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authordebashisdeb2014-06-21 00:52:25 +0530
committerdebashisdeb2014-06-21 00:52:25 +0530
commit7c756fcc12d21693818e58f6936cab5b7c112868 (patch)
tree009cb02ec85f4a75ac7b64239751f15361df2bfe /Fundamentals_of_Heat_and_Mass_Transfer
parent83c1bfceb1b681b4bb7253b47491be2d8b2014a1 (diff)
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Removed Problem Statements Completely
Diffstat (limited to 'Fundamentals_of_Heat_and_Mass_Transfer')
-rw-r--r--Fundamentals_of_Heat_and_Mass_Transfer/Chapter_1.ipynb6
-rw-r--r--Fundamentals_of_Heat_and_Mass_Transfer/Chapter_12.ipynb31
-rw-r--r--Fundamentals_of_Heat_and_Mass_Transfer/Chapter_13.ipynb12
-rw-r--r--Fundamentals_of_Heat_and_Mass_Transfer/Chapter_14.ipynb11
-rw-r--r--Fundamentals_of_Heat_and_Mass_Transfer/Chapter_2.ipynb5
5 files changed, 11 insertions, 54 deletions
diff --git a/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_1.ipynb b/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_1.ipynb
index 7c755d06..91987df5 100644
--- a/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_1.ipynb
+++ b/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_1.ipynb
@@ -1,7 +1,7 @@
{
"metadata": {
"name": "",
- "signature": "sha256:711f56c3e3096fd85ba076900a2d5d1fac9fbc28d9c6a8c278c36feee7744bc6"
+ "signature": "sha256:2ba7e707b3be5d9c0c54b9bb8556d6e5f96b70b9fbb7f8e292b6019cfe481029"
},
"nbformat": 3,
"nbformat_minor": 0,
@@ -125,7 +125,6 @@
"input": [
"\n",
"\n",
- "# Find Velocity of Coolant Fluid\n",
"import math\n",
"Ts = 56.4+273.15; \t\t\t\t\t#[K] - Surface Temperature of Steam\n",
"Tsurr = 25+273.15; \t\t\t\t\t#[K] - Temperature of Surroundings\n",
@@ -184,7 +183,6 @@
"input": [
"\n",
"\n",
- "# Find Skin Temperature & Heat loss rate\n",
"import math\n",
"A=1.8;\t \t\t\t\t\t\t\t\t# [m^2] Area for Heat transfer i.e. both surfaces\n",
"Ti = 35+273.; \t \t\t\t\t\t\t\t#[K] - Inside Surface Temperature of Body\n",
@@ -260,8 +258,6 @@
"input": [
"\n",
"%pylab inline\n",
- "# (a) Curie Temperature for h = 15 W/m^2\n",
- "# (b) Value of h for cure temp = 50 deg C\n",
"\n",
"import math\n",
"import numpy\n",
diff --git a/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_12.ipynb b/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_12.ipynb
index 9072d911..0458d8c6 100644
--- a/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_12.ipynb
+++ b/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_12.ipynb
@@ -1,7 +1,7 @@
{
"metadata": {
"name": "",
- "signature": "sha256:304ae148e504c8ed241176c62ed1b8e5847971fcae322bbded93788c7a0511f7"
+ "signature": "sha256:3f70bd8e66ed069013ea8da0a0db103f64597532e63478b727d2e9fd79a10d32"
},
"nbformat": 3,
"nbformat_minor": 0,
@@ -31,9 +31,7 @@
"\n",
"\n",
"import math\n",
- "# a) Intensity of emission in each of the three directions\n",
- "# b) Solid angles subtended by the three surfaces\n",
- "# c) Rate at which radiation is intercepted by the three surfaces\n",
+ "\n",
"\n",
"A1 = .001\t\t;#[m^2] Area of emitter\n",
"In = 7000\t\t;#[W/m^2.Sr] Intensity of radiation in normal direction\n",
@@ -172,10 +170,7 @@
"\n",
"\n",
"import math\n",
- "# Spectral Emissive Power of a small aperture on the enclosure\n",
- "# wavelengths below which and above which 10% of the radiation is concentrated\n",
- "# Spectral emissive power and wavelength associated with maximum emission\n",
- "# Irradiation on a small object inside the enclosure\n",
+ "\n",
"\n",
"T = 2000.\t\t\t\t\t\t\t\t;#[K] temperature of surface\n",
"stfncnstt = 5.67*math.pow(10,-8)\t\t;#[W/m^2.K^4] Stefan-Boltzmann constant\n",
@@ -245,7 +240,7 @@
"import math\n",
"import scipy\n",
"from scipy import integrate\n",
- "# Rate of emission per unit area over all directions between 0 degC and 60 degC and over all wavelengths between wavelengths 2 and 4 micro-m\n",
+ "\n",
"\n",
"T = 1500.\t\t\t\t\t\t\t\t;#[K] temperature of surface\n",
