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-rw-r--r--Problems_In_Fluid_Flow/ch1.ipynb49
-rw-r--r--Problems_In_Fluid_Flow/ch10.ipynb32
-rw-r--r--Problems_In_Fluid_Flow/ch11.ipynb40
-rw-r--r--Problems_In_Fluid_Flow/ch12.ipynb16
-rw-r--r--Problems_In_Fluid_Flow/ch13.ipynb25
-rw-r--r--Problems_In_Fluid_Flow/ch2.ipynb39
-rw-r--r--Problems_In_Fluid_Flow/ch3.ipynb41
-rw-r--r--Problems_In_Fluid_Flow/ch4.ipynb42
-rw-r--r--Problems_In_Fluid_Flow/ch5.ipynb78
-rw-r--r--Problems_In_Fluid_Flow/ch6.ipynb34
-rw-r--r--Problems_In_Fluid_Flow/ch7.ipynb13
-rw-r--r--Problems_In_Fluid_Flow/ch8.ipynb39
-rw-r--r--Problems_In_Fluid_Flow/ch9.ipynb28
13 files changed, 98 insertions, 378 deletions
diff --git a/Problems_In_Fluid_Flow/ch1.ipynb b/Problems_In_Fluid_Flow/ch1.ipynb
index 060862e5..468c5738 100644
--- a/Problems_In_Fluid_Flow/ch1.ipynb
+++ b/Problems_In_Fluid_Flow/ch1.ipynb
@@ -1,6 +1,7 @@
{
"metadata": {
- "name": ""
+ "name": "",
+ "signature": "sha256:0059190c3ee26fe93a1d293531a49cd3a6e92d5339c0638feafb8d9d1d250c2e"
},
"nbformat": 3,
"nbformat_minor": 0,
@@ -28,11 +29,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find whether\n",
- "the system is in turbulent motion \n",
- "the system is in laminar motion \n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -93,13 +90,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "The Stanton-Pannel friction factor per unit of length\n",
- "shear stress exerted by liquid\n",
- "Total shear force exerted \n",
- "viscosity of liquid \n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -155,7 +146,6 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find the difference between the rise levels of manometer\n",
"\n",
"import math \n",
"\n",
@@ -203,7 +193,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find The volume of pure material\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -243,12 +233,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "The percent value of d for which where pitot tube is kept show average velocity in streamline flow\n",
- "The percent value of d for which where pitot tube is kept show average velocity in turbulent flow \n",
- "The error shown by pitot tube at new position \n",
- "'''\n",
+ "\n",
"import math \n",
"\n",
"\n",
@@ -302,13 +287,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "The Power required to pump acid \n",
- "The gauge pressure at pump outlet \n",
- "The increase in power required to transfer\n",
- "The gauge pressure at pump outlet\n",
- "'''\n",
+ "\n",
"\n",
"# Initialization of Variable\n",
"rhon = 1068. #density of nitric acid\n",
@@ -382,11 +361,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "power required to drive pump \n",
- "The gauge pressure in (kPa)\n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -452,11 +427,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "Volumetric flow rate initial\n",
- "Volumetric flow rate final\n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -520,7 +491,6 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find Time required to water level to fall in the tank \n",
"\n",
"import math \n",
"from numpy import linspace\n",
@@ -580,7 +550,6 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find d\n",
"\n",
"import math \n",
"\n",
diff --git a/Problems_In_Fluid_Flow/ch10.ipynb b/Problems_In_Fluid_Flow/ch10.ipynb
index 6c990a70..b9f62b91 100644
--- a/Problems_In_Fluid_Flow/ch10.ipynb
+++ b/Problems_In_Fluid_Flow/ch10.ipynb
@@ -1,6 +1,7 @@
{
"metadata": {
- "name": ""
+ "name": "",
+ "signature": "sha256:88dad4167b8ab13af93e66ad11725020c7f1ec6496fdf0f78d38810f6f3baf41"
},
"nbformat": 3,
"nbformat_minor": 0,
@@ -27,7 +28,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# Draw Concentration vs Settling veocity\n",
+ "\n",
"\n",
"%pylab inline\n",
"import math \n",
@@ -107,11 +108,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "the area for each settling velocity\n",
- "Volumetric flow rate of clarified water\n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"from numpy import linspace\n",
