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author | debashisdeb | 2014-06-21 00:52:25 +0530 |
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committer | debashisdeb | 2014-06-21 00:52:25 +0530 |
commit | 7c756fcc12d21693818e58f6936cab5b7c112868 (patch) | |
tree | 009cb02ec85f4a75ac7b64239751f15361df2bfe /Fundamentals_of_Heat_and_Mass_Transfer | |
parent | 83c1bfceb1b681b4bb7253b47491be2d8b2014a1 (diff) | |
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Removed Problem Statements Completely
Diffstat (limited to 'Fundamentals_of_Heat_and_Mass_Transfer')
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", |