"stfncnstt = 5.67*math.pow(10,-8)\t\t;#[W/m^2.K^4] Stefan-Boltzmann constant\n",
@@ -298,9 +293,7 @@
"input": [
"\n",
"import math\n",
- "# Total hemispherical emissivity\n",
- "# Total emissive Power\n",
- "# Wavelength at which spectral emissive power will be maximum\n",
+ "\n",
"\n",
"T = 1600.\t\t\t\t\t\t\t\t;#[K] temperature of surface\n",
"wl1 = 2 \t\t\t\t\t\t;#[micro-m] wavelength 1\n",
@@ -381,8 +374,6 @@
"import math\n",
"import scipy\n",
"from scipy import integrate\n",
- "# Spectral , Normal emissivity en and spectral hemispherical emissivity e\n",
- "# Spectral normal intensity In and Spectral emissive power\n",
"\n",
"T = 2000.\t\t\t\t\t\t\t\t;#[K] temperature of surface\n",
"wl = 1 \t\t\t\t\t\t;#[micro-m] wavelength \n",
@@ -459,9 +450,7 @@
"import matplotlib\n",
"from matplotlib import pyplot\n",
"%pylab inline\n",
- "# Spectral distribution of reflectivity\n",
- "# Total, hemispherical absorptivity\n",
- "# Nature of surface temperature change\n",
+ "\n",
"\n",
"T = 500.\t\t\t\t\t\t\t\t;#[K] temperature of surface\n",
"e = .8;\n",
@@ -535,7 +524,6 @@
"input": [
"\n",
"import math\n",
- "# Total emissivity of cover glass to solar radiation\n",
"\n",
"T = 5800.\t\t\t\t\t\t\t\t;#[K] temperature of surface\n",
"e = .8;\n",
@@ -582,9 +570,6 @@
"\n",
"\n",
"import math\n",
- "# Total hemispherical emissivity of fire brick wall\n",
- "# Total emissive power of brick wall\n",
- "# Absorptivity of the wall to irradiation from coals\n",
"\n",
"Ts = 500.\t\t\t\t\t\t\t;#[K] temperature of brick surface\n",
"Tc = 2000. \t\t\t\t;#[K] Temperature of coal exposed\n",
@@ -650,8 +635,6 @@
"input": [
"\n",
"import math\n",
- "# Total hemispherical absorptivity and emissivity of sphere for initial condition\n",
- "# values of absoprtivity and emissivity after sphere has been in furnace a long time\n",
"\n",
"Ts = 300.;\t\t\t\t\t\t\t#[K] temperature of surface\n",
"Tf = 1200; \t\t\t\t#[K] Temperature of Furnace\n",
@@ -714,8 +697,6 @@
"\n",
"\n",
"import math\n",
- "# Useful heat removal rate per unit area\n",
- "# Efficiency of the collector\n",
"\n",
"Ts = 120+273.;\t\t\t\t\t\t\t#[K] temperature of surface\n",
"Gs = 750; \t\t\t\t#[W/m^2] Solar irradiation\n",
diff --git a/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_13.ipynb b/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_13.ipynb
index 908362f2..c86d6c34 100644
--- a/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_13.ipynb
+++ b/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_13.ipynb
@@ -1,7 +1,7 @@
{
"metadata": {
"name": "",
- "signature": "sha256:9fc173b0d74248d2dec7a4473e85a2d5663ed8938149f46e30b414437d81486f"
+ "signature": "sha256:0be077d15f32f0d1b8e0a08fdc77fccd31f63a0aa5b7d4531be27e5ff004495f"
},
"nbformat": 3,
"nbformat_minor": 0,
@@ -30,7 +30,6 @@
"input": [
"\n",
"\n",
- "# View Factors of known surface Geometries\n",
"import math\n",
"# (1) Sphere within Cube\n",
"F12a = 1 \t\t;#By Inspection\n",
@@ -93,7 +92,6 @@
"import math\n",
"import numpy\n",
"from numpy import linalg\n",
- "# Net rate of Heat transfer to the absorber surface\n",
"\n",
"L = 10 \t;#[m] Collector length = Heater Length\n",
"T2 = 600 \t;#[K] Temperature of curved surface\n",
@@ -164,7 +162,6 @@
"\n",
"\n",
"import math\n",
- "# Power required to maintain prescribed temperatures\n",
"\n",
"T3 = 300. \t\t\t\t\t;#[K] Temperature of surrounding\n",
"L = .15 \t\t\t\t\t\t;#[m] Furnace Length\n",
@@ -216,8 +213,6 @@
"\n",
"\n",
"import math\n",
- "# Heat gain by the fluid passing through the inner tube\n",
- "# Percentage change in heat gain with radiation shield inserted midway between inner and outer tubes\n",
"\n",
"T2 = 300 \t;#[K] Temperature of inner surface\n",
"D2 = .05 \t;#[m] Diameter of Inner Surface\n",
@@ -270,8 +265,6 @@
"input": [
"\n",
"import math\n",
- "# Rate at which heat must be supplied per unit length of duct\n",