@@ -184,13 +181,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "The fraction of heavy ore remained\n",
- "The percentage of heavy ore left \n",
- "the fraction of light ore in overhead product\n",
- "The minimum density required to seperate 2 ores\n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"from numpy import linspace\n",
@@ -280,7 +271,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find the density of suspension\n",
+ "\n",
"\n",
"import math \n",
"from numpy import true_divide\n",
@@ -338,7 +329,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# Draw undersize vs Particle Size(m)\n",
+ "\n",
"\n",
"\n",
"import math \n",
@@ -414,7 +405,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find mass and diameter\n",
+ "\n",
"\n",
"import math \n",
"from matplotlib.pyplot import *\n",
@@ -495,12 +486,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "fraction of particles separated \n",
- "total fraction of particles separated\n",
- "fraction of particles separated \n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"\n",
diff --git a/Problems_In_Fluid_Flow/ch11.ipynb b/Problems_In_Fluid_Flow/ch11.ipynb
index c36db144..a2484ed7 100644
--- a/Problems_In_Fluid_Flow/ch11.ipynb
+++ b/Problems_In_Fluid_Flow/ch11.ipynb
@@ -1,6 +1,7 @@
{
"metadata": {
- "name": ""
+ "name": "",
+ "signature": "sha256:c23ae85b629821355f70fc5abaa38e7f6336abdb19ba09fa0e8e1a4bdcd9679f"
},
"nbformat": 3,
"nbformat_minor": 0,
@@ -27,11 +28,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "Bubbling fluidisation \n",
- "fluidisation \n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -93,13 +90,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "The superficial linear flow rate\n",
- "Terminal Settling Velocity\n",
- "Stoke law assumption\n",
- "Pressure drop across fluidised bed \n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -157,11 +148,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "the linear air flow rate\n",
- "speed required for smallest particle\n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"from numpy import *\n",
@@ -232,12 +219,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "the diameter of vessel\n",
- "depth of bed \n",
- "depth of fluidised bed under operating condition\n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"from numpy import *\n",
@@ -312,7 +294,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find power supplies to the blower\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -368,11 +350,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "minimum fluidising velocity\n",
- "fluidising velocity\n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -424,7 +402,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find ratio of terminal velocity\n",
+ "\n",
"\n",
"import math \n",
"\n",
diff --git a/Problems_In_Fluid_Flow/ch12.ipynb b/Problems_In_Fluid_Flow/ch12.ipynb
index c84580f4..7b9dbb44 100644
--- a/Problems_In_Fluid_Flow/ch12.ipynb
+++ b/Problems_In_Fluid_Flow/ch12.ipynb
@@ -1,6 +1,7 @@
{
"metadata": {
- "name": ""
+ "name": "",
+ "signature": "sha256:8f1680a01385ff5949f5cb398f429f5e497854e1c9f1b526eeecdccb5f6a2e6a"
},
"nbformat": 3,
"nbformat_minor": 0,
@@ -29,7 +30,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find actual linear flow rate through duct\n",
+ "\n",
"\n",
"import math \n",
"from numpy import *\n",
@@ -83,7 +84,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find maximum carrying capacity of polythene particles\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -143,7 +144,6 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find Pressure value in kN/m**2\n",
"\n",
"import math \n",
"\n",
@@ -212,7 +212,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find The Pressure value in kN/m**2\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -280,11 +280,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "The maximum pressure drop\n",
- "The minimum pressure drop\n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"\n",
diff --git a/Problems_In_Fluid_Flow/ch13.ipynb b/Problems_In_Fluid_Flow/ch13.ipynb
