraction of A\n",
"x_B = 0.35;\t\t\t# Mole fraction of B\n",