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-rw-r--r--Chemical_Engineering_Thermodynamics/ch18_1.ipynb22
1 files changed, 9 insertions, 13 deletions
diff --git a/Chemical_Engineering_Thermodynamics/ch18_1.ipynb b/Chemical_Engineering_Thermodynamics/ch18_1.ipynb
index 730764b8..46865b0c 100644
--- a/Chemical_Engineering_Thermodynamics/ch18_1.ipynb
+++ b/Chemical_Engineering_Thermodynamics/ch18_1.ipynb
@@ -1,6 +1,7 @@
{
"metadata": {
- "name": ""
+ "name": "",
+ "signature": "sha256:32121f42f5b148741ef15da1993d191234c228c3ab7dcf05f69114fbe323a883"
},
"nbformat": 3,
"nbformat_minor": 0,
@@ -27,8 +28,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# Calculation of heat transfer\n",
- "\n",
+ " \n",
"\n",
"import math \n",
"from scipy.integrate import quad \n",
@@ -124,7 +124,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# Calculation of adiabatic flame temperature\n",
+ " \n",
"\n",
"from scipy.optimize import fsolve \n",
"\n",
@@ -205,8 +205,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# Calculation of mole fraction and average heat capacity\n",
- "\n",
+ " \n",
"# Variables\n",
"T_1 = 298.15;\t\t\t#[K] - Smath.tan(math.radiansard reaction temperature\n",
"\n",
@@ -258,8 +257,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# Determination of adiabatic flame temperature\n",
- "\n",
+ " \n",
"from scipy.optimize import fsolve \n",
"\n",
"\n",
@@ -348,8 +346,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# Calculation of conversion\n",
- "\n",
+ " \n",
"# Variables\n",
"\t\t\t# N2 + 3H2 - 2NH3\n",
"T_1 = 700;\t\t\t#[K] - Reaction temperature\n",
@@ -406,8 +403,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# Calculation of maximum pressure\n",
- "\n",
+ " \n",
"from scipy.optimize import fsolve \n",
"import math \n",
"from scipy.integrate import quad \n",
@@ -497,7 +493,7 @@
"input": [
"from scipy.optimize import fsolve\n",
"import math\n",
- "# Calculation of number of moles\n",
+ " \n",
"\n",
"# Variables\n",
"T_1 = 400 + 273.15;\t\t\t#[K]\n",