index 4422df84..3eb84b32 100644
--- a/Problems_In_Fluid_Flow/ch13.ipynb
+++ b/Problems_In_Fluid_Flow/ch13.ipynb
@@ -1,6 +1,7 @@
{
"metadata": {
- "name": ""
+ "name": "",
+ "signature": "sha256:8de14a272a9bc06516758c82d47f7c6c131e878e1053a9679880c251e49e360a"
},
"nbformat": 3,
"nbformat_minor": 0,
@@ -27,11 +28,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "ratio of cetrifugal force & gravitational force\n",
- "equivalent to gravity settling tank of crossectional area\n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -81,12 +78,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "The maximum safe speed allowed in rpm\n",
- "the power in N/m**2\n",
- "pressure gradient in radial direction \n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -150,7 +142,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find minimum diameter in organic pigment\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -193,7 +185,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find maximum volumetric flow rate\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -240,7 +232,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find distance of xis of rotation of cream milk interface\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -281,7 +273,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find volumetric flow rate\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -326,7 +318,6 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find overall efficiency of cyclone separator\n",
"\n",
"import math \n",
"from numpy import linspace\n",
diff --git a/Problems_In_Fluid_Flow/ch2.ipynb b/Problems_In_Fluid_Flow/ch2.ipynb
index b825a760..3ed00d28 100644
--- a/Problems_In_Fluid_Flow/ch2.ipynb
+++ b/Problems_In_Fluid_Flow/ch2.ipynb
@@ -1,6 +1,7 @@
{
"metadata": {
- "name": ""
+ "name": "",
+ "signature": "sha256:9728786ea75c57c39fe0761ee4fb63c15077dcd6bf03dc93443815257347de88"
},
"nbformat": 3,
"nbformat_minor": 0,
@@ -27,7 +28,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find pressure maintained at compressor\n",
+ "\n",
"\n",
"from scipy.optimize import fsolve\n",
"from math import *\n",
@@ -90,17 +91,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "ratio of Pw/P1\n",
- "maximum velocity in (m/s)\n",
- "maximum mass flow rate in(kg/s)\n",
- "heat taken up to maintain isothermal codition(J/s)\n",
- "crtical pressure ratio in adiabatic condition\n",
- "velocity at adiabatic condition in (m/s)\n",
- "mass flow rate at adiabatic condition in (kg/s)\n",
- "temperature of discharging gas in (Celcius)\n",
- "'''\n",
+ "\n",
"\n",
"from math import *\n",
"from numpy import *\n",
@@ -221,13 +212,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "new estimate assumed\n",
- "mass flow rate of steam through pipe\n",
- "pressure of pipe at downstream end in\n",
- "temperature of steam emerging from pipe\n",
- "'''\n",
+ "\n",
"\n",
"from scipy.optimize import fsolve \n",
"import math \n",
@@ -306,12 +291,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "pressure at nozzle throat\n",
- "diameter required at nozzle throat\n",
- "sonic velocity at throat\n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -365,7 +345,6 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find height of manometer\n",
"\n",
"import math \n",
"\n",
@@ -409,11 +388,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "both liquid phase and solid phase \n",
- "required pressure drop per unit length\n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"\n",
diff --git a/Problems_In_Fluid_Flow/ch3.ipynb b/Problems_In_Fluid_Flow/ch3.ipynb
index 092a98ed..aae6f3e2 100644
--- a/Problems_In_Fluid_Flow/ch3.ipynb
+++ b/Problems_In_Fluid_Flow/ch3.ipynb
@@ -1,6 +1,7 @@
{
"metadata": {
- "name": ""
+ "name": "",
+ "signature": "sha256:8dba2b3d7cbaa7605bb6013111bd417249fb9e6e7f076f776b644ff232eb7675"
},
"nbformat": 3,
"nbformat_minor": 0,
@@ -27,16 +28,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "fluid in boundary layer would be entirely\n",
- "reynolds \n",