- "# Temperature of the insulated surface\n",
"\n",
"T2 = 500 \t\t\t\t\t;#[K] Temperature of Painted surface\n",
"e2 = .4 \t \t\t\t\t;# emissivity of Painted Surface\n",
@@ -332,8 +325,7 @@
"\n",
"\n",
"import math\n",
- "# Rate at which heat must be supplied \n",
- "# Temperature of the insulated surface\n",
+ "\n",
"\n",
"T1 = 1000. \t\t\t\t;#[K] Temperature of Heated Surface\n",
"e1 = .8 \t\t\t\t\t;# emissivity of Heated Surface\n",
diff --git a/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_14.ipynb b/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_14.ipynb
index 6d3fd60d..b13d25b6 100644
--- a/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_14.ipynb
+++ b/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_14.ipynb
@@ -1,7 +1,7 @@
{
"metadata": {
"name": "",
- "signature": "sha256:23004d8fb27d32537f04ac072677553656b3c1c397997f3010334189894b890f"
+ "signature": "sha256:c20c5ffc14398659aab9089e6b803cb3218676cd974382b644456d53b86a097c"
},
"nbformat": 3,
"nbformat_minor": 0,
@@ -31,7 +31,6 @@
"\n",
"\n",
"import math\n",
- "# Molar and mass fluxes of hydrogen and the relative values of the mass and thermal diffusivities for the three cases\n",
"\n",
"T = 293. \t \t\t\t\t;#[K] Temperature\n",
"Ma = 2 \t\t\t\t\t;#[kg/kmol] Molecular Mass\n",
@@ -139,7 +138,6 @@
"from numpy import linalg\n",
"import matplotlib\n",
"from matplotlib import pyplot\n",
- "# Evaporation rate through a single pore\n",
"\n",
"T = 298 \t\t\t;#[K] Temperature\n",
"D = 10*math.pow(10,-6) \t;#[m]\n",
@@ -199,7 +197,6 @@
"#Variable Initialization\n",
"\n",
"import math\n",
- "# Rate of water vapor molar diffusive ttansfer through the trough wall\n",
"\n",
"D = .005 \t\t\t\t\t\t;#[m] Diameter\n",
"L = 50*math.pow(10,-6); \t#[m] Length\n",
@@ -245,7 +242,6 @@
"#Variable Initialization\n",
"\n",
"import math\n",
- "# The rate of change of the helium pressure dp/dt\n",
"\n",
"D = .2 \t\t\t;#[m] Diameter\n",
"L = 2*math.pow(10,-3) ;#[m] Thickness\n",
@@ -293,9 +289,6 @@
"#Variable Initialization\n",
"\n",
"import math\n",
- "# The Hydrogen mass diffusive flux nA (kg/s.m^2)\n",
- "#A -> Hydrogen\n",
- "#B -> Plastic\n",
"\n",
"Dab = 8.7*math.pow(10,-8) ;#[m^2/s] Diffusion coefficient\n",
"Sab = 1.5*math.pow(10,-3) ;#[kmol/m^3.bar] Solubility\n",
@@ -345,7 +338,6 @@
"#Variable Initialization\n",
"\n",
"import math\n",
- "# Maximum Thickness of a bacteria laden biofilm, that may be siccessfully treated\n",
"\n",
"Dab = 2*math.pow(10,-12) \t;#[m^2/s] Diffusion coefficient\n",
"Ca0 = 4*math.pow(10,-3) \t\t;#[kmol/m^3] Fixed Concentration of medication\n",
@@ -390,7 +382,6 @@
"#Variable Initialization\n",
"\n",
"import math\n",
- "# Total dosage of medicine delivered to the patient over a one-week time period, sensivity of the dosage to the mass duffusivity of the patch and skin\n",
"\n",
"Dap = .1*math.pow(10,-12) ;#[m^2/s] Diffusion coefficient of medication with patch\n",
"Das = .2*math.pow(10,-12) ;#[m^2/s] Diffusion coefficient of medication with skin\n",
diff --git a/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_2.ipynb b/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_2.ipynb
index 0de7a462..d440a2d3 100644
--- a/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_2.ipynb
+++ b/Fundamentals_of_Heat_and_Mass_Transfer/Chapter_2.ipynb
@@ -1,7 +1,7 @@
{
"metadata": {
"name": "",
- "signature": "sha256:9a142a6e8cf26110d3ff9748fc8583daf04a172f1232dcfc8ee5e1fe6a9f5ec3"
+ "signature": "sha256:4b81d2c2d1afd02d772e0a94bc27f4f0abc2b4c7049b86921017b2dd7bb1c1b3"
},
"nbformat": 3,
"nbformat_minor": 0,
@@ -33,9 +33,6 @@
"def alpha(p, Cp, k):\n",
" a=k/(p*Cp); #[m^2/s]\n",
" return a;\n",
- "#(a) Pure Aluminium at 300K\n",
- "# From Appendix A, Table A.1\n",
- "#calculations and results\n",
"\n",
"p = 2702.; \t\t#[Kg/m^3] - Density Of Material \n",
"Cp = 903.; \t\t\t#[J/kg.K] - Specific heat of Material\n",