- "boundary layer width\n",
- "velocity of water\n",
- "shear stress \n",
- "mean shear stress experienced\n",
- "total force experienced\n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -108,17 +100,6 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "% of surface over which turbulent boundary layer \n",
- "thickness of boundary layer \n",
- "velocity of air at mid point \n",
- "thickness of laminar boundary layer\n",
- "velocity at outer edge of laminar sublayer\n",
- "shearforce expericienced\n",
- "mean shearforce \n",
- "total drag force expericienced by the plate \n",
- "'''\n",
"\n",
"import math \n",
"\n",
@@ -204,21 +185,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "pipe flow reynolds\n",
- "Water will be in streamline motion in the pipe\n",
- "velocity gradient at the pipe wall\n",
- "Sherastress at pipe wall\n",
- "new av. fluid velocity \n",
- "thickness of laminar sublayer\n",
- "thickness of buffer layer \n",
- "percentage of pipe-s core occupied by turbulent core\n",
- "velocity where sublayer and buffer layer meet \n",
- "velocity where turbulent core and buffer layer meet\n",
- "fluid velocity \n",
- "shearstress \n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"\n",
diff --git a/Problems_In_Fluid_Flow/ch4.ipynb b/Problems_In_Fluid_Flow/ch4.ipynb
index cf855c54..5938d17b 100644
--- a/Problems_In_Fluid_Flow/ch4.ipynb
+++ b/Problems_In_Fluid_Flow/ch4.ipynb
@@ -1,6 +1,7 @@
{
"metadata": {
- "name": ""
+ "name": "",
+ "signature": "sha256:ffc24e4736ce76886d42f423c1c0ec0d6d6df9d9e5919471cf9355fdd075f7c0"
},
"nbformat": 3,
"nbformat_minor": 0,
@@ -27,17 +28,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "maximum fluid velocity \n",
- "reynold no. \n",
- "mass flow rate \n",
- "Volumetric flow rate \n",
- "maximum fluid velocity\n",
- "reynold no. \n",
- "volumetric flow rate\n",
- "mass flow rate\n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -120,11 +111,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "volumetric flow rate\n",
- "mass flow rate of chlorine gas\n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"import numpy\n",
@@ -219,12 +206,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "mass flow rate\n",
- "pressuer differnce between tapping points \n",
- "difference in water levels in manometer\n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -280,11 +262,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "diameter of orifice\n",
- "ratio of pressure drop \n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -340,12 +318,6 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "pressure drop over the float\n",
- "mass flow rate\n",
- "Volumetric flow rate\n",
- "'''\n",
"\n",
"import math \n",
"\n",
@@ -405,7 +377,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find mass of float equired \n",
+ "\n",
"\n",
"import math \n",
"\n",
diff --git a/Problems_In_Fluid_Flow/ch5.ipynb b/Problems_In_Fluid_Flow/ch5.ipynb
index 2f6c5b6c..9a1752c6 100644
--- a/Problems_In_Fluid_Flow/ch5.ipynb
+++ b/Problems_In_Fluid_Flow/ch5.ipynb
@@ -1,6 +1,7 @@
{
"metadata": {
- "name": ""
+ "name": "",
+ "signature": "sha256:f59ee9dc4c5262ffa9663e99f39b4e3b3c7c93a564a44e8c761f2c4379d0bbed"
},
"nbformat": 3,
"nbformat_minor": 0,
@@ -27,12 +28,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "volumetric flow rate\n",
- "chezy coefficient\n",
- "velocity gradient in the channel\n",
- "'''\n",
+ "\n",
"import math \n",
"\n",
"# Initialization of Variable\n",
@@ -85,7 +81,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find depth of water\n",
+ "\n",
"\n",
"from scipy.optimize import fsolve \n",
"import math \n",
@@ -134,7 +130,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find slope of channel\n",
+ "\n",
"\n",
"from scipy.optimize import fsolve \n",
"import math \n",
@@ -181,13 +177,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "maximum velocity\n",
- "maximum volumetric flow \n",
- "maximum velocity of obtained fluid \n",
- "maximum flow rate obtained\n",
- "'''\n",
+ "\n",
"\n",
"from scipy.optimize import fsolve \n",
"import math \n",
@@ -255,13 +245,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "velocity of fluid \n",
- "fluid depth over weir in (m)\n",
- "fluid depth over weir in if SI units \n",
- "base angle of the notch of weir\n",
- "'''\n",
+ "\n",
"\n",
"from scipy.optimize import fsolve \n",
"import math \n",
@@ -330,14 +314,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "alternative depth \n",
- "maximum volumetric flow\n",
- "Froude no.\n",
- "% of kinetic energy in initial system\n",
- "% of kinetic energy in final system \n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"from numpy import poly1d\n",
@@ -399,12 +376,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "alternate depths \n",
- "slode when depth is 12.9cm\n",
- "slode when depth is 45.1cm \n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"from numpy import *\n",
@@ -453,12 +425,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "critical depth\n",
- "critical velocity\n",
- "Critical volumetric flow\n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"from numpy import *\n",
@@ -522,11 +489,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "volumetric flow rate over flat topped weir over rectangular section in non uniform width\n",
- "volumetric flow rate over flat topped weir over rectangular section in uniform width\n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -577,12 +540,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "Normal depth \n",
- "Critical depth \n",
- "distance in (m) from upstream to that place\n",
- "'''\n",
+ "\n",
"\n",
"from numpy import linspace\n",
"from scipy.optimize import fsolve \n",
@@ -648,17 +606,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "critical depth \n",
- "normal depth upstream\n",
- "normal depth downstream \n",
- "conjugate depth for upstream \n",
- "conjugate depth for downstream \n",
- "distance in (m) of occurence of jump by accurate method\n",
- "distance in (m) of occurence of jump by not so accurate method\n",
- "power loss in hydraulic jump per unit width\n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"from numpy import linspace\n",
diff --git a/Problems_In_Fluid_Flow/ch6.ipynb b/Problems_In_Fluid_Flow/ch6.ipynb
index d95ae4fb..3eb6270f 100644
--- a/Problems_In_Fluid_Flow/ch6.ipynb
+++ b/Problems_In_Fluid_Flow/ch6.ipynb
@@ -1,6 +1,7 @@
{
"metadata": {
- "name": ""
+ "name": "",
+ "signature": "sha256:0f5ebffba7421842791b4539c2f380869e20570438cc6f427747cc5e01bc6228"
},
"nbformat": 3,
"nbformat_minor": 0,
@@ -27,14 +28,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "Max. height of toluene supported by atm. pressure\n",
- "reynolds no \n",
- "the maximum height above toulene \n",
- "Maximum delivery rate \n",
- "minimum smooth diameter of suction pipe\n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"from numpy import *\n",
@@ -121,11 +115,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "frequency of motor\n",
- "diametr of impeller\n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"# Initialization of Variable\n",
@@ -170,7 +160,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find Power required to pump fluid \n",
+ "\n",
"\n",
"from matplotlib.pyplot import *\n",
"import math \n",
@@ -276,7 +266,6 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find the flow rate at which H_sys takes over HeffA\n",
"\n",
"import math \n",
"from matplotlib.pyplot import *\n",
@@ -354,11 +343,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "time t when the acceleration will be maximum\n",
- "Maximum frequency of oscillation\n",
- "'''\n",
+ "\n",
"\n",
"import math\n",
"from numpy import *\n",
@@ -438,12 +423,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "mass of air required to lift the sulphuric acid tank\n",
- "work done is magnitude of value in kg\n",
- "The mass of air required \n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"\n",
diff --git a/Problems_In_Fluid_Flow/ch7.ipynb b/Problems_In_Fluid_Flow/ch7.ipynb
index 2c61cecf..1cf884f4 100644
--- a/Problems_In_Fluid_Flow/ch7.ipynb
+++ b/Problems_In_Fluid_Flow/ch7.ipynb
@@ -1,6 +1,7 @@
{
"metadata": {
- "name": ""
+ "name": "",
+ "signature": "sha256:2221589d3a230bd5e1c3d095a5ede0c1e2f30a613887d893f353723197c86dd5"
},
"nbformat": 3,
"nbformat_minor": 0,
@@ -28,11 +29,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "average particle diameter\n",
- "surface area per gram of cement\n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -88,7 +85,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find initial volumetric flow rate\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -142,7 +139,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find pressure drop in terms of (cm of H20)\n",
+ "\n",
"\n",
"import math \n",
"\n",
diff --git a/Problems_In_Fluid_Flow/ch8.ipynb b/Problems_In_Fluid_Flow/ch8.ipynb
index 97b6a74a..09ab4234 100644
--- a/Problems_In_Fluid_Flow/ch8.ipynb
+++ b/Problems_In_Fluid_Flow/ch8.ipynb
@@ -1,6 +1,7 @@
{
"metadata": {
- "name": ""
+ "name": "",
+ "signature": "sha256:00c3b1a67f83ca35bc811927488fe197c5bf1eb682a1e6ea0657f01c6f0d77b3"
},
"nbformat": 3,
"nbformat_minor": 0,
@@ -27,13 +28,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "pressure drop at t = 30 min\n",
- "the thickness of filtercake formed\n",
- "thickness of cake required\n",
- "average particle diameter\n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"from numpy import *\n",
@@ -103,13 +98,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "time at which the required pressure drop have taken place\n",
- "volume of filterate \n",
- "the time required to collect 750dm**3\n",
- "time required to pass 10dm**3 volume \n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"from numpy import *\n",
@@ -175,7 +164,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find the thickness of filter \n",
+ "\n",
"\n",
"import math \n",
"from numpy import *\n",
@@ -239,11 +228,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "Volume at P = 90kPa \n",
- "Volume at p = 45kPa \n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"from numpy import *\n",
@@ -319,12 +304,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "thickness of filter cake \n",
- "rate at which wet cake will be scrapped\n",
- "rate of which slurry is treated\n",
- "'''\n",
+ "\n",
"\n",
"from numpy import *\n",
"import math \n",
@@ -397,11 +377,6 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "time taken to collect sucrose crystal\n",
- "volume of liquid separated\n",
- "'''\n",
"\n",
"\n",
"import math \n",
diff --git a/Problems_In_Fluid_Flow/ch9.ipynb b/Problems_In_Fluid_Flow/ch9.ipynb
index 9644490f..8a82285f 100644
--- a/Problems_In_Fluid_Flow/ch9.ipynb
+++ b/Problems_In_Fluid_Flow/ch9.ipynb
@@ -1,6 +1,7 @@
{
"metadata": {
- "name": ""
+ "name": "",
+ "signature": "sha256:f2115f2ad7692dfe801ea214554c915af4da1fd1ef8995d6587f66bc81d26a08"
},
"nbformat": 3,
"nbformat_minor": 0,
@@ -27,11 +28,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "The drag force on sphere\n",
- "The drag force on cube\n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -90,13 +87,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "Drag force in N\n",
- "The drag coefficient\n",
- "The lift force\n",
- "The coefficient of lift\n",
- "'''\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -155,7 +146,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find Diameter of sphere\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -198,7 +189,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find The terminal velocity\n",
+ "\n",
"\n",
"import math \n",
"\n",
@@ -242,11 +233,6 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "'''\n",
- "find\n",
- "settling occurs in stoke-s law range\n",
- "settling velocity\n",
- "'''\n",
"\n",
"import math \n",
"\n",
@@ -313,7 +299,7 @@
"cell_type": "code",
"collapsed": false,
"input": [
- "# find Time taken by particle to reach 80% of its velocity\n",
+ "\n",
"\n",
"import math \n",
"from numpy import linspace\n",
generated by cgit (git 2.34.1) at 2025-06-22 04:42:32 +0000